Platinum-alkali/alkaline-earth catalyst formulations for hydrogen generation

Abstract

A method and catalysts and fuel processing apparatus for producing a hydrogen-rich gas, such as a hydrogen-rich syngas are disclosed. According to the method a CO-containing gas, such as a syngas, contacts a water gas shift catalyst in the presence of water, preferably at a temperature of less than about 450° C. to produce a hydrogen-rich gas, such as a hydrogen-rich syngas. Also disclosed is a water gas shift catalyst comprising:

Description

BACKGROUND OF THE INVENTION

[0002] 1. Field of the Invention

[0003] This invention relates to methods and catalysts to generate a hydrogen-rich gas from gas mixtures containing carbon monoxide and water, such as water-containing syngas mixtures. More particularly, the invention includes methods using platinum-based catalysts which contain alkali or alkaline-earth metals. The catalysts may be supported on a variety of catalyst support materials. Catalysts of the invention exhibit both high activity and selectivity to hydrogen generation and carbon monoxide oxidation.

[0004] 2. Discussion of the Related Art

[0005] Numerous chemical and energy-producing processes require a hydrogen-rich composition (e.g. feed stream.) A hydrogen-rich feed stream is typically combined with other reactants to carry out various processes. Nitrogen fixation processes, for example, produce ammonia by reacting feed streams containing hydrogen and nitrogen under high pressures and temperatures in the presence of a catalyst. In other processes, the hydrogen-rich feed stream should not contain components detrimental to the process. Fuel cells such as polymer electrode membrane (PEM) fuel cells, produce energy from a hydrogen-rich feed stream. PEM fuel cells typically operate with a feed stream gas inlet temperature of less than 450° C. Carbon monoxide is excluded from the feed stream to the extent possible to prevent poisoning of the electrode catalyst, which is typically a platinum-containing catalyst. See U.S. Pat. No. 6,299,995.

[0006] One route for producing a hydrogen-rich gas is hydrocarbon steam reforming. In a hydrocarbon steam reforming process steam is reacted with a hydrocarbon fuel, such as methane, iso-octane, toluene, etc., to produce hydrogen gas and carbon dioxide. The reaction, shown below with methane (CH4), is strongly endothermic; it requires a significant amount of heat.

CH4+2H2O→4H2+CO2

[0007] In the petrochemical industry, hydrocarbon steam reforming of natural gas is typically performed at temperatures in excess of 900° C. Even for catalyst assisted hydrocarbon steam reforming the temperature requirement is often still above 700° C. See, for example, U.S. Pat. No. 6,303,098. Steam reforming of hydrocarbons, such as methane, using nickel- and gold-containing catalysts and temperatures greater than 450° C. is described in U.S. Pat. No. 5,997,835. The catalyzed process forms a hydrogen-rich gas, with depressed carbon formation.

[0008] One example of effective hydrocarbon steam reforming catalysts is the Sinfelt compositions which are composed of Pt, a Group 11 metal, and a Group 8-10 metal. Group 111 metals include Cu, Ag and Au while Group 8-10 metals include the other noble metals. These catalyst formulations are well known in the promotion of hydrogenation, hydrogenolysis, hydrocracking, dealkylation of aromatics, and naphtha reforming processes. See, for example, U.S. Pat. Nos. 3,567,625 and 3,953,368. The application of catalysts based on the Sinfelt model to the water gas shift (“WGS”) reaction, in particular at conditions suitable for lower temperature WGS applications such as PEM fuel cells, has not been previously reported.

[0009] Purified hydrogen-containing feed streams have also been produced by filtering the gas mixture produced by hydrocarbon steam reformation through hydrogen-permeable and hydrogen-selective membranes. See, for example, U.S. Pat. No. 6,221,117. Such approaches suffer from drawbacks due to the complexity of the system and slow flow rates through the membranes.

[0010] Another method of producing a hydrogen-rich gas such as a feed stream starts with a gas mixture containing hydrogen and carbon monoxide and with the absence of any substantial amount of water. For instance, this may be the product of reforming a hydrocarbon or an alcohol, and selectively removes the carbon monoxide from that gas mixture. The carbon monoxide can be removed by absorption of the carbon monoxide and/or by its oxidation to carbon dioxide. Such a process utilizing a ruthenium based catalyst to remove and oxidize the carbon monoxide is disclosed in U.S. Pat. No. 6,190,430.

[0011] The WGS reaction is another mechanism for producing a hydrogen-rich gas but from water (steam) and carbon monoxide. An equilibrium process, the water gas shift reaction, shown below, converts water and carbon monoxide to hydrogen and carbon dioxide, and vice versa.

H2O+COH2+CO2

[0012] Various catalysts have been developed to catalyze the WGS reaction. These catalysts are typically intended for use at temperatures greater than 450° C. and/or pressures above 1 bar. For instance, U.S. Pat. No. 5,030,440 relates to a palladium and platinum-containing catalyst formulation for catalyzing the shift reaction at 550° C. to 650° C. See also U.S. Pat. No. 5,830,425 for an iron/copper based catalyst formulation.

[0013] Catalytic conversion of water and carbon monoxide under water gas shift reaction conditions has been used to produce hydrogen-rich and carbon monoxide-poor gas mixtures. Existing WGS catalysts, however, do not exhibit sufficient activity at a given temperature to reach or even closely approach thermodynamic equilibrium concentrations of hydrogen and carbon monoxide such that the product gas may subsequently be used as a hydrogen feed stream. Specifically, existing catalyst formulations are not sufficiently active at low temperatures, that is, below about 450° C. See U.S. Pat. No. 5,030,440.

[0014] Platinum (Pt) is a well-known catalyst for both hydrocarbon steam reforming and water gas shift reactions. Under typical hydrocarbon steam reforming conditions, high temperature (above 850° C.) and high pressure (greater than 10 bar), the WGS reaction may occur post-reforming over the hydrocarbon steam reforming catalyst due to the high temperature and generally unselective catalyst compositions. See, for instance, U.S. Pat. Nos. 6,254,807; 5,368,835; 5,134,109 and 5,030,440 for a variety of catalyst compositions and reaction conditions under which the water gas shift reaction may occur post-reforming.

[0015] Metals such as cobalt (Co), ruthenium (Ru), palladium (Pd), rhodium (Rh) and nickel (Ni) have also been used as WGS catalysts but are normally too active for the selective WGS reaction and cause methanation of CO to CH4 under typical reaction conditions. In other words, the hydrogen produced by the water gas shift reaction is consumed as it reacts with the CO present in the presence of such catalysts to yield methane. This methanation reaction activity has limited the utility of metals such as Co, Ru, Pd, Rh and Ni as water gas shift catalysts.

[0016] A need exists, therefore, for a method to produce a hydrogen-rich syngas, and catalysts which are highly active and highly selective for both hydrogen generation and carbon monoxide oxidation at moderate temperatures (e.g. below about 450° C.) to provide a hydrogen-rich syngas from a gas mixture containing hydrogen and carbon monoxide.

SUMMARY OF THE INVENTION

[0017] The invention meets the need for highly active and selective catalysts for the generation of hydrogen and the oxidation of carbon monoxide and to thereby provide a hydrogen-rich gas, such as a hydrogen-rich syngas, from a gas mixture of at least carbon monoxide and water. Accordingly, the invention provides methods and catalysts for producing a hydrogen-rich gas.

[0018] The invention is, in a first general embodiment, a method for producing a hydrogen- rich gas (e.g., syngas) by contacting a CO-containing gas, such as a syngas mixture, with a water gas shift catalyst in the presence of water at a temperature of not more than 450° C. In the first general embodiment, the water gas shift catalyst comprises a) Pt, its oxides or mixtures thereof, b) at least one of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, their oxides and mixtures thereof, and c) at least one of Sc, Y, Ti, Zr, V, Nb, Ta, Cr, Mo, W, Mn, Fe, Co, Ir, Ni, Pd, Rh, La, Ce, Pr, Nd, Sm, Eu, their oxides and mixtures thereof. In another method of the first general embodiment, the water gas shift catalyst comprises Pt, its oxides or mixtures thereof, at least one of V, Zr, their oxides and mixtures thereof, and at least one of Ti, Mo, Co, their oxides and mixtures thereof. The catalyst may be supported on a carrier, for example, at least one member selected from the group consisting of alumina, zirconia, titania, ceria, magnesia, lanthania, niobia, zeolite, perovskite, silica clay, yttria, iron oxide and mixtures thereof. The method of the invention may be conducted at a temperature ranging from about 150° C. to about 450° C.

[0019] In a second general embodiment, the invention relates to the water gas shift catalysts themselves—both supported and unsupported catalysts. The inventive water gas shift catalyst comprises a) Pt, its oxides or mixtures thereof, b) at least one of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, their oxides and mixtures thereof, and c) at least one of Sc, Y, Ti, Zr, V, Nb, Ta, Cr, Mo, W, Mn, Fe, Co, Ir, Ni, Pd, Rh, La, Ce, Pr, Nd, Sm, Eu, their oxides and mixtures thereof. In another catalyst of the second general embodiment, the water gas shift catalyst comprises Pt, its oxides or mixtures thereof, at least one of V, Zr, their oxides and mixtures thereof, and at least one of Ti, Mo, Co, their oxides and mixtures thereof. The catalysts may be supported on a carrier comprising at least one member selected from the group consisting of alumina, zirconia, titania, ceria, magnesia, lanthania, niobia, yttria, iron oxide and mixtures thereof.

[0020] In a third general embodiment, the invention is directed to the aforementioned water gas shift catalysts of the second general embodiment in an apparatus for generating a hydrogen gas containing stream from a hydrocarbon or substituted hydrocarbon feed stream. The apparatus further comprises, in addition to the WGS catalyst, a fuel reformer, a water gas shift reactor, and a temperature controller.

BRIEF DESCRIPTION OF THE DRAWINGS

[0021] The patent or application file contains at least one drawing executed in color. Copies of this patent or patent application publication with color drawing(s) will be provided by the Office upon request and payment of the necessary fee.

[0022] The accompanying drawings, which are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate preferred embodiments of the invention and together with the detailed description serve to explain the principles of the invention. In the drawings:

[0023] FIGS. 1A-1C illustrate the process of producing a library test wafer;

[0024] FIGS. 2A-2C illustrate the process of producing a library test wafer;

[0025] FIGS. 3A-3I, illustrate the process of producing a library test wafer;

[0026] FIGS. 3J-3K, illustrate SpotFire plots of the CO conversion versus CO2 production for the wafer under WGS conditions at various temperatures. The legend for FIG. 3A also applies to FIGS. 3B-3I exclusively;

[0027] FIGS. 4A-4C illustrate the process of producing a library test wafer;

[0028] FIGS. 5A-5C illustrate the process of producing a library test wafer;

[0029] FIGS. 5D-5H illustrate SpotFire plots of the CO conversion versus CO2 production for the wafer under WGS conditions. The legend for FIG. 5A also applies to FIGS. 5B and 5C exclusively;

[0030] FIGS. 6A-6F, illustrate the process of producing a library test wafer;

[0031] FIGS. 6G, 6H, and 6I, illustrate SpotFire plots of the CO conversion versus CO2 production for the wafer under WGS conditions at various temperatures. The legend for FIG. 6A also applies to FIGS. 6B-6F exclusively;

[0032] FIG. 7 illustrates plots of CO concentration versus temperature for scaled-up catalyst samples under WGS conditions;

[0033] FIG. 8 illustrates plots of CO concentration versus temperature for scaled-up catalyst samples under WGS conditions;

[0034] FIG. 9 illustrates plots of CO concentration versus temperature for scaled-up catalyst samples under WGS conditions;

[0035] FIGS. 10A-10F, illustrate the compositional make-up of various exemplary library test wafers. The legend for FIGS. 10A-10C applies only to FIGS. 10A-10C. The legend for FIGS. 10D-10F applies only to FIGS. 10D-10F;

[0036] FIG. 11A illustrates a representative plot of CO conversion versus CO2 production for a prototypical library test wafer at various temperatures;

[0037] FIG. 1I B illustrates the effect of catalyst selectivity and activity versus the WGS mass balance;

[0038] FIG. 11C illustrates the effect of temperature on catalyst performance under WGS conditions; and

[0039] FIG. 12 illustrates plots of CO concentration versus temperature for scaled-up catalyst samples under WGS conditions.

DETAILED DESCRIPTION OF THE INVENTION

[0040] The invention relates to a method for producing a hydrogen-rich gas, such as a hydrogen-rich syngas. According to the method, a CO-containing gas, such as a syngas, contacts a water gas shift catalyst, in the presence of water, preferably a stoichiometric excess of water, preferably at a reaction temperature of less than about 450° C. to produce a hydrogen-rich gas, such as a hydrogen-rich syngas. The reaction pressure is preferably not more than about 10 bar. The invention also relates to a water gas shift catalyst itself and to apparatus such as water gas shift reactors and fuel processing apparatus comprising such WGS catalysts.

[0041] A water gas shift catalyst according to the invention comprises a platinum-based catalyst containing at least one alkali or alkaline-earth metal and at least a third metal. The presence of the alkali or alkaline-earth metal enhances the activity of the water gas shift catalyst at low temperature reaction conditions. Water gas shift catalysts of the invention comprise:

[0042] a) Pt, its oxides or mixtures thereof;

[0043] b) at least one of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, their oxides and mixtures thereof; and

[0044] c) at least one of Sc, Y, Ti, Zr, V, Nb, Ta, Cr, Mo, W, Mn, Fe, Co, Ir, Ni, Pd, Rh, La, Ce, Pr, Nd, Sm, Eu, their oxides and mixtures thereof.

[0045] The WGS catalysts of the invention comprise combinations of at least three metals or metalloids, selected from at least three groups a), b) and c) indicated above, in each and every possible permutation and combination, except as specifically and expressly excluded. Although particular subgroupings of preferred combinations of metals or metalloids are also presented, the present invention is not limited to the particularly recited subgroupings.

[0046] In one particularly preferred subgrouping which incorporates additional metals not listed in the above groups a), b) and c), a water gas shift catalyst according to the invention comprises Pt, its oxides or mixtures thereof; at least one of V, Zr, their oxides and mixtures thereof; and at least one of Ti, Mo, Co, their oxides and mixtures thereof. This subgrouping comprises combinations of at least three metals or metalloids, selected from the three groups described immediately above, in each and every possible permutation and combination, except as specifically and expressly excluded.

[0047] Discussion regarding the particular function of various components of catalysts and catalyst systems is provided herein solely to explain the advantage of the invention, and is not limiting as to the scope of the invention or the intended use, function, or mechanism of the various components and/or compositions disclosed and claimed. As such, any discussion of component and/or compositional function is made, without being bound by theory and by current understanding, unless and except such requirements are expressly recited in the claims. Generally, for example, and without being bound by theory, Pt, component a), has activity as a WGS catalyst. The alkali and alkaline-earth metals enhance the low temperature activity of the catalyst and provide basic sites for the adsorption of water by the catalyst. The metals of component c) may or may not themselves have activity as WGS catalysts but function in combination with Pt and the alkali and/or alkaline-earth metals to impart beneficial properties to the catalyst of the invention.

[0048] Catalysts of the invention can catalyze the WGS reaction at varying temperatures, avoid or attenuate unwanted side reactions such as methanation reactions, as well as generate a hydrogen-rich gas, such as a hydrogen-rich syngas. The composition of the WGS catalysts of the invention and their use in WGS reactions are discussed below.

[0049] 1. Definitions

[0050] Water gas shift (“WGS”) reaction: Reaction which produces hydrogen and carbon dioxide from water and carbon monoxide, and vice versa:

H2O+COH2+CO2

[0051] Generally, and unless explicitly stated to the contrary, each of the WGS catalysts of the invention can be advantageously applied both in connection with the forward reaction as shown above (i.e., for the production of H2), or alternatively, in connection with the reverse reaction as shown above (i.e., for the production of CO). As such, the various catalysts disclosed herein can be used to specifically control the ratio of H2 to CO in a gas stream.

[0052] Methanation reaction: Reaction which produces methane and water from a carbon source, such as carbon monoxide or carbon dioxide, and hydrogen:

CO+3H2→CH4+H2O

CO2+4H2→CH4+2H2O

[0053] “Syngas” (also called synthesis gas): Gaseous mixture comprising hydrogen (H2) and carbon monoxide (CO) which may also contain other gas components such as carbon dioxide (CO2), water (H2O), methane (CH4) and nitrogen (N2).

[0054] LTS: Refers to “low temperature shift” reaction conditions where the reaction temperature is less than about 250° C., preferably ranging from about 150° C. to about 250° C.

[0055] MTS: Refers to “medium temperature shift” reaction conditions where the reaction temperature ranges from about 250° C. to about 350° C.

[0056] HTS: Refers to “high temperature shift” reaction conditions where the reaction temperature is more than about 350° C. and up to about 450° C.

[0057] Hydrocarbon: Compound containing hydrogen, carbon, and optionally, oxygen.

[0058] The Periodic Table of the Elements is based on the present TUPAC convention, thus, for example, Group 1 contains the alkali metals Li, Na, K, Rb, and Cs. (See http://www.iupac.org dated May 30, 2002.) As discussed herein, the catalyst composition nomenclature uses a dash (i.e., “-”) to separate catalyst component groups where a catalyst may contain one or more of the catalyst components listed for each component group, brackets (i.e., “{ }”) are used to enclose the members of a catalyst component group, “{two of . . . }” is used if two or more members of a catalyst component group are required to be present in a catalyst composition, “blank” is used within the “{ }” to indicate the possible choice that no additional element is added, and a slash (i.e., “/”) is used to separate supported catalyst components from their support material, if any. Additionally, the elements within catalyst composition formulations include all possible oxidation states, including oxides, or salts, or mixtures thereof.

[0059] Using this shorthand nomenclature, for example, “Pt-{Rh, Ni}-{Na, K, Fe, Os}/ZrO2” would represent catalyst compositions containing Pt, one or more of Rh and Ni, and one or more of Na, K, Fe, and Os supported on ZrO2; all of the catalyst elements may be in any possible oxidation state, unless explicitly indicated otherwise. “Pt-Rh-Ni-{two of Na, K, Fe, Os}” would represent a supported or unsupported catalyst composition containing Pt, Rh, and Ni, and two or more of Na, K, Fe, and Os. “Rh-{Cu, Ag, Au}-{Na, K, blank}/TiO2” would represent catalyst compositions containing Rh, one or more of Cu, Ag, and Au, and optionally, one of Na or K supported on TiO2.

[0060] 2. WGS Catalyst

[0061] A water gas shift catalyst of the invention comprises:

[0062] a) Pt, its oxides or mixtures thereof,

[0063] b) at least one of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, their oxides and mixtures thereof; and

[0064] c) at least one of Sc, Y, Ti, Zr, V, Nb, Ta, Cr, Mo, W, Mn, Fe, Co, Ir, Ni, Pd, Rh, La, Ce, Pr, Nd, Sm, Eu, their oxides and mixtures thereof.

[0065] Another water gas shift catalyst according to the invention comprises Pt, its oxides or mixtures thereof; at least one of V, Zr, their oxides and mixtures thereof; and at least one of Ti, Mo, Co, their oxides and mixtures thereof.

[0066] Suitable carriers for supported catalysts are discussed below.

[0067] The catalyst components are typically present in a mixture of the reduced or oxide forms; typically, one of the forms will predominate in the mixture. A WGS catalyst of the invention may be prepared by mixing the metals and/or metalloids in their elemental forms or as oxides or salts to form a catalyst precursor. This catalyst precursor mixture generally undergoes a calcination and/or reductive treatment, which may be in-situ (within the reactor), prior to use as a WGS catalyst. Without being bound by theory, the catalytically active species are generally understood to be species which are in the reduced elemental state or in other possible higher oxidation states. The catalyst precursor species are believed to be substantially completely converted to the catalytically active species by the pre-use treatment. Nonetheless, the catalyst component species present after calcination and/or reduction may be a mixture of catalytically active species such as the reduced metal or other possible higher oxidation states and uncalcined or unreduced species depending on the efficiency of the calcination and/or reduction conditions.

[0068] A. Catalyst Compositions

[0069] As discussed above, one embodiment of the invention is a catalyst for catalyzing the water gas shift reaction (or its reverse reaction). According to the invention, a WGS catalyst may have the following composition:

[0070] a) Pt, its oxides or mixtures thereof;

[0071] b) at least one of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, their oxides and mixtures thereof; and

[0072] c) at least one of Sc, Y, Ti, Zr, V, Nb, Ta, Cr, Mo, W, Mn, Fe, Co, Ir, Ni, Pd, Rh, La, Ce, Pr, Nd, Sm, Eu, their oxides and mixtures thereof.

[0073] Water gas shift catalysts where component b) is at least one of Li, Na, K, their oxides, and mixtures thereof represent a preferred group of catalysts. Another preferred group of catalysts are those where component c) is Fe, its oxides or a mixture thereof. Particularly preferred catalysts are those where component b) is at least one of Li, Na, K, their oxides, and mixtures thereof, and component c) is Fe, its oxides or a mixture thereof. Specific water gas shift catalysts of the invention, using the shorthand notation discussed above, include but are not limited to:

[0074] Pt-Li-{Fe, Co, Ce};

[0075] Pt-Na-{Zr, La, Y, Ce, Mo, Fe, Co, Mn};

[0076] Pt-Na-Zr-Co;

[0077] Pt-K-{Ce, Fe, Co}/ZrO2; and

[0078] Pt-K-Ce/ZrO2.

[0079] A discussion of each of the catalyst components a), b) and c) follows.

[0080] Another water gas shift catalyst according to the invention comprises Pt, its oxides or mixtures thereof, at least one of V, Zr, their oxides and mixtures thereof, and at least one of Ti, Mo, Co, their oxides and mixtures thereof.

[0081] The amount of a given metal present in a WGS catalyst of to the invention varies depending on the water gas shift reaction conditions under which the catalyst is to operate. The amount of each metal present depends on the total weight of the catalyst component in its final state in the catalyst composition after the final catalyst preparation step (i.e., the resulting oxidation state or states) with respect to the total weight of all catalyst components plus the support material, if any. Generally, a Group 8, 9, or 10 metal may be present in an amount ranging from about 0.01 wt. % to about 10 wt. %, preferably about 0.01 wt. % to about 2 wt. %, and more preferably about 0.05 wt. % to about 0.5 wt. %. The lanthanide elements and transition metals may be present, typically, in amounts ranging from about 0.01 wt. % to about 40 wt. %, preferably about 0.1 wt. % to about 30 wt. %. The main group elements, including the alkali and alkaline-earth metals, and the metalloid elements may be present in amounts ranging, generally, from about 0.02 wt. % to about 30 wt. %, preferably about 0.04 wt. % to about 20 wt. %. The presence of a given catalyst component in the support material and the extent and type of its interaction with other catalyst components may effect the amount of a component needed to achieve the desired performance effect.

[0082] B. Catalyst Component a): Pt

[0083] A first component in a catalyst of the invention is Pt, component a). Platinum may be present in its reduced form, as an oxide, or a combination of those forms. As discussed in the Background of the Invention, Pt itself is well known to catalyze the WGS reaction.

[0084] C. Catalyst Component b): Alkali/Alkaline-earth Metals

[0085] The catalysts of the invention, containing at least one alkali (Group 1) metals and/or alkaline-earth (Group 2) metals, are not only active WGS catalysts over a broad range of temperatures, but are particularly active under LTS water gas shift conditions. The presence of the alkali and/or alkaline-earth metal basic sites within the catalyst which are believed to adsorb and activate water in the WGS reaction, resulting in better WGS performance. Particularly preferred alkali and alkaline-earth metals include Li, Na and K, with Na and K being most preferred for use in WGS catalysts of the invention. In general, Na-containing catalysts show greater activity than K-containing catalysts at LTS water gas shift conditions. Under HTS water gas shift conditions the presence of an alkali and/or alkaline-earth metal may act to moderate or slightly deactivate the catalyst. It is preferred and in fact advantageous, then, to use the catalysts of the invention under LTS and MTS water gas shift reaction conditions.

[0086] D. Catalyst Component c): “Functional” Metals or Metalloids

[0087] The WGS catalysts of the invention contain at least three metals or metalloids. In addition to components a) and b), discussed above, a WGS catalyst contains metals or metalloids which, when used in combination with Pt and an alkali and/or alkaline-earth metal, function to impart beneficial properties to the catalyst of the invention. A catalyst of the invention, then, further comprises at least one of Sc, Y, Ti, Zr, V, Nb, Ta, Cr, Mo, W, Mn, Fe, Co, Ir, Ni, Pd, Rh, La, Ce, Pr, Nd, Sm, Eu, their oxides and mixtures thereof, component c).

[0088] In a preferred embodiment of the invention, component c) of the WGS catalyst is Fe. WGS catalysts according to the invention which contain Fe have high activity under MTS conditions. Fe has an affinity for CO which enhances CO absorption by the catalyst and the catalyst's activity.

[0089] E. Functional Classification of Catalyst Components

[0090] Without limiting the scope of the invention, a discussion of the functions of the various catalyst components is offered, along with a template for composing catalyst compositions according to the invention. The following classification of catalyst components will direct one of skill in the art in the selection of various catalyst components to formulate WGS catalyst compositions according to the present invention and depending on the reaction conditions of interest.

[0091] Furthermore, according to the invention, there are several classes of catalyst components and metals which may be incorporated into a water gas shift catalyst. Hence, the various elements recited as components in any of the described embodiments (e.g., as component (c)), may be included in any various combination and permutation to achieve a catalyst composition that is coarsely or finely tuned for a specific application (e.g. including for a specific set of conditions, such as, temperature, pressure, space velocity, catalyst precursor, catalyst loading, catalyst surface area/presentation, reactant flow rates, reactant ratios, etc.). In some cases, the effect of a given component may vary with the operating temperature for the catalyst. These catalyst components may function as, for instance, activators or moderators depending upon their effect on the performance characteristics of the catalyst. For example, if greater activity is desired, an activator may be incorporated into a catalyst, or a moderator may be replaced by at least one activator or, alternatively, by at least one moderator one step further up the “activity ladder.” An “activity ladder” ranks secondary or added catalyst components, such as activators or moderators, in order of the magnitude of their respective effect on the performance of a principal catalyst constituent. Conversely, if WGS selectivity of a catalyst needs to be increased (e.g., decrease the occurrence of the competing methanation reaction), then either an activator may be removed from the catalyst or, alternatively, the current moderator may be replaced by at least one moderator one step down the “activity ladder.” The function of these catalyst components may be further described as “hard” or “soft” depending on the relative effect obtained by incorporating a given component into a catalyst. The catalyst components may be metals, metalloids, or non-metals.

[0092] For instance, typically, a WGS catalyst according to the invention suitable for use under LTS conditions employs activators and may only be minimally moderated, if at all, because activation is generally the important parameter to be considered under LTS conditions. Such LTS catalysts also may preferably employ high surface area carriers to enhance catalyst activity. Conversely, WGS catalysts used in HTS conditions may benefit from the catalyst being moderated because selectivity and methanation are parameters to be considered. Such HTS catalysts may use, for example, low surface area carriers. Accordingly, operating temperature may be considered in selecting a WGS catalyst according to the present invention for a particular operating environment.

[0093] Activators used in catalysts according to the invention, such as for example Co, are active and selective WGS-promoting metals. Pd is an example of a metal that is moderately active but not very selective and also promotes methanation. Ir has also been observed to have a slight moderating or activating function, depending on the presence of other counter metals. Other activators may include, but are not limited to, Ti, Zr, V, Mo, La, Ce, Pr and Eu. Ce may be the most active rare earth metal for activating the WGS reaction. La, Pr, Sm and Eu may also be active, particularly at lower temperatures. For HTS, Pr and Sm are preferred soft moderators enhancing selectivity without sacrificing much activity. For LTS, La and Eu may be useful activators. In general, all lanthanides, other than Ce, show comparable performance and tend to moderate rather than activate noble metal containing catalyst systems. Y is a highly selective moderator for HTS systems whereas La and Eu are active and comparable to Ce for LTS. La is only slightly moderating when doping Ce, and may therefore be used to adjust the selectivity of Ce containing catalysts.

[0094] Catalyst components that are slightly moderating and highly selective over a relatively broad temperature range (e.g., a temperature range of at least about 50° C., preferably at least about 75° C., and most preferably a temperature range of at least about 100° C.), where such temperature range is included within the overall preferred temperature ranges of up to about 450° C., include Y, Mo, Fe, Pr and Sm; these tend to be selective but not very active at low temperatures, about 250° C. The redox dopants Mo, Fe, Pr and Sm generally lose activity with increasing pre-reduction temperatures while Fe becomes moderately active on its own at high WGS reaction temperatures.

[0095] F. Supports

[0096] The support or carrier may be any support or carrier used with the catalyst which allows the water gas shift reaction to proceed. The support or carrier may be a porous, adsorptive, high surface area support with a surface area of about 25 to about 500 m2/g. The porous carrier material may be relatively inert to the conditions utilized in the WGS process, and may include carrier materials that have traditionally be utilized in hydrocarbon steam reforming processes, such as, (1) activated carbon, coke, or charcoal; (2) silica or silica gel, silicon carbide, clays, and silicates including those synthetically prepared and naturally occurring, for example, china clay, diatomaceous earth, fuller's earth, kaolin, etc.; (3) ceramics, porcelain, bauxite; (4) refractory inorganic oxides such as alumina, titanium dioxide, zirconium oxide, magnesia, etc.; (5) crystalline and amorphous aluminosilicates such as naturally occurring or synthetically prepared mordenite and/or faujasite; and, (6) combinations of these groups.

[0097] When a WGS catalyst of the invention is a supported catalyst, the support utilized may contain one or more of the metals (or metalloids) of the catalyst. The support may contain sufficient or excess amounts of the metal for the catalyst such that the catalyst may be formed by combining the other components with the support. Examples of such supports include ceria which can contribute cerium, Ce, (component c)) to a catalyst, or iron oxide which can contribute iron, Fe, (component c)). When such supports are used the amount of the catalyst component in the support typically may be far in excess of the amount of the catalyst component needed for the catalyst. Thus the support may act as both an active catalyst component and a support material for the catalyst. Alternatively, the support may have only minor amounts of a metal making up the WGS catalyst such that the catalyst may be formed by combining all desired components on the support.

[0098] Carrier screening with catalysts containing Pt as the only active noble metal revealed that a water gas shift catalyst may also be supported on a carrier comprising alumina, zirconia, titania, ceria, magnesia, lanthania, niobia, yttria and iron oxide. Perovskite, supported on the above listed carriers or unsupported, may also be utilized as a support for the inventive catalyst formulations.

[0099] Zirconia, titania and ceria may be supports for the present invention and provide high activity for the WGS reaction. Preferably, zirconia is in the monoclinic phase. Highly pure ceria was found to activate Pt in LTS conditions more than cerias doped with additives. Niobia, yttria and iron oxide carriers provide high selectivity but are also less active which is believed to be due to a lack of surface area. In addition to their use as carriers, iron, yttrium, and magnesium oxides may be utilized as primary layers on carriers such as zirconia to provide both higher surface area and low moderator concentration. Pt on magnesia carriers formulated to have high surface areas (approximately 100 m2/g) exhibit high selectivity but also exhibit activity which decreases rapidly with falling reaction temperature.

[0100] In general, alumina has been found to be an active but unselective carrier for Pt only containing WGS catalysts. However, the selectivity of gamma alumina may be improved by doping with Zr, Co, or one of the rare earth elements, such as, for example, La and Ce alone or in combination. This doping may be accomplished by addition of the oxides or other salts such as nitrates, in either liquid or solid form, to the alumina. Other possible dopants to increase the selectivity include redox dopants, such as for instance, Mo, Fe and basic dopants. Preferred is an embodiment of gamma alumina combined with Zr and/or Co which exhibits both high activity and selectivity over a broad temperature range.

[0101] High surface area aluminas, such as gamma-, delta-, or theta-alumina are preferred alumina carriers. Other alumina carriers, such as mixed silica alumina, sol-gel alumina, as well as sol-gel or co-precipitated alumina-zirconia carriers may be used. Alumina typically has a higher surface area and a higher pore volume than carriers such as zirconia and offers a price advantage over other more expensive carriers.

[0102] Examples of a WGS catalyst of the invention supported on a carrier, using the shorthand notation discussed above, include:

[0103] Pt-Na-{Zr, La, Y, Ce, Mo, Fe, Co, Mn}/Al2O3;

[0104] Pt-Na-Zr-Co/Al2O3;

[0105] Pt-Na-{Fe, Co, Ce}/ZrO2;

[0106] Pt-K-{Fe, Co, Ce}/ZrO2; and

[0107] Pt-Li-{Fe, Co, Ce}/ZrO2.

[0108] For the alumina supported catalysts, gamma alumina (γ-Al2O3) is preferred.

[0109] G. Methods of Making a WGS Catalyst

[0110] As set forth above, a WGS catalyst of the invention may be prepared by mixing the metals and/or metalloids in their elemental forms or as oxides or salts to form a catalyst precursor, which generally undergoes a calcination and/or reductive treatment. Without being bound by theory, the catalytically active species are generally understood to be species which are in the reduced elemental state or in other possible higher oxidation states.

[0111] The WGS catalysts of the invention may be prepared by any well known catalyst synthesis processes. See, for example, U.S. Pat. Nos. 6,299,995 and 6,293,979. Spray drying, precipitation, impregnation, incipient wetness, ion exchange, fluid bed coating, physical or chemical vapor deposition are just examples of several methods that may be utilized to make the present WGS catalysts. Preferred approaches, include, for instance, impregnation or incipient wetness. The catalyst may be in any suitable form, such as, pellets, granular, bed, or monolith. See also co-pending U.S. patent application Ser. No. ______, entitled “Methods For The Preparation Of Catalysts For Hydrogen Generation” to Hagemeyer et al. (Attorney Docket No. 7080-011-01), filed on the same date as the present application, for further details on methods of catalyst preparation and catalyst precursors.

[0112] The WGS catalyst of the invention may be prepared on a solid support or carrier material. Preferably, the support or carrier is, or is coated with, a high surface area material onto which the precursors of the catalyst are added by any of several different possible techniques, as set forth above and as known in the art. The catalyst of the invention may be employed in the form of pellets, or on a support, preferably a monolith, for instance a honeycomb monolith.

[0113] One preferred method of preparing the catalysts involves depositing or impregnating catalyst components onto the catalyst in a sequence such that the catalyst components are deposited onto the substrate in the order of decreasing calcination temperature, with a calcination step following each deposition step, and with Pt typically impregnated and calcined last. One exception to this preparation procedure concerns catalyst formulations which contain both Pt and an alkali metal, like Na; in such a case the Pt is impregnated and calcined next to last, with the alkali metal then added and calcined at a calcination temperature of less than about 300° C., preferably about 200° C., or more preferably about the reaction temperature of the intended function of the catalyst. Pre-reduction under, for example, H2 of the calcined Pt-containing catalyst formulation may also be beneficial to catalyst performance. High temperature, greater than about 300° C. tends to be deleterious to the performance of Na containing formulations. This procedure appears to be especially beneficial to catalysts formulated to operate at LTS and/or MTS operating conditions.

[0114] Catalyst precursor solutions are preferably composed of easily decomposable forms of the catalyst component in a sufficiently high enough concentration to permit convenient preparation. Examples of easily decomposable precursor forms include the nitrate, amine, and oxalate salts. Typically, chlorine containing precursors are avoided to prevent chlorine poisoning of the catalyst. Solutions can be aqueous or non-aqueous solutions. Exemplary non-aqueous solvents can include polar solvents, aprotic solvents, alcohols, and crown ethers, for example, tetrahydrofuran and ethanol. Concentration of the precursor solutions generally may be up to the solubility limitations of the preparation technique with consideration given to such parameters as, for example, porosity of the support, number of impregnation steps, pH of the precursor solutions, and so forth. The appropriate catalyst component precursor concentration can be readily determined by one of ordinary skill in the art of catalyst preparation.

[0115] Li—The acetate, hydroxide, nitrate and formate salts are both possible catalyst precursors for lithium.

[0116] Na—Sodium acetate, alkoxides including methoxide, propoxide, and ethoxide, bicarbonate, carbonate, citrate, formate, hydroxide, nitrate, nitrite and oxalate may be used to prepare WGS catalysts of the invention.

[0117] Mg—Water soluble magnesium precursors include the nitrate, acetate, lactate and formate salts.

[0118] K—Potassium nitrate, acetate, carbonate, hydroxide and formate are possible potassium catalyst precursors. The KOAc salt is volatile with possible potassium losses when heating up to calcination temperature.

[0119] Ca—The nitrate, acetate and hydroxide salts, preferable salts highly soluble in water, may be used to prepare catalysts of the invention.

[0120] Sc—The nitrate salt, Sc(NO3)3 may be a precursor for scandium.

[0121] Ti—Titanium precursors which may be utilized in the present invention include ammonium titanyl oxalate, (NH4)2TiO(C2O4)2, available from Aldrich, and titanium(IV) bis(ammonium lactato)dihydroxide, 50 wt % solution in water, [CH3CH(O—)CO2NH4]2Ti(OH)2, available from Aldrich. Other titanium containing precursors include Ti oxalate prepared by dissolving a Ti(IV) alkoxide, such as Ti(IV) propoxide, Ti(OCH2CH2CH3)4, (Aldrich) in 1M aqueous oxalic acid at 60° C. and stirring for a couple of hours, to produce a 0.72M clear colorless solution; TiO(acac)oxalate prepared by dissolving Ti(IV) oxide acetylacetonate, TiO(acac)2, (Aldrich) in 1.5M aqueous oxalic acid at 60° C. with stirring for a couple of hours, following by cooling to room temperature overnight to produce 1M clear yellow-brown solution; TiO(acac)2, may also be dissolved in dilute acetic acid (50:50 HOAc:H2O) at room temperature to produce a 1M clear yellow solution of TiO acac. Preferably, titanium dioxide in the anatase form is utilized as a catalyst precursor material.

[0122] V—Vanadium (IV) oxalate, a vanadium precursor, may be prepared from V2O5, (Aldrich), which is slurried in 1.5M aqueous oxalic acid on hot plate for 1 hour until it turns dark blue due to V(V) reduction to V(IV) by oxalic acid. Ammonium metavanadate(V), (NH4)VO3, (Cerac, Alfa) may be used as a precursor by dissolving it in water, preferably hot, about 80° C. water. Various polycarboxylic organic acid vanadium precursors can be prepared and used as catalyst precursors, for example, citric, maleic, malonic, and tartatic. Vanadium citrate can be prepared by reacting V2O5 with citric acid and heating to about 80° C. Ammonium vanadium(V) oxalate may be prepared by reacting (NH4)VO3 and NH4OH in room temperature water, increasing temperature to 90° C., stirring to dissolve all solids, cooling to room temperature and adding oxalic acid; this produces a clear orange solution, which is stable for about 2 days. Ammonium vanadium(V) citrate and ammonium vanadium(V) lactate are both prepared by shaking NH4VO3 in, respectively, aqueous citric acid or aqueous lactic acid, at room temperature. Diammonium vanadium(V) citrate may be prepared by dissolving, for instance, 0.25M NH4VO3 in citric acid diammonium salt (Alfa) at room temperature. An exemplary method of preparing ammonium vanadium(V) formate is to dissolve NH4VO3 (0.25M) in water at 95° C., react with 98% formic acid and NH4OH to produce the desired ammonium vanadium(V) formate.

[0123] Cr—Both the nitrate and acetate hydroxides are possible catalyst precursors for chromium.

[0124] Mn—Manganese nitrate, manganese acetate (Aldrich) and manganese formate (Alfa) are all possible catalyst precursors for manganese.

[0125] Fe—Iron (III) nitrate, Fe(NO3)3, iron(III) ammonium oxalate, (NH4)3 Fe(C2O4)3, iron(III) oxalate, Fe2(C2O4)3, and iron(II) acetate, Fe(OAc)2, are all water soluble; although the iron(III)oxalate undergoes thermal decomposition at only 100° C. Potassium iron(III) oxalate, iron(III) formate and iron(III) citrate are additional iron precursors.

[0126] Co—Both cobalt nitrate and acetate are water soluble precursor solutions. The cobalt (II) formate, Co(OOCH)2, has low solubility in cold water of about 5 g/100 ml, while cobalt (II) oxalate is soluble in aqueous NH4OH. Another possible precursor is sodium hexanitrocobaltate(III), Na3Co(NO2)6 which is water soluble, with gradual decomposition of aqueous solutions slowed by addition of small amounts of acetic acid. Hexaammine Co(III) nitrate is also soluble in hot (65° C.) water and NMe4OH. Cobalt citrate, prepared by dissolving Co(OH)2 in aqueous citric acid at 80° C. for 1 to 2 hours, is another suitable cobalt precursor.

[0127] Ni—Nickel nitrate, Ni(NO3)2, and nickel formate are both possible nickel precursors. The nickel formate may be prepared by dissolving Ni(HCO2)2 in water and adding formic acid, or by dissolving in dilute formic acid, to produce clear greenish solutions.

[0128] Cu—Copper precursors include nitrate, Cu(NO3)2, acetate, Cu(OAc)2, and formate, Cu(OOCH)2, which are increasingly less water soluble in the order presented. Ammonium hydroxide is used to solublize oxalate, Cu(C2O4)2, and Cu(NH3)4(OH)2 which is soluble in aqueous 5N NH4OH. Copper citrate and copper amine carbonate may be prepared from Cu(OH)2.

[0129] Zn—Zinc nitrate, acetate and formate are all water soluble and possible catalyst precursors. Ammonium zinc carbonate, (NH4)2Zn(OH)2CO3, prepared by reacting zinc hydroxide and ammonium carbonate for a week at room temperature, is another possible precursor for zinc.

[0130] Ge—Germanium oxalate may be prepared from amorphous Ge(IV) oxide, glycol-soluble GeO2, (Aldrich) by reaction with 1M aqueous oxalic acid at room temperature. H2GeO3 may be prepared by dissolving GeO2 in water at 80° C. and adding 3 drops of NH4OH (25%) to produce a clear, colorless H2GeO3 solution. (NMe4)2GeO3 may be prepared by dissolving 0.25 M GeO2 in 0.1 M NMe4OH. (NH4)2GeO3 may be prepared by dissolving 0.25 M GeO2 in 0.25M NH4OH.

[0131] Rb—The nitrate, acetate, carbonate and hydroxide salts may be used as catalyst precursors to prepare the WGS catalyst of the invention. Preferred are water soluble salts.

[0132] Sr—The acetate is soluble in cold water to produce a clear colorless solution.

[0133] Y—Yttrium nitrate and acetate are both possible catalyst precursors.

[0134] Zr—Zirconyl nitrate and acetate, commercially available from Aldrich, and ammonium Zr carbonate and zirconia, available from MEI, are possible precursors for zirconium in either or both the support or catalyst formulation itself.

[0135] Nb—Niobium oxalate prepared by dissolving niobium (V) ethoxide in aqueous oxalic acid at 60° C. for 12 hours is a possible catalyst precursor. Another preparative route to the oxalate is dissolving niobic acid or niobic oxide (Nb2O5) in oxalic acid at 65° C. Ammonium Nb oxalate is also a possible catalyst precursor for niobium. Dissolving niobic oxide (0.10 M Nb) in NMe4OH (0.25 M) and stirring overnight at 65° C. will produce (NMe4)2NbO6.

[0136] Mo—Molybdenum containing precursor solutions may be derived from ammonium molybdate (NH4)2MoO4 (Aldrich) dissolved in room temperature water; Mo oxalate prepared by dissolving MoO3 (Aldrich) in 1.5M aqueous oxalic acid at 60° C. overnight; and ammonium Mo oxalate prepared from (NH4)6Mo7O244H2O (Strem) dissolved in 1M aqueous oxalic acid at room temperature. (NH4)6Mo7O24.4H2O (Strem) may also be dissolved in water at room temperature to produce a stable solution of ammonium paramolybdate tetrahydrate. Molybdic acid, H2MoO4, (Alfa Aesar or Aldrich) may each be dissolved in room temperature water to produce 1M Mo containing solutions.

[0137] Ru—Ru nitrosyl nitrate, Ru(NO)(NO3)3 (Aldrich), potassium ruthenium oxide, K2RuO4.H2O, potassium perruthenate, KRuO4, ruthenium nitrosyl acetate, Ru(NO)(OAc)3, and tetrabutylammonium perruthenate, NBu4RuO4, are all possible ruthenium metal catalyst precursors. NMe4Ru(NO)(OH)4 solution can be prepared by dissolving Ru(NO)(OH)3 (0.1 M) (H. C. Starck) in NMe4OH (0.12M) at 80° C. produces a clear dark red-brown 0.1M Ru solution useful as a catalyst precursor solution.

[0138] Rh—A suitable rhodium catalyst precursor is Rh nitrate (Aldrich or Strem).

[0139] Pd—Catalyst compositions containing Pd can be prepared by using precursors like Pd nitrate, typically stabilized by dilute HNO3, and available as a 10 wt. % solution from Aldrich, or Pd(NH3)2(NO2)2 available as a 5 wt. % Pd commercial solution, stabilized by dilute NH4OH. Pd(NH3)4(NO3)2 and Pd(NH3)4(0H)2 are also available commercially.

[0140] Ag—Silver nitrate, silver nitrite, silver diammine nitrite, and silver acetate are possible silver catalyst precursors.

[0141] Cd—Cadmium nitrate is water soluble and a suitable catalyst precursor.

[0142] In—Indium formate and indium nitrate are preferred precursors for indium.

[0143] Sn—Tin oxalate produced by reacting the acetate with oxalic acid may be used as a catalyst precursor. Tin tartrate, 5 nC4H4O6, in NMe4OH at about 0.25 M Sn concentration, and tin acetate, also dissolved in NMe4OH at about 0.25 M Sn concentration, may be used as catalyst precursors.

[0144] Sb—Ammonium antimony oxalate produced by reacting the acetate with oxalic acid and ammonia is a suitable antimony precursor. Antimony oxalate, Sb2(C2O4)3, available from Pfaltz & Bauer, is a water soluble precursor. Potassium antimony oxide, KSbO3, and antimony citrate, prepared by stirring antimony(II) acetate in 1 M citric acid at room temperature, are both possible catalyst precursors.

[0145] Te—Telluric acid, Te(OH)6, may be used as a precursor for tellurium.

[0146] Cs—Cs salts including the nitrate, acetate, carbonate, and hydroxide are soluble in water and possible catalyst precursors.

[0147] Ba—Barium acetate and barium nitrate are both suitable precursors for barium catalyst components.

[0148] La—Lanthanum precursors include nitrate, La(NO3)3, acetate, La(OAc)3, and perchlorate, La(ClO4)3, all of which may be prepared as aqueous solutions.

[0149] Ce—Ce(III) and Ce(IV) solutions may be prepared from Ce(III) nitrate hexahydrate, Ce(NO3)3.6H2O, (Aldrich) and ammonium cerium(IV) nitrate, (NH4)2Ce(NO3)6, (Aldrich), respectively, by dissolution in room temperature water. Nitric acid, 5 vol. %, may be added to the Ce(III) salt to increase solubility and stability. Ce(OAc)3 (Alfa) or Ce(NO3)4 (Alfa) may also be utilized as a catalyst precursor.

[0150] Pr, Nd, Sm and Eu—The nitrate, Ln(NO3)3, or acetate, Ln(O2CCH3)3, are possible catalyst precursors for these lanthanides.

[0151] Hf—Hafnoyl chloride and nitrate are both possible precursors. Preparing the hafnoyl nitrate by dissolving Hf(acac)4 in dilute HNO3 at low heat provides a clear stable solution of hafnoyl nitrate.

[0152] Ta—Tantalum oxalate solution, Ta2O(C2O4)4, available from H. C. Starck, or prepared by dissolving Ta(OEt)5 in aqueous oxalic acid at 60° C. for 12 hours, is a possible catalyst precursor.

[0153] W—Ammonium metatungstate hydrate, (NH4)6W12O39, is water soluble and a possible tungsten catalyst precursor. H2WO4 is reacted with NH4OH and NMe4OH, respectively, to prepare (NH4)2WO4 and (NMe4)2WO4 which are both possible precursors.

[0154] Re—Rhenium oxide in H2O2, perrhenic acid, (HReO4), NaReO4 and NH4ReO4 are suitable rhenium precursors.

[0155] Ir—Hexachloroiridate acid, H2IrCl6, potassium hexacyanoiridate and potassium hexanitroiridate are all possible catalyst precursors for iridium.

[0156] Pt—Platinum containing catalyst compositions may be prepared by using any one of a number of precursor solutions, such as, Pt(NH3)4(NO3)2 (Aldrich, Alfa, Heraeus, or Strem), Pt(NH3)2(NO2)2 in nitric acid, Pt(NH3)4(OH)2 (Alfa), K2Pt(NO2)4, Pt(NO3)2, PtCl4 and H2PtCl6 (chloroplatinic acid). Pt(NH3)4(HCO3)2, Pt(NH3)4(HPO4), (NMe4)2Pt(OH)6, H2Pt(OH)6, K2Pt(OH)6, Na2Pt(OH)6 and K2Pt(CN)6 are also possible choices along with Pt oxalate salts, such as K2Pt(C2O4)2. The Pt oxalate salts may be prepared from Pt(NH3)4(OH)2 which is reacted with 1M oxalic acid solution to produce a clear, colorless solution of the desired Pt oxalate salts.

[0157] Au—Auric acid, HAuCl4, in dilute HCl at about 5% Au may be a gold precursor. Gold nitrate in 0.1 M concentration may be prepared by dissolving HAu(NO3)4 (Alfa) in concentrated nitric acid, followed by stirring at room temperature for 1 week in the dark, then diluting 1:1 with water to produce a yellow solution. It should be noted that further dilution may result in Au precipitation. More concentrated, 0.25M, for example, gold nitrate may be prepared by starting with Au(OH)3 (Alfa). NaAu(OH)4, KAu(OH)4, and NMe4Au(OH)4 may each be prepared from Au(OH)3 dissolved in bases NaOH, KOH, or NMe4OH, respectively, in base concentrations ranging from, for instance, 0.25 M or higher.

[0158] 3. Producing a Hydrogen-rich Gas, such as a Hydrogen-Rich Syngas

[0159] The invention also relates to a method for producing a hydrogen-rich gas, such as a hydrogen-rich syngas. An additional embodiment of the invention may be directed to a method of producing a CO depleted gas, such as a CO-depleted syngas.

[0160] A CO-containing gas, such as a syngas contacts a water gas shift catalyst in the presence of water according to the method of the invention. The reaction preferably may occur at a temperature of less than 450° C. to produce a hydrogen-rich gas such as a hydrogen-rich syngas.

[0161] A method of the invention may be utilized over a broad range of reaction conditions. Preferably, the method is conducted at a pressure of no more than about 75 bar, preferably at a pressure of no more than about 50 bar to produce a hydrogen-rich syngas. Even more preferred is to have the reaction occur at a pressure of no more than about 25 bar, or even no more than about 15 bar, or not more than about 10 bar. Especially preferred is to have the reaction occur at, or about atmospheric pressure. Depending on the formulation of the catalyst according to the present invention, the present method may be conducted at reactant gas temperatures ranging from less than about 250° C. to up to about 450° C. Preferably, the reaction occurs at a temperature selected from one or more temperature subranges of LTS, MTS and/or HTS as described above. Space velocities may range from about 1 hr−1 up to about 1,000,000 hr−1. Feed ratios, temperature, pressure and the desired product ratio are factors that would normally be considered by one of skill in the art to determine a desired optimum space velocity for a particular catalyst formulation.

[0162] 4. Fuel Processor Apparatus

[0163] The invention further relates to a fuel processing system for generation of a hydrogen-rich gas from a hydrocarbon or substituted hydrocarbon fuel. Such a fuel processing system would comprise, for example, a fuel reformer, a water gas shift reactor and a temperature controller.

[0164] The fuel reformer would convert a fuel reactant stream comprising a hydrocarbon or a substituted hydrocarbon fuel to a reformed product stream comprising carbon monoxide and water. The fuel reformer may typically have an inlet for receiving the reactant stream, a reaction chamber for converting the reactant stream to the product stream, and an outlet for discharging the product stream.

[0165] The fuel processor system would also comprise a water gas shift reactor for effecting a water gas shift reaction at a temperature of less than about 450° C. This water gas shift reactor may comprise an inlet for receiving a water gas shift feed stream comprising carbon monoxide and water from the product stream of the fuel reformer, a reaction chamber having a water gas shift catalyst as described herein located therein, and an outlet for discharging the resulting hydrogen-rich gas. The water gas shift catalyst would preferable be effective for generating hydrogen and carbon dioxide from the water gas shift feed stream.

[0166] The temperature controller may be adapted to maintain the temperature of the reaction chamber of the water gas shift reactor at a temperature of less than about 450° C.

[0167] 5. Industrial Applications

[0168] Syngas is used as a reactant feed in number of industrial applications, including for example, methanol synthesis, ammonia synthesis, oxoaldehyde synthesis from olefins (typically in combination with a subsequent hydrogenation to form the corresponding oxoalcohol), hydrogenations and carbonylations. Each of these various industrial applications preferably includes a certain ratio of H2 to CO in the syngas reactant stream. For methanol synthesis the ratio of H2:CO is preferably about 2:1. For oxosynthesis of oxoaldehydes from olefins, the ratio of H2:CO is preferably about 1:1. For ammonia synthesis, the ratio of H2 to N2 (e.g., supplied from air) is preferably about 3:1. For hydrogenations, syngas feed streams that have higher ratios of H2:CO are preferred (e.g., feed streams that are H2 enriched, and that are preferably substantially H2 pure feed streams). Carbonylation reactions are preferably effected using feed streams that have lower ratios of H2:CO (e.g., feed streams that are CO enriched, and that are preferably substantially CO pure feed streams).

[0169] The WGS catalysts of the present invention, and the methods disclosed herein that employ such WGS catalysts, can be applied industrially to adjust or control the relative ratio H2:CO in a feed stream for a synthesis reaction, such as methanol synthesis, ammonia synthesis, oxoaldehyde synthesis, hydrogenation reactions and carbonylation reactions. In one embodiment, for example, a syngas product stream comprising CO and H2 can be produced from a hydrocarbon by a reforming reaction in a reformer (e.g., by steam reforming of a hydrocarbon such as methanol or naphtha). The syngas product stream can then be fed (directly or indirectly after further downstream processing) as the feed stream to a WGS reactor, preferably having a temperature controller adapted to maintain the temperature of the WGS reactor at a temperature of about 450° C. or less during the WGS reaction (or at lower temperatures or temperature ranges as described herein in connection with the catalysts of the present invention). The WGS catalyst(s) employed in the WGS reactor are preferably selected from one or more of the catalysts and/or methods of the invention. The feed stream to the WGS reactor is contacted with the WGS catalyst(s) under reaction conditions effective for controlling the ratio of H2:CO in the product stream from the WGS reactor (i.e., the “shifted product stream”) to the desired ratio for the downstream reaction of interest (e.g., methanol synthesis), including to ratios described above in connection with the various reactions of industrial significance. As a non-limiting example, a syngas product stream from a methane steam reformer will typically have a H2:CO ratio of about 6:1. The WGS catalyst(s) of the present invention can be employed in a WGS reaction (in the forward direction as shown above) to further enhance the amount of H2 relative to CO, for example to more than about 10:1, for a downstream hydrogenation reaction. As another example, the ratio of H2:CO in such a syngas product stream can be reduced by using a WGS catalyst(s) of the present invention in a WGS reaction (in the reverse direction as shown above) to achieve or approach the desired 2:1 ratio for methanol synthesis. Other examples will be known to a person of skill in the art in view of the teachings of the present invention.

[0170] 6. Preparative Method for Li- and Fe-Containing Catalyst Formulations

[0171] The invention further provides a method of producing a water gas shift catalyst comprising Pt, Li and Fe, their oxides or mixtures thereof. The preparative method comprises the steps of depositing Li and Fe onto a surface, preferably a catalyst support, calcining at a calcination temperature from about 600° C. to about 900° C. and then depositing Pt onto the Li and Fe containing catalyst. More preferably the calcination temperature is from about 650° C. to about 800° C., and most preferably at a temperature of about 700° C. A further embodiment of this invention includes a step of depositing Na onto the catalyst after the calcination of Li and Fe. The Na deposition may occur simultaneous with the Pt deposition.

[0172] A person of skill in the art will understand and appreciate that with respect to each of the preferred catalyst embodiments as described in the preceding paragraphs, the particular components of each embodiment can be present in their elemental state, or in one or more oxide states, or mixtures thereof.

[0173] Although the foregoing description is directed to the preferred embodiments of the invention, it is noted that other variations and modifications will be apparent to those skilled in the art, and which may be made without departing from the spirit or scope of the invention.

EXAMPLES

[0174] General

[0175] Small quantity catalyst composition samples are generally prepared by automated liquid dispensing robots (Cavro Scientific Instruments) on flat quartz test wafers.

[0176] Generally, supported catalysts are prepared by providing a catalyst support (e.g. alumina, silica, titania, etc.) to the wafer substrate, typically as a slurry composition using a liquid-handling robot to individual regions or locations on the substrate or by wash-coating a surface of the substrate using techniques known to those of skill in the art, and drying to form dried solid support material on the substrate. Discrete regions of the support-containing substrate are then impregnated with specified compositions intended to operate as catalysts or catalyst precursors, with the compositions comprising metals (e.g. various combinations of transition metal salts). In some circumstances the compositions are delivered to the region as a mixture of different metal-containing components and in some circumstances (additionally or alternatively) repeated or repetitive impregnation steps are performed using different metal-containing precursors. The compositions are dried to form supported catalyst precursors. The supported catalyst precursors are treated by calcining and/or reducing to form active supported catalytic materials at discrete regions on the wafer substrate.

[0177] Bulk catalysts may also be prepared on the substrate. Such multi-component bulk catalysts are purchased from a commercial source and/or are prepared by precipitation or co-precipitation protocols, and then optionally treated—including mechanical pretreatment (grinding, sieving, pressing). The bulk catalysts are placed on the substrate, typically by slurry dispensing and drying, and then optionally further doped with additional metal-containing components (e.g. metal salt precursors) by impregnation and/or incipient wetness techniques to form bulk catalyst precursors, with such techniques being generally known to those of skill in the art. The bulk catalyst precursors are treated by calcining and/or reducing to form active bulk catalytic materials at discrete regions on the wafer substrate.

[0178] The catalytic materials (e.g., supported or bulk) on the substrate are tested for activity and selectivity for the WGS reaction using a scanning mass spectrometer (SMS) comprising a scanning/sniffing probe and a mass spectrometer. More details on the scanning mass spectrometer instrument and screening procedure are set forth in U.S. Pat. No. 6,248,540, in European Patent No. EP 1019947, and in European Patent Application No. EP 1186892 and corresponding U.S. application Ser. No. 09/652,489 filed Aug. 31, 2000 by Wang et al., the complete disclosure of each of which is incorporated herein in its entirety. Generally, the reaction conditions (e.g. contact time and/or space velocities, temperature, pressure, etc.) associated with the scanning mass spectrometer catalyst screening reactor are controlled such that partial conversions (i.e., non-equilibrium conversions, e.g., ranging from about 10% to about 40% conversion) are obtained in the scanning mass spectrometer, for discrimination and ranking of catalyst activities for the various catalytic materials being screened. Additionally, the reaction conditions and catalyst loadings are established such that the results scale appropriately with the reaction conditions and catalyst loadings of larger scale laboratory research reactors for WGS reactions. A limited set of tie-point experiments are performed to demonstrate the scalability of results determined using the scanning mass spectrometer to those using larger scale laboratory research reactors for WGS reactions. See, for example, Example 12 of U.S. Provisional Patent Application Serial No. 60/434,708 entitled “Platinum-Ruthenium Containing Catalyst Formulations for Hydrogen Generation” filed by Hagemeyer et al. on Dec. 20, 2002.

[0179] Preparative and Testing Procedures

[0180] The catalysts and compositions of the present invention were identified using high- throughput experimental technology, with the catalysts being prepared and tested in library format, as described generally above, and in more detail below. Specifically, such techniques were used for identifying catalyst compositions that were active and selective as WGS catalysts. As used in these examples, a “catalyst library” refers to an associated collection of candidate WGS catalysts arrayed on a wafer substrate, and having at least two, and typically three or more common metal components (including metals in the fully reduced state, or in a partially or fully oxidized state, such as metal salts), but differing from each other with respect to relative stoichiometry of the common metal components.

[0181] Depending on the library design and the scope of the investigation with respect to a particular library, multiple (i.e., two or more) libraries were typically formed on each wafer substrate. A first group of test wafers each comprised about 100 different catalyst compositions formed on a three-inch wafer substrate, typically with most catalysts being formed using at least three different metals. A second group of test wafers each comprised about 225 different catalyst compositions on a four-inch wafer substrate, again typically with most catalysts being formed using at least three different metals. Each test wafer itself typically comprised multiple libraries. Each library typically comprised binary, ternary or higher-order compositions—that is, for example, as ternary compositions that comprised at least three components (e.g., A, B, C) combined in various relative ratios to form catalytic materials having a molar stoichiometry covering a range of interest (e.g., typically ranging from about 20% to about 80% or more (e.g. to about 100% in some cases) of each component). For supported catalysts, in addition to varying component stoichiometry for the ternary compositions, relative total metal loadings were also investigated.

[0182] Typical libraries formed on the first group of (three-inch) test wafers included, for example, “five-point libraries” (e.g., twenty libraries, each having five different associated catalyst compositions), or “ten-point” libraries (e.g., ten libraries, each having ten different associated catalyst compositions), or “fifteen-point libraries” (e.g., six libraries, each having fifteen different associated catalyst compositions) or “twenty-point libraries” (e.g., five libraries, each having twenty different associated catalyst compositions). Typical libraries formed on the second group of (four-inch) test wafers included, for example, “nine-point libraries” (e.g., twenty-five libraries, each having nine different associated catalyst compositions), or “twenty-five point” libraries (e.g., nine libraries, each having twenty-five different associated catalyst compositions). Larger compositional investigations, including “fifty-point libraries” (e.g., two or more libraries on a test wafer, each having fifty associated catalyst compositions), were also investigated. Typically, the stoichiometric increments of candidate catalyst library members ranged from about 1.5% (e.g. for a “fifty-five point ternary”) to about 15% (e.g., for a “five- point” ternary). See, generally, for example, WO 00/17413 for a more detailed discussion of library design and array organization. FIGS. 10A-10F show library designs for libraries prepared on a common test wafer, as graphically represented using Library Studios (Symyx Technologies, Inc., Santa Clara, Calif.), where the libraries may vary with respect to both stoichiometry and catalyst loading. Libraries of catalytic materials that vary with respect to relative stoichiometry and/or relative catalyst loading can also be represented in a compositional table, such as is shown in the several examples of this application.

[0183] Referring to FIG. 10A, for example, the test wafer includes nine libraries, where each of the nine libraries comprise nine different ternary compositions of the same three-component system. In the nomenclature of the following examples, such a test wafer is said to include nine, nine-point-ternary (“9PT”) libraries. The library depicted in the upper right hand corner of this test wafer includes catalyst compositions comprising components A, B and XI in 9 different stoichiometries. As another example, with reference to FIG. 10B, a partial test wafer is depicted that includes a fifteen-point-ternary (“15PT”) library having catalyst compositions of Pt, Pd and Cu in fifteen various stoichiometries. Generally, the composition of each catalyst included within a library is graphically represented by an association between the relative amount (e.g., moles or weight) of individual components of the composition and the relative area shown as corresponding to that component. Hence, referring again to the fifteen different catalyst compositions depicted on the partial test wafer represented in FIG. 10B, it can be seen that each composition includes Pt (red), Pd (green) and Cu (blue), with the relative amount of Pt increasing from column 1 to column 5 (but being the same as compared between rows within a given column), with the relative amount of Pd decreasing from row 1 to row 5 (but being the same as compared between columns within a given row), and with the relative amount of Cu decreasing from a maximum value at row 5, column 1 to a minimum at, for example, row 1, column 1. FIG. 10C shows a test wafer that includes a fifty-point-ternary (“50PT”) library having catalyst compositions of Pt, Pd and Cu in fifty various stoichiometries. This test library could also include another fifty-point ternary library (not shown), for example with three different components of interest.

[0184] FIGS. 10D-10F are graphical representations of two fifty-point ternary libraries (“bis 50PT libraries”) at various stages of preparation—including a Pt-Au-Ag/CeO2 library (shown as the upper right ternary library of FIG. 10E) and a Pt-Au-Ce/ZrO2 library (shown as the lower left ternary library of FIG. 1E). Note that the Pt-Au-Ag/CeO2 library also includes binary- impregnated compositions—Pt-Au/CeO2 binary catalysts (row 2) and Pt-Ag/CeO2 (column 10). Likewise, the Pt-Au-Ce/ZrO2 library includes binary-impregnated compositions—Pt-Ce/ZrO2 (row 11) and Au-Ce/ZrO2 (column 1). Briefly, the bis 50PT libraries were prepared by depositing CeO2 and ZrO2 supports onto respective portions of the test wafer as represented graphically in FIG. 10D. The supports were deposited onto the test wafer as a slurry in a liquid media using a liquid handling robot, and the test wafer was subsequently dried to form dried supports. Thereafter, salts of Pt, Au and Ag were impregnated onto the regions of the test wafer containing the CeO2 supports in the various relative stoichiometries as represented in FIG. 10E (upper-right-hand library). Likewise, salts of Pt, Au and Ce were impregnated onto the regions of the test wafer containing the ZrO2 supports in the various relative stoichiometries as represented in FIG. 10E (lower-left-hand library). FIG. 10F is a graphical representation of the composite library design, including the relative amount of catalyst support.

[0185] Specific compositions of tested catalytic materials of the invention are detailed in the following examples for selected libraries.

[0186] Performance benchmarks and reference experiments (e.g., blanks) were also provided on each quartz catalyst test wafer as a basis for comparing the catalyst compositions of the libraries on the test wafer. The benchmark catalytic material formulations included a Pt/zirconia catalyst standard with about 3% Pt catalyst loading (by weight, relative to total weight of catalyst and support). The Pt/zirconia standard was typically synthesized by impregnating 3 μL of, for example, 1.0% or 2.5% by weight, Pt stock solution onto zirconia supports on the wafer prior to calcination and reduction pretreatment.

[0187] Typically wafers were calcined in air at a temperature ranging from 300° C. to 500° C. and/or reduced under a continuous flow of 5% hydrogen at a temperature ranging from about 200° C. to about 500° C. (e.g., 450° C.). Specific treatment protocols are described below with respect to each of the libraries of the examples.

[0188] For testing using the scanning mass spectrometer, the catalyst wafers were mounted on a wafer holder which provided movement in an XY plane. The sniffing/scanning probe of the scanning mass spectrometer moved in the Z direction (a direction normal to the XY plane of movement for the wafer holder), and approached in close proximity to the wafer to surround each independent catalyst element, deliver the feed gas and transmit the product gas stream from the catalyst surface to the quadrupole mass spectrometer. Each element was heated locally from the backside using a CO2 laser, allowing for an accessible temperature range of about 200° C. to about 600° C. The mass spectrometer monitored seven masses for hydrogen, methane, water, carbon monoxide, argon, carbon dioxide and krypton: 2, 16, 18, 28, 40, 44 and 84, respectively.

[0189] Catalyst compositions were tested at various reaction temperatures, typically including for example at about 300° C., 350° C. and/or 400° C. and additionally, usually for more active formulations, at 250° C. Particularly for LTS formulations, testing of catalyst activity at reaction temperatures starting as low as 200° C. may occur. The feed gas typically consisted of 51.6% H2, 7.4% Kr, 7.4% CO, 7.4% CO2 and 26.2% H2O. The H2, CO, CO2 and Kr internal standard are premixed in a single gas cylinder and then combined with the water feed. Treated water (18.1 mega-ohms-cm at 27.5° C.) produced by a Barnstead Nano Pure Ultra Water system was used, without degassing.

[0190] Data Processing and Analysis

[0191] Data analysis was based on mass balance plots where CO conversion was plotted versus CO2 production. The mass spectrometer signals were uncalibrated for CO and CO2 but were based on Kr-normalized mass spectrometer signals. The software package SpotFire™ (sold by SpotFire, Inc. of Somerville, Mass.) was used for data visualization.

[0192] A representative plot of CO conversion versus CO2 production for a WGS reaction is shown in FIG. 11A involving, for discussion purposes, two ternary catalyst systems—a Pt-Au- Ag/CeO2 catalyst library and a Pt-Au-Ce/ZrO2 catalyst library—as described above in connection with FIGS. 10D-10F. The catalyst compositions of these libraries were screened at four temperatures: 250° C., 300° C., 350° C. and 400° C. With reference to the schematic diagram shown in FIG. 1I B, active and highly selective WGS catalysts (e.g., Line I of FIG. 11B) will approach a line defined by the mass balance for the water-gas-shift reaction (the “WGS diagonal”) with minimal deviation, even at relatively high conversions (i.e., at CO conversions approaching the thermodynamic equilibrium conversion (point “TE” on FIG. 11B)). Highly active catalysts may begin to deviate from the WGS diagonal due to cross-over to the competing methanation reaction (point “M” on FIG. 11C). Catalyst compositions that exhibit such deviation may still, however, be useful WGS catalysts depending on the conversion level at which such deviation occurs. For example, catalysts that first deviate from the WGS diagonal at higher conversion levels (e.g., Line II of FIG. 11B) can be employed as effective WGS catalysts by reducing the overall conversion (e.g., by lowering catalyst loading or by increasing space velocity) to the operational point near the WGS diagonal. In contrast, catalysts that deviate from the WGS diagonal at low conversion levels (e.g., Line III of FIG. 11B) will be relatively less effective as WGS catalysts, since they are unselective for the WGS reaction even at low conversions. Temperature affects the thermodynamic maximum CO conversion, and can affect the point of deviation from the mass-balance WGS diagonal as well as the overall shape of the deviating trajectory, since lower temperatures will generally reduce catalytic activity. For some compositions, lower temperatures will result in a more selective catalyst, demonstrated by a WGS trajectory that more closely approximates the WGS mass-balance diagonal. (See FIG. 11C). Referring again to FIG. 11A, it can be seen that the Pt-Au-Ag/CeO2 and the Pt-Au-Ce/ZrO2 catalyst compositions are active and selective WGS catalysts at each of the screened temperatures, and particularly at lower temperatures.

[0193] Generally, the compositions on a given wafer substrate were tested together in a common experimental run using the scanning mass spectrometer and the results were considered together. In this application, candidate catalyst compositions of a particular library on the substrate (e.g., ternary or higher-order catalysts comprising three or more metal components) were considered as promising candidates for an active and selective commercial catalyst for the WGS reaction based on a comparison to the Pt/ZrO2 standard composition included on that wafer. Specifically, libraries of catalytic materials were deemed to be particularly preferred WGS catalysts if the results demonstrated that a meaningful number of catalyst compositions in that library compared favorably to the Pt/ZrO2 standard composition included on the wafer substrate with respect to catalytic performance. In this context, a meaningful number of compositions was generally considered to be at least three of the tested compositions of a given library. Also in this context, favorable comparison means that the compositions had catalytic performance that was as good as or better than the standard on that wafer, considering factors such as conversion, selectivity and catalyst loading. All catalyst compositions of a given library were in many cases positively identified as active and selective WGS catalysts even in situations where only some of the library members compared favorably to the Pt/ZrO2 standard, and other compositions within that library compared less than favorably to the Pt/ZrO2 standard. In such situations, the basis for also including members of the library that compared somewhat less favorably to the standard is that these members in fact positively catalyzed the WGS reaction (i.e., were effective as catalysts for this reaction). Additionally, it is noted that such compositions may be synthesized and/or tested under more optimally tuned conditions (e.g., synthesis conditions, treatment conditions and/or testing conditions (e.g., temperature)) than occurred during actual testing in the library format, and significantly, that the optimal conditions for the particular catalytic materials being tested may differ from the optimal conditions for the Pt/ZrO2 standard—such that the actual test conditions may have been closer to the optimal conditions for the standard than for some of the particular members. Therefore, it was specifically contemplated that optimization of synthesis, treatment and/or screening conditions, within the generally defined ranges of the invention as set forth herein, would result in even more active and selective WGS catalysts than what was demonstrated in the experiments supporting this invention. Hence, in view of the foregoing discussion, the entire range of compositions defined by each of the claimed compositions (e.g., each three-component catalytic material, or each four-component catalytic material) was demonstrated as being effective for catalyzing the WGS reaction. Further optimization is considered, with various specific advantages associated with various specific catalyst compositions, depending on the desired or required commercial application of interest. Such optimization can be achieved, for example, using techniques and instruments such as those described in U.S. Pat. No. 6,149,882, or those described in WO 01/66245 and its corresponding U.S. applications, U.S. Ser. No. 09/801,390, entitled “Parallel Flow Process Optimization Reactor” filed Mar. 7, 2001 by Bergh et al., and U.S. Ser. No. 09/801,389, entitled “Parallel Flow Reactor Having Variable Feed Composition” filed Mar. 7, 2001 by Bergh et al., each of which are incorporated herein by reference for all purposes.

[0194] Additionally, based on the results of screening of initial libraries, selective additional “focus” libraries were selectively prepared and tested to confirm the results of the initial library screening, and to further identify better performing compositions, in some cases under the same and/or different conditions. The test wafers for the focus libraries typically comprised about 225 different candidate catalyst compositions formed on a four-inch wafer substrate, with one or more libraries (e.g. associated ternary compositions A, B, C) formed on each test wafer. Again, the metal-containing components of a given library were typically combined in various relative ratios to form catalysts having stoichiometry ranging from about 0% to about 100% of each component, and for example, having stoichiometric increments of about 10% or less, typically about 2% or less (e.g., for a “fifty-six point ternary”). Focus libraries are more generally discussed, for example, in WO 00/17413. Such focus libraries were evaluated according to the protocols described above for the initial libraries.

[0195] The raw residual gas analyzer (“rga”) signal values generated by the mass spectrometer for the individual gases are uncalibrated and therefore different gases may not be directly compared. Methane data (mass 16) was also collected as a control. The signals are typically standardized by using the raw rga signal for krypton (mass 84) to remove the effect of gas flow rate variations. Thus, for each library element, the standardized signal is determined as, for example, sH2O=raw H2O/raw Kr; sCO=raw CO/raw Kr; sCO2=raw CO2/raw Kr and so forth.

[0196] Blank or inlet concentrations are determined from the average of the standardized signals for all blank library elements, i.e. library elements for which the composition contains at most only support. For example, bavg H2O=average sH2O for all blank elements in the library; bavg CO=average sCO for all blank elements in the library; and so forth.

[0197] Conversion percentages are calculated using the blank averages to estimate the input level (e.g., bavg CO) and the standardized signal (e.g., sCO) as the output for each library element of interest. Thus, for each library element, COconversion=100×(bavg CO−sCO)/bavg CO and H2Oconversion=100×(bavg H2O−sH2O)/bavg H2O.

[0198] The carbon monoxide (CO) to carbon dioxide (CO2) selectivity is estimated by dividing the amount of CO2 produced (sCO2−bavg CO2) by the amount of CO consumed (bavg CO−sCO). The CO2 and CO signals are not directly comparable because the rga signals are uncalibrated. However, an empirical conversion constant (0.6 CO2 units=1 CO unit) has been derived, based on the behavior of highly selective standard catalyst compositions. The selectivity of the highly selective standard catalyst compositions approach 100% selectivity at low conversion rates. Therefore, for each library element, estimated CO to CO2 selectivity=100×0.6×(sCO2−bavg CO2)/(bavg CO−sCO). Low CO consumption rates can produce highly variable results, and thus the reproducibility of CO2 selectivity values is maintained by artificially limiting the CO2 selectivity to a range of 0 to 140%.

[0199] The complete disclosure of all references cited herein are incorporated herein in their entireties for all purposes.

[0200] The following examples are representative of the screening of libraries that lead to identification of the particularly claimed inventions herein.

Example 1

[0201] A 4″ quartz wafer was precoated with a γ-Al2O3 (Catalox Sba-150) carrier by slurry dispensing 3 μL (1 g of γ-Al2O3 in 4 mL of ethylene glycol (“EG”)/H2O, 50:50) to each element of a 15×15 square on the wafer. The wafer was then oven-dried at 70° C. for 12 minutes.

[0202] Six internal standards were synthesized by Cavro spotting 3 μL of a Pt(NH3)2(NO2)2 (2.5% Pt) stock solution into the corresponding first row/last column positions. The wafer was impregnated with a uniform Pt layer by dispensing into columns C1 to C5 (2.5 μL per well) a stock solution of Na2Pt(OH)6 (from powder, 1% Pt) to the wafer.

[0203] Columns C6 to C15 of the wafer were then impregnated with the following ten metal-gradients respectively from top to bottom: ZrO(NO3)2, La(NO3)3, Y(NO3)3, Ce(NO3)3, H2MoO4, Fe(NO3)3, Co(NO3)2, ZrO(OAc)2, Mn(NO3)2 and KRuO4 by Cavro dispensing from the respective stock solution vials to a microtiter plate and diluted with distilled water. A replica transfer of the microtiter plate pattern to the wafer followed (2.5 μL dispense volume per well), resulting in a 10×15 point rectangle on the wafer (10 columns with metal gradients).

[0204] The wafer was dried for 3.5 hours at room temperature and then coated with base gradients (0.5M, opposing gradients) including CsOH—NaOH, LiOH—NaOH, RbOH—NaOH and KOH—NaOH separately in each of the first four columns, respectively, and NaOH in columns 5 to 15 (1M base with a gradient from bottom to top) by Cavro dispensing from the corresponding stock solution vials to the microtiter plate and diluting with distilled water. A replica transfer of the microtiter plate pattern to the wafer followed (2.5 μL dispense volume per well), resulting in a 15×15 point rectangle on the wafer (15 columns with base gradients). The wafer was dried overnight at room temperature and oven-dried for 2 minutes.

[0205] The final impregnation was a uniform dispensing (2.5 μL dispense volume per well, resulting a 10×15 point square) from a stock solution vial of Na2Pt(OH)6 (from powder, 1% Pt) to the wafer (C6-C15.) as a ternary layer.

[0206] The wafer was dried at room temperature for 4 hours and then calcined in air at 450° C. for 2 hours followed by reduction with 5% H2/N2 at 250° C. for 2 hours. Commercial catalyst was slurried into 5 positions of the first row and last column as an external standard (3 μL). See FIGS. 1A-1C.

[0207] The library was screened in a scanning mass spectrometer (“SMS”) for WGS activity with a H2/CO/CO2/H2O mixed feed at 200° C., 230° C. and 260° C.

[0208] This experiment demonstrated active and selective WGS catalyst formulations of various alkali and Pt containing formulations on the wafer.

Example 2

[0209] A 4″ 16×16 quartz wafer was pre-coated with ZrO2 (Norton ZrO2 XZ16052) carrier by slurry dispensing 3 μL (1.5 g of ZrO2 in 4 mL of EG/H2O/MEO, 32.5:30:37.5) to each element of a 15×15 square on the wafer. The wafer was then oven-dried at 70° C. for 12 minutes.

[0210] The zirconia carrier pre-coated wafer was impregnated with a 8-point Ce(NO3)3 concentration gradient (0.25M Ce stock solution) and a 7-point Fe(NO3)3 concentration gradient (0.5M Fe stock solution) by Cavro dispensing from the Ce- and Fe-nitrate stock solution vials to a microtiter plate and diluting with distilled water. A replica transfer of the microtiter plate pattern to the wafer followed (2.5 μL dispense volume per well).

[0211] The wafer was dried for 4 hours at room temperature and then coated with Na- and K-hydroxide gradients by Cavro dispensing from NaOH (1M) and KOH (1M) stock solution vials to the microtiter plate and diluting with distilled water (sodium onto the upper and potassium onto the lower part of the wafer). A replica transfer of the microtiter plate pattern to the wafer followed (2.5 μL dispense volume per well, 7 replicas of the 8-point gradient and 8 replicas of the 7-point gradient, 7×8=56 point ternaries). The wafer was dried at room temperature overnight and oven-dried for 2 minutes.

[0212] The final impregnation was a uniform dispensing (2.5 μl dispense volume per well, resulting in a 15×15 point square) from a stock solution vial of Pt(NH3)2(NO2)2 (1% Pt) to the wafer. Six internal standards were synthesized by spotting 3 μL of Pt(NH3)2(NO2)2 stock solution (2.5% Pt) into the corresponding first row/last column positions.

[0213] The wafer was dried at room temperature for 2 hours and then calcined in air at 450° C. for 2 hours followed by reduction with 5% H2/N2 at 200° C. for 2 hours. Commercial catalyst was slurried into 5 positions of the first row and last column as an external standard (3 μL). See FIGS. 2A-AC.

[0214] The library was then screened in SMS for WGS activity with a H2/CO/CO2/H2O mixed feed at 200° C., 230° C. and 260° C.

[0215] This experiment demonstrated active and selective WGS catalyst formulations of Pt, alkali and Fe or Ce containing formulations on the wafer.

Example 3

[0216] A 4″ quartz wafer was pre-coated with a ZrO2 (Norton XZ16052) carrier by slurry dispensing 3 μL (1.5 g of ZrO2 in 4 mL of EG/H2O/MEO, 32.5:30:37.5) to each element of a 15×15 square on the wafer. The wafer was then oven-dried at 70° C. for 12 minutes.

[0217] Nine internal standards were synthesized by Cavro spotting 2.5 μL of a Pt(NH3)2(NO2)2 (1% Pt) stock solution into the corresponding first row/last column positions. The wafer was impregnated with 3 metal gradients (5-point gradients) from top to bottom as follows: rows 2 through 6 with Co(NO3)2 (0.25M), rows 7 through 11 with Ru(NO)(NO3)3 (0.05M) and rows 12-16 with H2MoO4 (0.25M) by Cavro dispensing from the corresponding stock solution vials to a microtiter plate and diluted with distilled water. A replica transfer of the microtiter plate pattern to the wafer followed (2.5 μL dispense volume per well), resulting in three 5×15 point rectangles on the wafer.

[0218] The wafer was dried for 4 hours at room temperature and then coated with the following metal gradients (reverse gradients) from bottom to top to produce 5 point dopant binaries at various column/row positions on the wafer: (NH4)2Ce(NO3)6, Co(NO3)2, Ru(NO)(NO3)3, H2MoO4, Co(OAc)2, Na3Co(NO3)6, KRuO4, Ru(NO)(OAc)3, La(NO3)3, Cd(NO3)3, ZrO(NO3)2, ZrO(OAc)2, Cu(NO3)2, NH4ReO4 and Ge(OX)2 by Cavro dispensing from the respective stock solution vials to the microtiter plate and diluted with distilled water. A replica transfer of the microtiter plate to the wafer followed (2.5 μL dispense volume per well), resulting in three 5×15 point rectangles on the wafer.

[0219] The wafer was dried for 4 hours at room temperature and then coated with a uniform top layer (2.5 μL dispense volume per well) from the corresponding stock solution vials to the wafer consisting of Pt(NH3)2(NO2)2 (1% Pt) as a third layer.

[0220] The wafer was dried overnight at room temperature and then calcined in air at 350° C. for 2 hours followed by reduction with 5% H2/N2 at 300° C. for 2 hours. See FIGS. 3A-31.

[0221] The library was then screened in SMS for WGS activity with a H2/CO/CO2/H2O mixed feed at 250° C. Detailed test results, such as CO conversion, CO2 production and CH4 production at 250° C. for each of the 225 individual catalyst wells are presented in Table 1.

[0222] This experiment demonstrated that Pt—Co—Na where both Na and Co were derived from Na3Co(NO2)6 exhibited WGS activity superior to the Pt/ZrO2 standards. See FIGS. 3J-3K.

Example 4

[0223] A 4″ quartz wafer was precoated with 7 different carriers by slurry dispensing an amount of 3 μL to vertical 15 point columns on the wafer. The carrier deposition was carried out with the following carriers: CeO2, 99.5% (Alfa, 0.75 g in 4 mL of EG/H2O, 50:50); La2O3, 99.9% (Gernch, 1.5 g in 4 mL of EG/H2O/MEO, 40:30:30); ZrVOx (1 g in 4 mL of EG/H2O, 50:50); ZrO2 FZO 923 (MEI 1.5 g in 4 mL of EG/H2O/MEO, 32.5:30:37.5); TiO2 (Aerolyst 7708, P25, Degussa, 1 g in 4 mL of EG/H2O/MEO, 32.5:30:37.5); TiO2 VKR611 (BASF, 1 g in 4 mL of EG/H2O/MEO, 32.5.5:30:37.5); TiO2 XT25384 (Norton, 1 g in 4 mL of EG/H2O/MEO, 32.5.5:30:37.5) and ZrO2 XZ16052 (Norton, 1.5 g in 4 mL of EG/H2O/MEO, 32.5.5:30:37.5). After dispensing, the samples were oven-dried at 70° C. for 12 minutes, except for the dispensed ceria from Alfa which was oven-dried for 24 minutes at 70° C.

[0224] Selected carrier pre-coated columns were impregnated by Cavro with 6 metal gradients from top to bottom: Co(NO3)2, Fe(NO3)3, Ce(NO3)3, (NH4)2MoO4, Pd(NH3)2(NO2)2 and La(NO3)3 by Cavro dispensing from the corresponding stock solution vials to microtiter plate and diluting with distilled water. A replica transfer of the microtiter plate to the wafer followed (2.5 μL dispense volume per well), resulting in a 6×15 point rectangle on the wafer.

[0225] Six internal standards were synthesized by Cavro spotting of 3 μL of a Pt(NH3)2(NO2)2 (2.5% Pt) stock solution into the corresponding first row/last column positions and then the last column was coated with a uniform layer of HAu(NO3)4 (0.1M) by dispensing of 2 μL by pipette.

[0226] The non-impregnated columns were coated with 2 platinum gradients from bottom to top consisting of Pt(NH3)2(NO2)2 (1% Pt) by Cavro dispensing from the respective stock solution vials to the microtiter plate and diluting with distilled water. A replica transfer of the microtiter plate to the wafer followed (2.5 μL dispense volume per well), resulting in a 8×15 point rectangle on the wafer and dispensing 2.5 μl dispense volume per well.

[0227] The wafer was dried overnight at room temperature and then coated with a uniform layer of sodium hydroxide (NaOH, 1M) by Cavro dispensing (2.5 μL dispense volume per well) from the respective stock solution vial to water resulting in a 7×15 point rectangle on the lower part of the wafer.

[0228] The wafer was dried for 2 hours at room temperature and oven-dried for 2 minutes at 70° C. The last impregnation was a dispensing of the ternary layer to the columns with 2 Pt- gradients from bottom to top consisting of Pt(NH3)2(NO2)2 (1% Pt) by Cavro dispensing from the corresponding stock solution vial to the microtiter plate and diluting with distilled water. A replica transfer of the microtiter plate to the wafer followed (2.5 μL dispense volume per well), resulting in a 7×15 point rectangle on the wafer.

[0229] The wafer was dried at room temperature for 4 hours and then calcined in air at 500° C. for 2 hours followed by reduction with 5% H2/N2 at 500° C. for 2 hours. See FIGS. 4A-4C.

[0230] The library was then screened in SMS for WGS activity with a H2/CO/CO2/H2O mixed feed at 230° C. and 260° C. More detailed test results, such as CO conversion, CO2 production and CH4 production at 200° C. for each of the 225 individual catalyst wells are presented in Table 2.

[0231] This experiment demonstrated active and selective WGS catalyst formulations of Pt and alkali metal containing compositions on the wafer. Also the positive effect of Na post-impregnation is observed.

Example 5

[0232] A 3″ quartz wafer was coated with niobia, ceria and magnesia carriers by slurry- dispensing aqueous carrier slurries onto the wafer (4 μl slurry/well, 1 g of carrier powder slurried in 2 ml H2O for niobia and ceria; 500 mg of carrier powder slurried in 2 ml H2O for magnesia). Niobia carriers were produced by Norton, product numbers 2001250214, 2000250356, 2000250355, 2000250354 and 2000250351. Cerias came from Norton (product numbers 2001080053, 2001080052 and 2001080051) and Aldrich (product number 21,157-50. Magnesia was obtained from Aldrich (product number 24,338-8).

[0233] The carrier precoated wafer was then loaded with the same Pt gradient for each carrier in a single impregnation step by liquid dispensing 3 μl Pt(NH3)2(NO2)2 solution (5% Pt) from microtiter plate to wafer. The wafer was dried and then reduced in 5% H2/Ar at 450° C. for 2 hours. See FIGS. 5A-5C.

[0234] The reduced library was then screened in SMS for WGS activity with a H2/CO/CO2/H2O mixed feed at 250° C., 300° C., 350° C., and 400° C. Results at 250° C., 300° C., 350° C., and 400° C. are presented in FIGS. 5D-5H. This set of experiments demonstrated active and selective WGS catalyst formulations of various Pt on one of Nb oxide, Ce oxide or Mg oxide formulations on the wafer. Various Norton niobia carriers were found to be very active and selective over a broad temperature range. Norton ceria 2001080051 was found to be very selective at higher temperatures. Magnesia was less active than either of niobia or ceria but did exhibit highly selective WGS performance.

Example 6

[0235] A 4″ quartz wafer was coated with fourteen different catalyst carriers by slurry- dispensing the carrier slurries onto the wafer. The carriers were slurried in a mixture of EG/H2O/MEO at a ratio of 40:30:30. Each wafer column was coated with a different carrier, except for columns 14 and 15 which were both coated with gamma-alumina, described below:

[0236] 1) Ceria, 99.5% purity; 9 to 15 nm particle size; BET (m2/g): 55-95; Alfa 43136; dispensed onto the wafer from a slurry of 0.75 g powder slurried in 4 mL EG/H2O/MEO.

[0237] 2) Ceria, produced by the low temperature calcination of precipitated Ce hydroxide; dispensed onto the wafer from a slurry of 1.5 g powder slurried in 4 mL EG/H2O/MEO.

[0238] 3) Zirconia; 99.8% purity; BET (m2/g): greater than 90; Norton XZ16052; dispensed onto the wafer from a slurry of 1.5 g powder slurried in 4 mL EG/H2O/MEO.

[0239] 4) Zirconia; 99.8% purity; BET (m2/g): 269; Norton XZ16154; dispensed onto the wafer from a slurry of 1.5 g powder slurried in 4 mL EG/H2O/MEO.

[0240] 5) Titania; BET (m2/g): 45; Degussa Aerolyst 7708; dispensed onto the wafer from a slurry of 1.0 g powder slurried in 4 mL EG/H2O/MEO.

[0241] 6) Titania; 99% purity; BET (m2/g): 37; Norton XT25384; dispensed onto the wafer from a slurry of 1.0 g powder slurried in 4 mL EG/H2O/MEO.

[0242] 7) Niobia; 97% purity; BET (m2/g): 27; Norton 2000250355; dispensed onto the wafer from a slurry of 1.0 g powder slurried in 4 mL EG/H2O/MEO.

[0243] 8) Lanthania; 99.999% purity; Gemre-5N from Gemch Co., Ltd. (Shanghai, China); dispensed onto the wafer from a slurry of 1.5 g powder slurried in 4 mL EG/H2O/MEO.

[0244] 9) Mixed Fe—Ce—O; coprecipitated Fe and Ce oxalate; calcined at 360° C.; dispensed onto the wafer from a slurry of 1.0 g powder slurried in 4 mL EG/H2O/MEO.

[0245] 10) Mixed La—Ce—O; coprecipitated La and Ce oxalate; calcined at 760° C.; dispensed onto the wafer from a slurry of 1.0 g powder slurried in 4 mL EG/H2O/MEO.

[0246] 11) Mixed Sb3O4—SnO2 carrier from Alfa; 99.5% purity; BET (m2/g): 30-80; Sb3O4:SnO2 ratio is 10:90 by weight; dispensed onto the wafer from a slurry of 1.0 g powder slurried in 4 mL EG/H2O/MEO.

[0247] 12) Mixed Fe—Cr—Al—O; commercially available high temperature water gas shift catalyst; dispensed onto the wafer from a slurry of 1.0 powder slurried in 4 mL. EG/H2O/MEO.

[0248] 13) Fe2O3/FeOOH; BET (m2/g): 14; 50:50 physical mixture of commercial powders (Bayferrox 720N: Bayoxide E3920 from Bayer); dispensed onto the wafer from a slurry of 1.0 g powder slurried in 4 mL EG/H2O/MEO.

[0249] 14 and 15) Gamma-Al2O3; BET (m2/g): 150; Condea Catalox Sbal50; dispensed onto the wafer from a slurry of 1.0 g powder slurried in 4 mL EG/H2O/MEO.

[0250] In all cases, except for carrier 1, the slurries were applied in 3 μl/well; carrier 1 was deposited as two aliquots of 3 μl/well. The wafer was then dried at 70° C. for 10 minutes.

[0251] Columns 14 and 15 were coated with 2.5 μl/well of zirconyl nitrate (0.25 M) and lanthanum nitrate (0.25 M), respectively, then dried for 10 minutes at 70° C. The first 13 columns of the carrier coated wafer were then loaded with a 15 point Pt gradient by liquid dispensing of 3 μl Pt(NH3)2(NO2)2 solution (1% Pt) from microtiter plate to wafer. The wafer was dried at 70° C. for 10 minutes. Columns 14 and 15 were then loaded with a 15 point Pt gradient by liquid dispensing of 3 μl Pt(NH3)2(NO2)2 solution (1% Pt) from microtiter plate to wafer. The wafer was dried at 70° C. for 10 minutes, calcined in air at 350° C. for 2 hours, then reduced in 5% H2/Ar at 450° C. for 2 hours. Six internal standards were synthesized by spotting 3 μl Pt(NH3)2(NO2)2 solution (1.0% Pt) into the corresponding first row/last column positions. See FIGS. 6A-6F.

[0252] The reduced library was then screened in SMS for WGS activity with a H2/CO/CO2/H2O mixed feed at 250° C. and 300° C. The CO conversion versus CO2 production results at 250° C. and 300° C. are presented in FIGS. 6G, 6H, and 61. More detailed test results, such as, CO conversion, CO2 production and CH4 production at 250° C. and 300° C. for each of the 225 individual catalyst wells on the test wafer are presented in Table 3.

[0253] This set of experiments demonstrated active and selective WGS catalyst formulations of various Pt on various of the oxide carrier formulations on the wafer.

Example 7

[0254] Scale-up catalyst samples were prepared by using incipient wetness impregnation of 0.75 grams of ZrO2 support (Norton, 80-120 mesh) which had been weighed into a 10-dram vial. Aqueous metal precursor salt solutions were then added in the order: Co, Mo, or V, Pt, and then K. The precursor salt solutions were tetraammineplatinum (II) hydroxide (9.09% Pt (w/w)), cobalt (II) nitrate (11.0M), molydbic acid (1.0M), vanadium citrate (1.0M), and potassium hydroxide (13.92% K). All reagents were nominally research grade from Aldrich, Strem, or Alfa. Following each metal addition, the catalysts were dried at 80° C. overnight and then calcined in air as follows:

After Pt addition      300° C. for 3 hours
After Co addition      450° C. for 3 hours
After Mo or V addition 350° C. for 3 hours

[0255] Following K addition, the catalysts were calcined at 300° C. for 3 hours, then the catalysts were reduced in-situ at 300° C. for 3 hours in a 10% H2/N2 feed.

[0256] Catalyst Testing Conditions

[0257] Catalysts were tested in a fixed bed reactor. Approximately 0.15 g of catalyst was weighed and mixed with an equivalent mass of SiC. The mixture was loaded into a reactor and heated to reaction temperature. Reaction gases were delivered via mass flow controllers (Brooks) with water introduced with a metering pump (Quizix). The composition of the reaction mixture was as follows: H2 50%, CO 10%, CO2 10%, and H2O 30%. The reactant mixture was passed through a pre-heater before contacting the catalyst bed. Following reaction, the product gases were analyzed using a micro gas chromatograph (Varian Instruments, or Shimadzu). Compositional data on the performance diagram (FIG. 7) is on a dry basis with water removed. Testing Results

[0258] FIG. 7 shows the CO composition in the product stream following the scale-up testing at a gas hour space velocity of 50,000 h−1.

TABLE 4
Catalyst Compositions (mass ratio)
Row	Col	ZrO2	Co	Water	Pt	K	Mo	V
1	1	0.91	0.005	0	0.06	0.025	0	0
1	2	0.885	0.005	0	0.06	0.05	0	0
1	3	0.91	0	0	0.06	0.025	0.005	0
1	4	0.885	0	0	0.06	0.05	0.005	0
1	5	0.905	0	0	0.06	0.025	0	0.01
1	6	0.88	0	0	0.06	0.05	0	0.01
2	1	0.905	0.01	0	0.06	0.025	0	0
2	2	0.88	0.01	0	0.06	0.05	0	0
2	3	0.905	0	0	0.06	0.025	0.01	0
2	4	0.88	0	0	0.06	0.05	0.01	0
2	5	0.895	0	0	0.06	0.025	0	0.02
2	6	0.87	0	0	0.06	0.05	0	0.02
3	1	0.9	0.015	0	0.06	0.025	0	0
3	2	0.875	0.015	0	0.06	0.05	0	0
3	3	0.9	0	0	0.06	0.025	0.015	0
3	4	0.875	0	0	0.06	0.05	0.015	0
3	5	0.885	0	0	0.06	0.025	0	0.03
3	6	0.86	0	0	0.06	0.05	0	0.03
4	1	0.895	0.02	0	0.06	0.025	0	0
4	2	0.87	0.02	0	0.06	0.05	0	0
4	3	0.895	0	0	0.06	0.025	0.02	0
4	4	0.87	0	0	0.06	0.05	0.02	0
4	5	0.875	0	0	0.06	0.025	0	0.04
4	6	0.85	0	0	0.06	0.05	0	0.04

Example 8

[0259] Scale-up catalyst samples were prepared by using incipient wetness impregnation of 0.75 grams of ZrO2 support (Norton, 80-120 mesh) which had been weighed into a 10-dram vial. Aqueous metal precursor salt solutions were then added in the order: Co, Mo, or V, Pt, and then Li. The precursor salt solutions were tetraammineplatinum (II) hydroxide (9.09% Pt (w/w)), cobalt (II) nitrate (1.0M), molydbic acid (1.0M), vanadium citrate (1.0M), and lithium hydroxide monohydrate (2.5M). All reagents were nominally research grade from Aldrich, Strem, or Alfa. Following each metal addition, the catalysts were dried at 80° C. overnight and then calcined in air as follows:

After Pt addition       300° C. for 3 hours
After Co addition       450° C. for 3 hours
After Mo, or V addition 350° C. for 3 hours
After Li addition       300° C. for 3 hours.

[0260] Following final addition, the catalysts were reduced in-situ at 300° C. for 3 hours in a 10% H2/N2 feed.

[0261] Catalyst Testing Conditions

[0262] Catalysts were tested in a fixed bed reactor. Approximately 0.15 g of catalyst was weighed and mixed with an equivalent mass of SiC. The mixture was loaded into a reactor and heated to reaction temperature. Reaction gases were delivered via mass flow controllers (Brooks) with water introduced with a metering pump (Quizix). The composition of the reaction mixture was as follows: H2 50%, CO 10%, CO2 10%, and H2O 30%. The reactant mixture was passed through a pre-heater before contacting the catalyst bed. Following reaction, the product gases were analyzed using a micro gas chromatograph (Varian Instruments, or Shimadzu). Compositional data on the performance diagram (FIG. 8) is on a dry basis with water removed.

[0263] Testing Results

[0264] FIG. 8 shows the CO composition in the product stream following the scale-up testing at a gas hour space velocity of 50,000 h−1.

TABLE 5
Catalyst Compositions (mass ratio)
Row	Col	ZrO2	Co	Water	Pt	Li	Mo	V
A	1	0.91	0.005	0	0.06	0.025	0	0
A	2	0.91	0.005	0	0.06	0.025	0	0
A	3	0.91	0	0	0.06	0.025	0.005	0
A	4	0.91	0	0	0.06	0.025	0.005	0
A	5	0.905	0	0	0.06	0.025	0	0.01
A	6	0.905	0	0	0.06	0.025	0	0.01
B	1	0.905	0.01	0	0.06	0.025	0	0
B	2	0.905	0.01	0	0.06	0.025	0	0
B	3	0.905	0	0	0.06	0.025	0.01	0
B	4	0.905	0	0	0.06	0.025	0.01	0
B	5	0.895	0	0	0.06	0.025	0	0.02
B	6	0.895	0	0	0.06	0.025	0	0.02
C	1	0.9	0.015	0	0.06	0.025	0	0
C	2	0.9	0.015	0	0.06	0.025	0	0
C	3	0.9	0	0	0.06	0.025	0.015	0
C	4	0.9	0	0	0.06	0.025	0.015	0
C	5	0.885	0	0	0.06	0.025	0	0.03
C	6	0.885	0	0	0.06	0.025	0	0.03
D	1	0.895	0.02	0	0.06	0.025	0	0
D	2	0.895	0.02	0	0.06	0.025	0	0
D	3	0.895	0	0	0.06	0.025	0.02	0
D	4	0.895	0	0	0.06	0.025	0.02	0
D	5	0.875	0	0	0.06	0.025	0	0.04
D	6	0.875	0	0	0.06	0.025	0	0.04

Example 9

[0265] Scale-up catalyst samples were prepared by using incipient wetness impregnation of 0.75 grams of ZrO2 support (Norton, 80-120 mesh) which had been weighed into a 10-dram vial. Aqueous metal precursor salt solutions were then added in the order: La, Ce, one of Co, Mo, or V, Pt, and finally Na. The precursor salt solutions were tetraammineplatinum (II) hydroxide (9.09% Pt (w/w)), lanthanum (III) nitrate (1.0M), cerium (IV) nitrate (1.0N), cobalt (II) nitrate (11.0M), molydbic acid (1.0M), vanadium citrate (1.0M), and sodium hydroxide (3.0N). All reagents were nominally research grade from Aldrich, Strem, or Alfa. Following each metal addition, the catalysts were dried at 80° C. overnight and then calcined in air as follows:

After Pt addition           300° C. for 3 hours
After La or Ce addition     450° C. for 3 hours
After Co, Mo, or V addition 350° C. for 3 hours.

[0266] Following Na addition, the catalysts were calcined at 300° C. for 3 hours, then the catalysts were reduced in-situ at 300° C. for 3 hours in a 10% H2/N2 feed.

[0267] Catalyst Testing Conditions

[0268] Catalysts were tested in a fixed bed reactor. Approximately 0.15 g of catalyst was weighed and mixed with an equivalent mass of SiC. The mixture was loaded into a reactor and heated to reaction temperature. Reaction gases were delivered via mass flow controllers (Brooks) with water introduced with a metering pump (Quizix). The composition of the reaction mixture was as follows: H2 50%, CO 10%, CO2 10%, and H2O 30%. The reactant mixture was passed through a pre-heater before contacting the catalyst bed. Following reaction, the product gases were analyzed using a micro gas chromatograph (Varian Instruments, or Shimadzu). Compositional data on the performance diagram (FIG. 9) is on a dry basis with water removed.

[0269] Testing Results

[0270] FIG. 9 shows the CO composition in the product stream following the scale-up testing at a gas hour space velocity of 50,000 h−1.

TABLE 6
Catalyst Compositions (mass ratio)
Row	Col	Support	Co	Pt	La	Na	Ce	Mo	V
A	1	0.885	0.005	0.06	0.025	0.025	0	0	0
A	2	0.885	0.005	0.06	0	0.025	0.025	0	0
A	3	0.885	0	0.06	0.025	0.025	0	0.005	0
A	4	0.885	0	0.06	0	0.025	0.025	0.005	0
A	5	0.88	0	0.06	0.025	0.025	0	0	0.01
A	6	0.88	0	0.06	0	0.025	0.025	0	0.01
B	1	0.86	0.005	0.06	0.05	0.025	0	0	0
B	2	0.86	0.005	0.06	0	0.025	0.05	0	0
B	3	0.86	0	0.06	0.05	0.025	0	0.005	0
B	4	0.86	0	0.06	0	0.025	0.05	0.005	0
B	5	0.855	0	0.06	0.05	0.025	0	0	0.01
B	6	0.855	0	0.06	0	0.025	0.05	0	0.01
C	1	0.88	0.01	0.06	0.025	0.025	0	0	0
C	2	0.88	0.01	0.06	0	0.025	0.025	0	0
C	3	0.88	0	0.06	0.025	0.025	0	0.01	0
C	4	0.88	0	0.06	0	0.025	0.025	0.01	0
C	5	0.87	0	0.06	0.025	0.025	0	0	0.02
C	6	0.87	0	0.06	0	0.025	0.025	0	0.02
D	1	0.855	0.01	0.06	0.05	0.025	0	0	0
D	2	0.855	0.01	0.06	0	0.025	0.05	0	0
D	3	0.855	0	0.06	0.05	0.025	0	0.01	0
D	4	0.855	0	0.06	0	0.025	0.05	0.01	0
D	5	0.845	0	0.06	0.05	0.025	0	0	0.02
D	6	0.845	0	0.06	0	0.025	0.05	0	0.02

Example 10

[0271] Scale-up catalyst samples were prepared by using incipient wetness impregnation of 0.75 grams of ZrO2 support (Norton, 80-120 mesh) which had been weighed into a 10-dram vial. Aqueous metal precursor salt solutions were then added in the order: V, Pt, and finally Na. The precursor salt solutions were tetraammineplatinum (II) hydroxide solution (9.09% Pt (w/w)), vanadium citrate (1.0M), and sodium hydroxide (3.0 N). All starting reagents were nominally research grade from Aldrich, Strem, or Alfa. Following each metal addition, the catalysts were dried at 80° C. overnight and then calcined in air as follows:

After Pt addition 300° C. for 3 hours
After V addition  350° C. for 3 hours.

[0272] Following Na addition, the catalysts were calcined at 300° C. for 3 hours, then the catalysts were reduced in-situ at 300° C. for 3 hours in a 10% H2/N2 feed.

[0273] Catalyst Testing Conditions

[0274] Catalysts were tested in a fixed bed reactor. Approximately 0.15 g of catalyst was weighed and mixed with an equivalent mass of SiC. The mixture was loaded into a reactor and heated to reaction temperature. Reaction gases were delivered via mass flow controllers (Brooks) with water introduced with a metering pump (Quizix). The composition of the reaction mixture was as follows: H2 50%, CO 10%, CO2 10%, and H2O 30%. The reactant mixture was passed through a pre-heater before contacting the catalyst bed. Following reaction, the product gases were analyzed using a micro gas chromatograph (Varian Instruments, or Shimadzu). Compositional data on the performance diagram (FIG. 12) is on a dry basis with water removed.

[0275] Testing Results

[0276] FIG. 12 shows the CO composition in the product stream following the scale-up testing at a gas hour space velocity of 50,000 h−1.

TABLE 7
Catalyst Compositions (mass ratio)
	Row	Col	Support	Pt	Na	V
	A	1	94.00	2.00	2.50	1.5
	A	2	91.50	2.00	5.00	1.5
	A	3	92.00	4.00	2.50	1.5
	A	4	89.50	4.00	5.00	1.5
	A	5	90.00	6.00	2.50	1.5
	A	6	87.50	6.00	5.00	1.5
	B	1	92.50	2.00	2.50	3.0
	B	2	90.00	2.00	5.00	3.0
	B	3	90.50	4.00	2.50	3.0
	B	4	88.00	4.00	5.00	3.0
	B	5	88.50	6.00	2.50	3.0
	B	6	86.00	6.00	5.00	3.0
	C	1	91.00	2.00	2.50	4.5
	C	2	88.50	2.00	5.00	4.5
	C	3	89.00	4.00	2.50	4.5
	C	4	86.50	4.00	5.00	4.5
	C	5	87.00	6.00	2.50	4.5
	C	6	84.50	6.00	5.00	4.5
	D	1	89.50	2.00	2.50	6.0
	D	2	87.00	2.00	5.00	6.0
	D	3	87.50	4.00	2.50	6.0
	D	4	85.00	4.00	5.00	6.0
	D	5	85.50	6.00	2.50	6.0
	D	6	83.00	6.00	5.00	6.0

[0277]

TABLE I
							Pt1.0%/
R	C	COCONV	H2OCONV	CO2PROD	CO2PERPROD	CH4PROD	ZrO2_std	CeNO33	NH42CeNO36	CoNO32
real	real	real	real	real	real	real	real	real	real	real
Temperature
250 C
1	1	29.8402	21.1977	1.0839	39.7897	0.1693	0.1275	0	0	0
1	2	−0.8066	−0.3468	0.0199	0.7318	0.015	0	0	0	0
1	3	−1.342	−0.8883	−0.0103	−0.3788	0.0069	0	0	0	0
1	4	−0.4471	−0.8737	−0.0209	−0.7679	0.0045	0	0	0	0
1	5	0.2051	−0.7078	0.0201	0.7386	0.0086	0	0	0	0
1	6	−0.2701	−1.1286	−0.0074	−0.273	0.0008	0	0	0	0
1	7	28.4296	17.0396	0.9422	34.5858	0.1303	0.1275	0	0	0
1	8	0.3481	−0.0616	−0.0199	−0.7298	−0.0025	0	0	0	0
1	9	−0.1214	−1.3018	−0.0217	−0.7951	0.001	0	0	0	0
1	10	1.2904	−0.1752	−0.0251	−0.9203	−0.0045	0	0	0	0
1	11	−0.1983	−0.4964	−0.0223	−0.8192	0.0005	0	0	0	0
1	12	−0.0741	−1.2392	−0.019	−0.6989	0.0004	0	0	0	0
1	13	27.9999	15.9352	0.9526	34.9687	0.128	0.1275	0	0	0
1	14	0.6232	−0.3023	0.0112	0.4122	0.0003	0	0	0	0
1	15	−0.1018	0.0336	−0.0235	−0.8632	−0.0047	0	0	0	0
1	16	27.2351	16.5803	0.888	32.5966	0.1185	0.1275	0	0	0
2	1	25.6429	17.9695	0.8313	30.5152	0.0986	0	0	0	0.125
2	2	29.4104	18.6834	0.9576	35.1519	0.1186	0	0	0.5	0.125
2	3	22.3392	8.9723	0.6239	22.9019	0.1378	0	0	0	0.125
2	4	0.8395	0.2708	0.0014	0.0528	−0.0013	0	0	0	0.125
2	5	22.4525	13.4385	0.672	24.6699	0.1033	0	0	0	0.125
2	6	30.6495	18.9614	1.028	37.7387	0.136	0	0	0	0.125
2	7	22.8992	14.6855	0.7054	25.8949	0.0994	0	0	0	0.125
2	8	16.4705	11.3025	0.4957	18.197	0.0643	0	0	0	0.125
2	9	25.2898	17.1191	0.8418	30.903	0.1018	0	0	0	0.125
2	10	27.7651	17.855	0.9307	34.1645	0.1134	0	0.5	0	0.125
2	11	15.2353	10.1525	0.5062	18.5825	0.0625	0	0	0	0.125
2	12	6.6516	3.7768	0.2027	7.4414	0.0231	0	0	0	0.125
2	13	5.6662	4.3865	0.1536	5.6377	0.0183	0	0	0	0.125
2	14	20.5443	12.549	0.6838	25.1023	0.0868	0	0	0	0.125
2	15	2.2164	0.1212	0.0573	2.1049	0.0061	0	0	0	0.125
2	16	0.393	1.3011	−0.0224	−0.821	−0.0062	0	0	0	0
3	1	22.2454	15.3754	0.7105	26.0826	0.0816	0	0	0	0.2188
3	2	28.0083	19.5547	0.885	32.4878	0.1083	0	0	0.4063	0.2188
3	3	23.6895	14.2896	0.6787	24.9136	0.1246	0	0	0	0.2188
3	4	0.9693	2.2659	−0.0302	−1.1081	−0.0146	0	0	0	0.2188
3	5	28.2742	16.4476	0.8881	32.6016	0.1315	0	0	0	0.2188
3	6	40.4567	21.9704	1.2225	44.8759	0.2055	0	0	0	0.2188
3	7	25.2346	17.7275	0.8079	29.6585	0.1051	0	0	0	0.2188
3	8	23.7508	16.0999	0.736	27.0183	0.1041	0	0	0	0.2188
3	9	26.3184	19.4909	0.8642	31.7233	0.098	0	0	0	0.2188
3	10	26.3066	17.5553	0.8712	31.9817	0.1009	0	0.4063	0	0.2188
3	11	16.5069	12.0298	0.525	19.2728	0.0577	0	0	0	0.2188
3	12	15.7501	11.8225	0.4936	18.1205	0.0521	0	0	0	0.2188
3	13	6.2855	5.3787	0.1728	6.3432	0.01	0	0	0	0.2188
3	14	18.4215	14.2445	0.619	22.7235	0.0672	0	0	0	0.2188
3	15	1.6097	3.5749	0.0233	0.8544	−0.0089	0	0	0	0.2188
3	16	1.3509	0.7363	0.0005	0.0168	−0.0077	0	0	0	0
4	1	23.1744	16.9866	0.7784	28.5757	0.0904	0	0	0	0.3125
4	2	28.5323	20.2685	0.9161	33.6276	0.112	0	0	0.3125	0.3125
4	3	24.9023	16.5852	0.7687	28.2199	0.1184	0	0	0	0.3125
4	4	8.3484	7.4139	0.2462	9.0365	0.0236	0	0	0	0.3125
4	5	28.2314	16.652	0.814	29.8824	0.1533	0	0	0	0.3125
4	6	39.4798	24.09	1.1719	43.0211	0.2026	0	0	0	0.3125
4	7	25.0657	17.1429	0.7976	29.2776	0.105	0	0	0	0.3125
4	8	20.8684	14.4244	0.6484	23.8022	0.0887	0	0	0	0.3125
4	9	26.476	18.4214	0.8784	32.2449	0.1005	0	0	0	0.3125
4	10	25.3804	18.1039	0.8522	31.2829	0.0975	0	0.3125	0	0.3125
4	11	13.9181	9.2274	0.4588	16.8412	0.0498	0	0	0	0.3125
4	12	13.6987	10.4619	0.434	15.9319	0.0459	0	0	0	0.3125
4	13	8.069	7.5589	0.2327	8.5431	0.0185	0	0	0	0.3125
4	14	21.7048	15.5036	0.7237	26.5651	0.0794	0	0	0	0.3125
4	15	7.1383	7.611	0.2204	8.0914	0.0168	0	0	0	0.3125
4	16	28.2274	18.5972	0.9383	34.4443	0.1182	0.1275	0	0	0
5	1	25.0356	17.8739	0.8182	30.0351	0.0996	0	0	0	0.4063
5	2	29.5211	21.5832	0.9284	34.0807	0.1135	0	0	0.2188	0.4063
5	3	25.5889	17.3611	0.7957	29.211	0.1149	0	0	0	0.4063
5	4	11.1187	9.9822	0.3389	12.4417	0.0338	0	0	0	0.4063
5	5	27.9457	16.713	0.8317	30.5293	0.1491	0	0	0	0.4063
5	6	38.1172	21.2674	1.1043	40.539	0.2047	0	0	0	0.4063
5	7	24.6847	17.5415	0.8004	29.3828	0.098	0	0	0	0.4063
5	8	24.8369	17.0456	0.7916	29.0571	0.1039	0	0	0	0.4063
5	9	25.2684	19.1268	0.8271	30.3624	0.0942	0	0	0	0.4063
5	10	25.9949	19.5089	0.8585	31.5149	0.0991	0	0.2188	0	0.4063
5	11	17.6559	13.8567	0.5775	21.1997	0.0635	0	0	0	0.4063
5	12	19.56	14.366	0.6131	22.5058	0.0705	0	0	0	0.4063
5	13	7.807	6.7271	0.2181	8.005	0.021	0	0	0	0.4063
5	14	22.2026	14.967	0.748	27.4571	0.0898	0	0	0	0.4063
5	15	11.4161	8.8494	0.3588	13.173	0.0373	0	0	0	0.4063
5	16	0.0343	0.2746	−0.0017	−0.0622	−0.007	0	0	0	0
6	1	28.3635	19.4266	0.9197	33.7623	0.1222	0	0	0	0.5
6	2	30.4663	20.8458	0.9865	36.2151	0.1288	0	0	0.125	0.5
6	3	24.5123	16.1173	0.794	29.1455	0.1075	0	0	0	0.5
6	4	20.2767	14.6918	0.6733	24.7161	0.0801	0	0	0	0.5
6	5	33.2496	16.76	0.9351	34.3274	0.2217	0	0	0	0.5
6	6	38.5058	19.2941	1.0938	40.154	0.2327	0	0	0	0.5
6	7	24.1336	17.4112	0.7994	29.3455	0.1052	0	0	0	0.5
6	8	22.6528	14.9365	0.7653	28.0945	0.0974	0	0	0	0.5
6	9	26.9144	19.6802	0.8845	32.4702	0.1055	0	0	0	0.5
6	10	26.6038	18.7414	0.9208	33.8001	0.11	0	0.125	0	0.5
6	11	22.4349	14.9258	0.7817	28.6959	0.0944	0	0	0	0.5
6	12	20.9112	14.2122	0.6922	25.4099	0.0817	0	0	0	0.5
6	13	11.904	7.5826	0.4014	14.7338	0.0486	0	0	0	0.5
6	14	23.5252	16.7311	0.7707	28.2915	0.0917	0	0	0	0.5
6	15	17.2103	10.833	0.5735	21.0513	0.067	0	0	0	0.5
6	16	1.0088	−0.1805	0.0177	0.6503	−0.0041	0	0	0	0
7	1	29.1091	18.3888	0.9377	34.4238	0.1288	0	0	0	0
7	2	23.4675	15.9929	0.7993	29.3427	0.1033	0	0	0	0.5
7	3	24.4	17.9806	0.8052	29.5583	0.0931	0	0	0.5	0
7	4	23.9259	17.6284	0.8206	30.1251	0.0928	0	0	0	0
7	5	21.9374	15.2657	0.7495	27.5124	0.0915	0	0	0	0
7	6	34.6888	23.3528	1.131	41.5182	0.1544	0	0	0	0
7	7	23.0341	16.9495	0.7009	25.7276	0.099	0	0	0	0
7	8	28.7153	15.6433	0.8015	29.4221	0.1671	0	0	0	0
7	9	21.8886	15.6142	0.7632	28.0152	0.0898	0	0	0	0
7	10	21.9107	15.6183	0.7745	28.4325	0.0907	0	0.5	0	0
7	11	18.5907	14.206	0.615	22.5768	0.0714	0	0	0	0
7	12	24.8013	17.9553	0.8391	30.8011	0.1049	0	0	0	0
7	13	4.148	4.5963	0.1558	5.7193	0.01	0	0	0	0
7	14	25.1707	16.9965	0.8683	31.875	0.1033	0	0	0	0
7	15	10.053	7.9852	0.3638	13.3549	0.0383	0	0	0	0
7	16	27.3338	18.6129	0.9314	34.1925	0.1154	0.1275	0	0	0
8	1	27.8709	16.8374	0.9039	33.1799	0.1419	0	0	0	0
8	2	25.0239	16.3557	0.8605	31.5885	0.1186	0	0	0	0.4063
8	3	23.3124	16.5445	0.7803	28.6442	0.1016	0	0	0.4063	0
8	4	30.4167	20.755	1.0121	37.1518	0.1278	0	0	0	0
8	5	22.4729	15.5952	0.7556	27.7364	0.0987	0	0	0	0
8	6	33.8859	22.7736	1.1246	41.2829	0.1534	0	0	0	0
8	7	23.0982	15.007	0.72	26.4315	0.1098	0	0	0	0
8	8	27.9822	13.7786	0.811	29.7729	0.1778	0	0	0	0
8	9	23.7305	17.1175	0.8213	30.1477	0.1059	0	0	0	0
8	10	24.1435	16.057	0.8058	29.5803	0.1029	0	0.4063	0	0
8	11	22.7845	15.9341	0.7662	28.126	0.1051	0	0	0	0
8	12	22.5472	14.8209	0.7762	28.4929	0.1038	0	0	0	0
8	13	4.6	5.0283	0.1611	5.9139	0.0164	0	0	0	0
8	14	26.3117	17.5568	0.8937	32.8057	0.1158	0	0	0	0
8	15	19.2935	13.6483	0.7008	25.725	0.0827	0	0	0	0
8	16	0.3501	2.3807	0.0044	0.1601	−0.0072	0	0	0	0
9	1	30.2669	17.4031	0.9382	34.439	0.1638	0	0	0	0
9	2	24.7831	15.5168	0.8133	29.856	0.1193	0	0	0	0.3125
9	3	24.8843	16.3799	0.8144	29.8952	0.1144	0	0	0.3125	0
9	4	27.7158	18.3043	0.9486	34.8222	0.1209	0	0	0	0
9	5	22.301	14.7031	0.7678	28.1862	0.1077	0	0	0	0
9	6	31.7529	21.8186	1.0511	38.5834	0.1407	0	0	0	0
9	7	22.4223	13.2509	0.6914	25.3794	0.1125	0	0	0	0
9	8	26.7272	10.823	0.7966	29.2411	0.1718	0	0	0	0
9	9	18.6358	11.9972	0.6423	23.5776	0.0893	0	0	0	0
9	10	21.5732	13.0857	0.7295	26.7785	0.0998	0	0.3125	0	0
9	11	21.8603	13.7562	0.7383	27.1031	0.1087	0	0	0	0
9	12	23.2584	14.2339	0.7779	28.5546	0.1092	0	0	0	0
9	13	6.1089	5.8813	0.2145	7.8737	0.0226	0	0	0	0
9	14	21.796	14.0238	0.7518	27.5966	0.1012	0	0	0	0
9	15	14.7758	10.7605	0.524	19.2341	0.0608	0	0	0	0
9	16	0.0047	0.3621	0.0345	1.268	0.0006	0	0	0	0
10	1	32.2957	12.969	0.8786	32.253	0.2259	0	0	0	0
10	2	22.9073	13.5906	0.7444	27.3268	0.1229	0	0	0	0.2188
10	3	24.02	14.4655	0.7658	28.1101	0.1285	0	0	0.2188	0
10	4	27.4735	18.2379	0.9287	34.0901	0.1247	0	0	0	0
10	5	25.7888	14.3222	0.7908	29.0301	0.1508	0	0	0	0
10	6	28.2681	18.4984	0.959	35.2041	0.1403	0	0	0	0
10	7	26.3335	13.7746	0.7698	28.257	0.1587	0	0	0	0
10	8	27.2793	11.6159	0.7715	28.3222	0.181	0	0	0	0
10	9	23.7532	13.9992	0.7647	28.0727	0.1187	0	0	0	0
10	10	23.0104	12.8612	0.7501	27.5368	0.1242	0	0.2188	0	0
10	11	24.3958	13.8516	0.7821	28.7085	0.1283	0	0	0	0
10	12	24.7178	14.4298	0.7945	29.1648	0.1251	0	0	0	0
10	13	6.2103	5.4757	0.2329	8.5508	0.0276	0	0	0	0
10	14	20.3259	13.0573	0.6932	25.4467	0.0987	0	0	0	0
10	15	18.1743	12.8071	0.6685	24.5392	0.0818	0	0	0	0
10	16	25.148	16.3311	0.9105	33.4226	0.1159	0.1275	0	0	0
11	1	33.2657	13.7869	0.9096	33.389	0.2236	0	0	0	0
11	2	26.3629	12.996	0.8123	29.819	0.1618	0	0	0	0.125
11	3	24.9661	13.9343	0.8015	29.4223	0.135	0	0	0.125	0
11	4	25.749	14.2206	0.8562	31.4286	0.1402	0	0	0	0
11	5	23.3622	11.0514	0.726	26.6504	0.1408	0	0	0	0
11	6	25.4002	15.3152	0.8622	31.652	0.1297	0	0	0	0
11	7	23.7527	11.0405	0.7081	25.9945	0.1474	0	0	0	0
11	8	25.2713	10.4518	0.7606	27.9193	0.1663	0	0	0	0
11	9	22.1004	12.2049	0.7055	25.8981	0.1177	0	0	0	0
11	10	21.8975	12.2273	0.7148	26.2406	0.1184	0	0.125	0	0
11	11	22.2123	12.4559	0.7208	26.4587	0.1235	0	0	0	0
11	12	22.4272	13.3655	0.7375	27.0716	0.1141	0	0	0	0
11	13	10.6819	7.0626	0.3567	13.095	0.0525	0	0	0	0
11	14	22.4528	12.9362	0.7568	27.7801	0.1206	0	0	0	0
11	15	19.7448	13.9333	0.6951	25.5175	0.0875	0	0	0	0
11	16	−0.1972	1.471	0.0237	0.8717	0.0002	0	0	0	0
12	1	31.5656	21.6797	1.0782	39.5788	0.1397	0	0	0	0
12	2	19.6043	13.572	0.6955	25.5322	0.089	0	0	0	0.5
12	3	28.1666	17.3647	0.9244	33.9334	0.1488	0	0	0	0
12	4	31.3253	21.7961	1.0594	38.89	0.1349	0	0	0.5	0
12	5	17.3834	14.0571	0.6238	22.8995	0.0749	0	0	0	0
12	6	35.3057	24.5521	1.1878	43.6046	0.1566	0	0	0	0
12	7	23.1431	16.6639	0.8015	29.4211	0.1066	0	0	0	0
12	8	26.6065	17.7981	0.9318	34.2045	0.1338	0	0	0	0
12	9	31.073	22.4346	1.0697	39.269	0.1354	0	0	0	0
12	10	29.9328	22.2939	1.0514	38.5962	0.1273	0	0.5	0	0
12	11	28.5736	20.9007	1.0125	37.1693	0.1236	0	0	0	0
12	12	28.8195	19.4676	1.0399	38.1729	0.1274	0	0	0	0
12	13	2.9218	3.3576	0.0985	3.6155	0.0097	0	0	0	0
12	14	25.7013	17.9671	0.9023	33.1211	0.1147	0	0	0	0
12	15	8.492	5.9126	0.3308	12.1433	0.0423	0	0	0	0
12	16	−0.1015	0.1618	0.0165	0.6066	0.0023	0	0	0	0
13	1	32.929	23.1662	1.1398	41.8401	0.1451	0	0	0	0
13	2	12.9188	10.5882	0.449	16.481	0.0547	0	0	0	0.4063
13	3	28.0856	18.7043	0.9401	34.5103	0.126	0	0	0	0
13	4	31.7131	22.9009	1.054	38.6919	0.1335	0	0	0.4063	0
13	5	10.3872	8.6629	0.3924	14.405	0.0454	0	0	0	0
13	6	32.6469	22.0266	1.0976	40.2904	0.1422	0	0	0	0
13	7	26.7979	19.1216	0.9313	34.1868	0.1168	0	0	0	0
13	8	27.1205	19.4829	0.9549	35.0517	0.1223	0	0	0	0
13	9	29.5931	21.5231	1.038	38.1041	0.1264	0	0	0	0
13	10	28.868	20.7843	1.0163	37.3068	0.1254	0	0.4063	0	0
13	11	19.8455	15.1061	0.6906	25.353	0.0865	0	0	0	0
13	12	28.8191	20.6337	1.0134	37.1994	0.1238	0	0	0	0
13	13	2.6024	3.2972	0.0961	3.526	0.0071	0	0	0	0
13	14	25.0501	16.2104	0.9126	33.5022	0.1159	0	0	0	0
13	15	6.4246	5.1337	0.2835	10.4071	0.0349	0	0	0	0
13	16	24.6043	16.341	0.9005	33.0556	0.1142	0.1275	0	0	0
14	1	31.1905	22.5852	1.0761	39.5045	0.1379	0	0	0	0
14	2	15.3686	12.5627	0.5534	20.3138	0.0672	0	0	0	0.3125
14	3	28.5902	21.079	0.9573	35.1415	0.1252	0	0	0	0
14	4	30.8225	21.6996	1.0648	39.0881	0.1372	0	0	0.3125	0
14	5	10.1619	9.3091	0.3843	14.1078	0.0446	0	0	0	0
14	6	25.9037	19.3547	0.9378	34.425	0.1151	0	0	0	0
14	7	28.9615	21.1086	0.9966	36.5847	0.129	0	0	0	0
14	8	25.3268	19.6253	0.9096	33.392	0.1117	0	0	0	0
14	9	30.5368	22.8098	1.0517	38.6072	0.1317	0	0	0	0
14	10	30.4639	21.8604	1.0468	38.4279	0.1319	0	0.3125	0	0
14	11	28.5368	20.5826	1.0152	37.2667	0.1262	0	0	0	0
14	12	28.9878	20.031	1.0283	37.748	0.1277	0	0	0	0
14	13	1.9405	3.4997	0.1021	3.7493	0.0083	0	0	0	0
14	14	26.2698	18.1259	0.9407	34.5326	0.1172	0	0	0	0
14	15	3.5222	3.4456	0.1728	6.345	0.0193	0	0	0	0
14	16	−1.2721	0.2876	0.0152	0.5574	0	0	0	0	0
15	1	21.9285	16.5533	0.7944	29.1616	0.0981	0	0	0	0
15	2	8.5556	7.9322	0.3176	11.6581	0.0386	0	0	0	0.2188
15	3	28.9139	19.3873	1.0115	37.1305	0.1329	0	0	0	0
15	4	29.4947	20.5675	1.0129	37.1816	0.1319	0	0	0.2188	0
15	5	10.3199	7.8183	0.3758	13.7939	0.0488	0	0	0	0
15	6	19.07	12.9719	0.6822	25.0424	0.0872	0	0	0	0
15	7	24.4592	16.5438	0.8787	32.2577	0.1122	0	0	0	0
15	8	26.1966	19.0364	0.9283	34.0753	0.1149	0	0	0	0
15	9	28.805	20.399	1.0007	36.7353	0.1231	0	0	0	0
15	10	27.8671	19.9279	0.9883	36.2797	0.1237	0	0.2188	0	0
15	11	25.9077	18.1393	0.9238	33.9133	0.1174	0	0	0	0
15	12	26.8168	19.5131	0.9364	34.3739	0.1198	0	0	0	0
15	13	3.1831	4.1719	0.1255	4.6087	0.0135	0	0	0	0
15	14	25.6485	17.9831	0.9073	33.3061	0.1142	0	0	0	0
15	15	3.4019	2.8501	0.1862	6.8334	0.0252	0	0	0	0
15	16	−0.6764	0.6935	0.0304	1.1161	0.0028	0	0	0	0
16	1	27.2358	17.9797	0.9948	36.5199	0.1324	0	0	0	0
16	2	20.4235	13.9408	0.7544	27.693	0.0997	0	0	0	0.125
16	3	22.1148	16.7994	0.7919	29.0693	0.101	0	0	0	0
16	4	27.8457	18.1657	0.9706	35.6285	0.1316	0	0	0.125	0
16	5	16.0515	10.9271	0.6032	22.1443	0.0766	0	0	0	0
16	6	21.5319	16.4412	0.8048	29.5417	0.101	0	0	0	0
16	7	28.6538	19.2213	1.0145	37.243	0.1346	0	0	0	0
16	8	27.0582	20.0777	0.9481	34.8038	0.1218	0	0	0	0
16	9	28.251	19.2368	1.0097	37.0662	0.132	0	0	0	0
16	10	28.3144	19.6597	0.9907	36.3661	0.1282	0	0.125	0	0
16	11	25.2372	17.9227	0.9037	33.1748	0.1146	0	0	0	0
16	12	27.1113	19.9798	0.984	36.1202	0.1221	0	0	0	0
16	13	7.0222	6.86	0.2888	10.6009	0.0359	0	0	0	0
16	14	24.3113	16.5973	0.9032	33.1567	0.1156	0	0	0	0
16	15	11.0117	7.8026	0.4408	16.1825	0.0553	0	0	0	0
16	16	24.9744	15.3136	0.9047	33.2092	0.1182	0.1275	0	0	0
R	CoOAc2	Na3CoNO36	CuNO32	GeOX2	H2MoO4	KRuO4	RuNONO33	RuNOOAc3	LaNO33	NH4ReO4	PtNH32NO22
real	real	real	real	real	real	real	real	real	real	real	real
Temper-
ature:
250 C.
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0
2	0	0	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0.0989	0	0	0	0.1275
2	0	0	0	0	0.5	0	0	0	0	0	0.1275
2	0.5	0	0	0	0	0	0	0	0	0	0.1275
2	0	0.5	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0.098	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0.098	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.5	0	0.1275
2	0	0	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0	0	0.1275
2	0	0	0.5	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0	0.1074	0.1275
2	0	0	0	0.2	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0	0	0
3	0	0	0	0	0	0	0	0	0	0	0.1275
3	0	0	0	0	0	0	0	0	0	0	0.1275
3	0	0	0	0	0	0	0.0804	0	0	0	0.1275
3	0	0	0	0	0.4063	0	0	0	0	0	0.1275
3	0.4063	0	0	0	0	0	0	0	0	0	0.1275
3	0	0.4063	0	0	0	0	0	0	0	0	0.1275
3	0	0	0	0	0	0	0	0	0	0	0.1275
3	0	0	0	0	0	0	0	0.0796	0	0	0.1275
3	0	0	0	0	0	0	0	0	0.4063	0	0.1275
3	0	0	0	0	0	0	0	0	0	0	0.1275
3	0	0	0	0	0	0	0	0	0	0	0.1275
3	0	0	0	0	0	0	0	0	0	0	0.1275
3	0	0	0.4063	0	0	0	0	0	0	0	0.1275
3	0	0	0	0	0	0	0	0	0	0.0873	0.1275
3	0	0	0	0.1625	0	0	0	0	0	0	0.1275
3	0	0	0	0	0	0	0	0	0	0	0
4	0	0	0	0	0	0	0	0	0	0	0.1275
4	0	0	0	0	0	0	0	0	0	0	0.1275
4	0	0	0	0	0	0	0.0618	0	0	0	0.1275
4	0	0	0	0	0.3125	0	0	0	0	0	0.1275
4	0.3125	0	0	0	0	0	0	0	0	0	0.1275
4	0	0.3125	0	0	0	0	0	0	0	0	0.1275
4	0	0	0	0	0	0.0613	0	0	0	0	0.1275
4	0	0	0	0	0	0	0	0.0613	0	0	0.1275
4	0	0	0	0	0	0	0	0	0.3125	0	0.1275
4	0	0	0	0	0	0	0	0	0	0	0.1275
4	0	0	0	0	0	0	0	0	0	0	0.1275
4	0	0	0	0	0	0	0	0	0	0	0.1275
4	0	0	0.3125	0	0	0	0	0	0	0	0.1275
4	0	0	0	0	0	0	0	0	0	0.0671	0.1275
4	0	0	0	0.125	0	0	0	0	0	0	0.1275
4	0	0	0	0	0	0	0	0	0	0	0
5	0	0	0	0	0	0	0	0	0	0	0.1275
5	0	0	0	0	0	0	0	0	0	0	0.1275
5	0	0	0	0	0	0	0.0433	0	0	0	0.1275
5	0	0	0	0	0.2188	0	0	0	0	0	0.1275
5	0.2188	0	0	0	0	0	0	0	0	0	0.1275
5	0	0.2188	0	0	0	0	0	0	0	0	0.1275
5	0	0	0	0	0	0.0429	0	0	0	0	0.1275
5	0	0	0	0	0	0	0	0.0429	0	0	0.1275
5	0	0	0	0	0	0	0	0	0.2188	0	0.1275
5	0	0	0	0	0	0	0	0	0	0	0.1275
5	0	0	0	0	0	0	0	0	0	0	0.1275
5	0	0	0	0	0	0	0	0	0	0	0.1275
5	0	0	0.2188	0	0	0	0	0	0	0	0.1275
5	0	0	0	0	0	0	0	0	0	0.047	0.1275
5	0	0	0	0.0875	0	0	0	0	0	0	0.1275
5	0	0	0	0	0	0	0	0	0	0	0
6	0	0	0	0	0	0	0	0	0	0	0.1275
6	0	0	0	0	0	0	0	0	0	0	0.1275
6	0	0	0	0	0	0	0.0247	0	0	0	0.1275
6	0	0	0	0	0.125	0	0	0	0	0	0.1275
6	0.125	0	0	0	0	0	0	0	0	0	0.1275
6	0	0.125	0	0	0	0	0	0	0	0	0.1275
6	0	0	0	0	0	0.0245	0	0	0	0	0.1275
6	0	0	0	0	0	0	0	0.0245	0	0	0.1275
6	0	0	0	0	0	0	0	0	0.125	0	0.1275
6	0	0	0	0	0	0	0	0	0	0	0.1275
6	0	0	0	0	0	0	0	0	0	0	0.1275
6	0	0	0	0	0	0	0	0	0	0	0.1275
6	0	0	0.125	0	0	0	0	0	0	0	0.1275
6	0	0	0	0	0	0	0	0	0	0.0269	0.1275
6	0	0	0	0.05	0	0	0	0	0	0	0.1275
6	0	0	0	0	0	0	0	0	0	0	0
7	0	0	0	0	0	0	0.0247	0	0	0	0.1275
7	0	0	0	0	0	0	0.0247	0	0	0	0.1275
7	0	0	0	0	0	0	0.0247	0	0	0	0.1275
7	0	0	0	0	0.5	0	0.0247	0	0	0	0.1275
7	0.5	0	0	0	0	0	0.0247	0	0	0	0.1275
7	0	0.5	0	0	0	0	0.0247	0	0	0	0.1275
7	0	0	0	0	0	0.098	0.0247	0	0	0	0.1275
7	0	0	0	0	0	0	0.0247	0.098	0	0	0.1275
7	0	0	0	0	0	0	0.0247	0	0.5	0	0.1275
7	0	0	0	0	0	0	0.0247	0	0	0	0.1275
7	0	0	0	0	0	0	0.0247	0	0	0	0.1275
7	0	0	0	0	0	0	0.0247	0	0	0	0.1275
7	0	0	0.5	0	0	0	0.0247	0	0	0	0.1275
7	0	0	0	0	0	0	0.0247	0	0	0.1074	0.1275
7	0	0	0	0.2	0	0	0.0247	0	0	0	0.1275
7	0	0	0	0	0	0	0	0	0	0	0
8	0	0	0	0	0	0	0.0433	0	0	0	0.1275
8	0	0	0	0	0	0	0.0433	0	0	0	0.1275
8	0	0	0	0	0	0	0.0433	0	0	0	0.1275
8	0	0	0	0	0.4063	0	0.0433	0	0	0	0.1275
8	0.4063	0	0	0	0	0	0.0433	0	0	0	0.1275
8	0	0.4063	0	0	0	0	0.0433	0	0	0	0.1275
8	0	0	0	0	0	0.0796	0.0433	0	0	0	0.1275
8	0	0	0	0	0	0	0.0433	0.0796	0	0	0.1275
8	0	0	0	0	0	0	0.0433	0	0.4063	0	0.1275
8	0	0	0	0	0	0	0.0433	0	0	0	0.1275
8	0	0	0	0	0	0	0.0433	0	0	0	0.1275
8	0	0	0	0	0	0	0.0433	0	0	0	0.1275
8	0	0	0.4063	0	0	0	0.0433	0	0	0	0.1275
8	0	0	0	0	0	0	0.0433	0	0	0.0873	0.1275
8	0	0	0	0.1625	0	0	0.0433	0	0	0	0.1275
8	0	0	0	0	0	0	0	0	0	0	0
9	0	0	0	0	0	0	0.0618	0	0	0	0.1275
9	0	0	0	0	0	0	0.0618	0	0	0	0.1275
9	0	0	0	0	0	0	0.0618	0	0	0	0.1275
9	0	0	0	0	0.3125	0	0.0618	0	0	0	0.1275
9	0.3125	0	0	0	0	0	0.0618	0	0	0	0.1275
9	0	0.3125	0	0	0	0	0.0618	0	0	0	0.1275
9	0	0	0	0	0	0.0613	0.0618	0	0	0	0.1275
9	0	0	0	0	0	0	0.0618	0.0613	0	0	0.1275
9	0	0	0	0	0	0	0.0618	0	0.3125	0	0.1275
9	0	0	0	0	0	0	0.0618	0	0	0	0.1275
9	0	0	0	0	0	0	0.0618	0	0	0	0.1275
9	0	0	0	0	0	0	0.0618	0	0	0	0.1275
9	0	0	0.3125	0	0	0	0.0618	0	0	0	0.1275
9	0	0	0	0	0	0	0.0618	0	0	0.0671	0.1275
9	0	0	0	0.125	0	0	0.0618	0	0	0	0.1275
9	0	0	0	0	0	0	0	0	0	0	0
10	0	0	0	0	0	0	0.0804	0	0	0	0.1275
10	0	0	0	0	0	0	0.0804	0	0	0	0.1275
10	0	0	0	0	0	0	0.0804	0	0	0	0.1275
10	0	0	0	0	0.2188	0	0.0804	0	0	0	0.1275
10	0.2188	0	0	0	0	0	0.0804	0	0	0	0.1275
10	0	0.2188	0	0	0	0	0.0804	0	0	0	0.1275
10	0	0	0	0	0	0.0429	0.0804	0	0	0	0.1275
10	0	0	0	0	0	0	0.0804	0.0429	0	0	0.1275
10	0	0	0	0	0	0	0.0804	0	0.2188	0	0.1275
10	0	0	0	0	0	0	0.0804	0	0	0	0.1275
10	0	0	0	0	0	0	0.0804	0	0	0	0.1275
10	0	0	0	0	0	0	0.0804	0	0	0	0.1275
10	0	0	0.2188	0	0	0	0.0804	0	0	0	0.1275
10	0	0	0	0	0	0	0.0804	0	0	0.047	0.1275
10	0	0	0	0.0875	0	0	0.0804	0	0	0	0.1275
10	0	0	0	0	0	0	0	0	0	0	0
11	0	0	0	0	0	0	0.0989	0	0	0	0.1275
11	0	0	0	0	0	0	0.0989	0	0	0	0.1275
11	0	0	0	0	0	0	0.0989	0	0	0	0.1275
11	0	0	0	0	0.125	0	0.0989	0	0	0	0.1275
11	0.125	0	0	0	0	0	0.0989	0	0	0	0.1275
11	0	0.125	0	0	0	0	0.0989	0	0	0	0.1275
11	0	0	0	0	0	0.0245	0.0989	0	0	0	0.1275
11	0	0	0	0	0	0	0.0989	0.0245	0	0	0.1275
11	0	0	0	0	0	0	0.0989	0	0.125	0	0.1275
11	0	0	0	0	0	0	0.0989	0	0	0	0.1275
11	0	0	0	0	0	0	0.0989	0	0	0	0.1275
11	0	0	0	0	0	0	0.0989	0	0	0	0.1275
11	0	0	0.125	0	0	0	0.0989	0	0	0	0.1275
11	0	0	0	0	0	0	0.0989	0	0	0.0269	0.1275
11	0	0	0	0.05	0	0	0.0989	0	0	0	0.1275
11	0	0	0	0	0	0	0	0	0	0	0
12	0	0	0	0	0.125	0	0	0	0	0	0.1275
12	0	0	0	0	0.125	0	0	0	0	0	0.1275
12	0	0	0	0	0.125	0	0.0989	0	0	0	0.1275
12	0	0	0	0	0.125	0	0	0	0	0	0.1275
12	0.5	0	0	0	0.125	0	0	0	0	0	0.1275
12	0	0.5	0	0	0.125	0	0	0	0	0	0.1275
12	0	0	0	0	0.125	0.098	0	0	0	0	0.1275
12	0	0	0	0	0.125	0	0	0.098	0	0	0.1275
12	0	0	0	0	0.125	0	0	0	0.5	0	0.1275
12	0	0	0	0	0.125	0	0	0	0	0	0.1275
12	0	0	0	0	0.125	0	0	0	0	0	0.1275
12	0	0	0	0	0.125	0	0	0	0	0	0.1275
12	0	0	0.5	0	0.125	0	0	0	0	0	0.1275
12	0	0	0	0	0.125	0	0	0	0	0.1074	0.1275
12	0	0	0	0.2	0.125	0	0	0	0	0	0.1275
12	0	0	0	0	0	0	0	0	0	0	0
13	0	0	0	0	0.2188	0	0	0	0	0	0.1275
13	0	0	0	0	0.2188	0	0	0	0	0	0.1275
13	0	0	0	0	0.2188	0	0.0804	0	0	0	0.1275
13	0	0	0	0	0.2188	0	0	0	0	0	0.1275
13	0.4063	0	0	0	0.2188	0	0	0	0	0	0.1275
13	0	0.4063	0	0	0.2188	0	0	0	0	0	0.1275
13	0	0	0	0	0.2188	0.0796	0	0	0	0	0.1275
13	0	0	0	0	0.2188	0	0	0.0796	0	0	0.1275
13	0	0	0	0	0.2188	0	0	0	0.4063	0	0.1275
13	0	0	0	0	0.2188	0	0	0	0	0	0.1275
13	0	0	0	0	0.2188	0	0	0	0	0	0.1275
13	0	0	0	0	0.2188	0	0	0	0	0	0.1275
13	0	0	0.4063	0	0.2188	0	0	0	0	0	0.1275
13	0	0	0	0	0.2188	0	0	0	0	0.0873	0.1275
13	0	0	0	0.1625	0.2188	0	0	0	0	0	0.1275
13	0	0	0	0	0	0	0	0	0	0	0
14	0	0	0	0	0.3125	0	0	0	0	0	0.1275
14	0	0	0	0	0.3125	0	0	0	0	0	0.1275
14	0	0	0	0	0.3125	0	0.0618	0	0	0	0.1275
14	0	0	0	0	0.3125	0	0	0	0	0	0.1275
14	0.3125	0	0	0	0.3125	0	0	0	0	0	0.1275
14	0	0.3125	0	0	0.3125	0	0	0	0	0	0.1275
14	0	0	0	0	0.3125	0.0613	0	0	0	0	0.1275
14	0	0	0	0	0.3125	0	0	0.0613	0	0	0.1275
14	0	0	0	0	0.3125	0	0	0	0.3125	0	0.1275
14	0	0	0	0	0.3125	0	0	0	0	0	0.1275
14	0	0	0	0	0.3125	0	0	0	0	0	0.1275
14	0	0	0	0	0.3125	0	0	0	0	0	0.1275
14	0	0	0.3125	0	0.3125	0	0	0	0	0	0.1275
14	0	0	0	0	0.3125	0	0	0	0	0.0671	0.1275
14	0	0	0	0.125	0.3125	0	0	0	0	0	0.1275
14	0	0	0	0	0	0	0	0	0	0	0
15	0	0	0	0	0.4063	0	0	0	0	0	0.1275
15	0	0	0	0	0.4063	0	0	0	0	0	0.1275
15	0	0	0	0	0.4063	0	0.0433	0	0	0	0.1275
15	0	0	0	0	0.4063	0	0	0	0	0	0.1275
15	0.2188	0	0	0	0.4063	0	0	0	0	0	0.1275
15	0	0.2188	0	0	0.4063	0	0	0	0	0	0.1275
15	0	0	0	0	0.4063	0.0429	0	0	0	0	0.1275
15	0	0	0	0	0.4063	0	0	0.0429	0	0	0.1275
15	0	0	0	0	0.4063	0	0	0	0.2188	0	0.1275
15	0	0	0	0	0.4063	0	0	0	0	0	0.1275
15	0	0	0	0	0.4063	0	0	0	0	0	0.1275
15	0	0	0	0	0.4063	0	0	0	0	0	0.1275
15	0	0	0.2188	0	0.4063	0	0	0	0	0	0.1275
15	0	0	0	0	0.4063	0	0	0	0	0.047	0.1275
15	0	0	0	0.0875	0.4063	0	0	0	0	0	0.1275
15	0	0	0	0	0	0	0	0	0	0	0
16	0	0	0	0	0.5	0	0	0	0	0	0.1275
16	0	0	0	0	0.5	0	0	0	0	0	0.1275
16	0	0	0	0	0.5	0	0.0247	0	0	0	0.1275
16	0	0	0	0	0.5	0	0	0	0	0	0.1275
16	0.125	0	0	0	0.5	0	0	0	0	0	0.1275
16	0	0.125	0	0	0.5	0	0	0	0	0	0.1275
16	0	0	0	0	0.5	0.0245	0	0	0	0	0.1275
16	0	0	0	0	0.5	0	0	0.0245	0	0	0.1275
16	0	0	0	0	0.5	0	0	0	0.125	0	0.1275
16	0	0	0	0	0.5	0	0	0	0	0	0.1275
16	0	0	0	0	0.5	0	0	0	0	0	0.1275
16	0	0	0	0	0.5	0	0	0	0	0	0.1275
16	0	0	0.125	0	0.5	0	0	0	0	0	0.1275
16	0	0	0	0	0.5	0	0	0	0	0.0269	0.1275
16	0	0	0	0.05	0.5	0	0	0	0	0	0.1275
16	0	0	0	0	0	0	0	0	0	0	0
R	ZrONO32	ZrOOAc2	SUM—	mol %	mol %	mol %	mol %	mol %	mol %	mol %	mol %	mol %	mol %
real	real	real	micromols	Ce	Co	Cu	Ge	Mo	Ru	La	Re	Pt	Zr
Temperature:
250 C
1	0	0	0.1275	0	0	0	0	0	0	0	0	100	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0.1275	0	0	0	0	0	0	0	0	100	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0.1275	0	0	0	0	0	0	0	0	100	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0	0	0	0
1	0	0	0.1275	0	0	0	0	0	0	0	0	100	0
2	0	0	0.2525	0	49.5	0	0	0	0	0	0	50.5	0
2	0	0	0.7525	66.45	16.61	0	0	0	0	0	0	16.94	0
2	0	0	0.3514	0	35.57	0	0	0	28.14	0	0	36.28	0
2	0	0	0.7525	0	16.61	0	0	66.45	0	0	0	16.94	0
2	0	0	0.7525	0	83.06	0	0	0	0	0	0	16.94	0
2	0	0	0.7525	0	83.06	0	0	0	0	0	0	16.94	0
2	0	0	0.3505	0	35.66	0	0	0	27.96	0	0	36.38	0
2	0	0	0.3505	0	35.66	0	0	0	27.96	0	0	36.38	0
2	0	0	0.7525	0	16.61	0	0	0	0	66.45	0	16.94	0
2	0	0	0.7525	66.45	16.61	0	0	0	0	0	0	16.94	0
2	0.5	0	0.7525	0	16.61	0	0	0	0	0	0	16.94	66.45
2	0	0.5	0.7525	0	16.61	0	0	0	0	0	0	16.94	66.45
2	0	0	0.7525	0	16.61	66.45	0	0	0	0	0	16.94	0
2	0	0	0.3599	0	34.73	0	0	0	0	0	29.84	35.43	0
2	0	0	0.4525	0	27.62	0	44.2	0	0	0	0	28.18	0
2	0	0	0	0	0	0	0	0	0	0	0	0	0
3	0	0	0.3463	0	63.18	0	0	0	0	0	0	36.82	0
3	0	0	0.7525	53.99	29.07	0	0	0	0	0	0	16.94	0
3	0	0	0.4266	0	51.28	0	0	0	18.84	0	0	29.89	0
3	0	0	0.7525	0	29.07	0	0	53.99	0	0	0	16.94	0
3	0	0	0.7525	0	83.06	0	0	0	0	0	0	16.94	0
3	0	0	0.7525	0	83.06	0	0	0	0	0	0	16.94	0
3	0	0	0.4259	0	51.36	0	0	0	18.7	0	0	29.94	0
3	0	0	0.4259	0	51.36	0	0	0	18.7	0	0	29.94	0
3	0	0	0.7525	0	29.07	0	0	0	0	53.99	0	16.94	0
3	0	0	0.7525	53.99	29.07	0	0	0	0	0	0	16.94	0
3	0.4063	0	0.7525	0	29.07	0	0	0	0	0	0	16.94	53.99
3	0	0.4063	0.7525	0	29.07	0	0	0	0	0	0	16.94	53.99
3	0	0	0.7525	0	29.07	53.99	0	0	0	0	0	16.94	0
3	0	0	0.4335	0	50.46	0	0	0	0	0	20.13	29.41	0
3	0	0	0.5088	0	43	0	31.94	0	0	0	0	25.06	0
3	0	0	0	0	0	0	0	0	0	0	0	0	0
4	0	0	0.44	0	71.02	0	0	0	0	0	0	28.98	0
4	0	0	0.7525	41.53	41.53	0	0	0	0	0	0	16.94	0
4	0	0	0.5018	0	62.27	0	0	0	12.32	0	0	25.41	0
4	0	0	0.7525	0	41.53	0	0	41.23	0	0	0	16.94	0
4	0	0	0.7525	0	83.06	0	0	0	0	0	0	16.94	0
4	0	0	0.7525	0	83.06	0	0	0	0	0	0	16.94	0
4	0	0	0.5013	0	62.34	0	0	0	12.22	0	0	25.44	0
4	0	0	0.5013	0	62.34	0	0	0	12.22	0	0	25.44	0
4	0	0	0.7525	0	41.53	0	0	0	0	41.53	0	16.94	0
4	0	0	0.7525	0	41.53	0	0	0	0	0	0	16.94	0
4	0.3125	0	0.7525	41.53	41.53	0	0	0	0	0	0	16.94	41.53
4	0	0.3125	0.7525	0	41.53	0	0	0	0	0	0	16.94	41.53
4	0	0	0.7525	0	41.53	41.53	0	0	0	0	0	16.94	0
4	0	0	0.5071	0	61.62	0	0	0	0	0	13.24	25.14	0
4	0	0	0.565	0	55.31	0	22.12	0	0	0	0	22.57	0
4	0	0	0.1275	0	0	0	0	0	0	0	0	100	0
5	0	0	0.5338	0	76.11	0	0	0	0	0	0	23.89	0
5	0	0	0.7525	29.07	53.99	0	0	0	0	0	0	16.94	0
5	0	0	0.577	0	70.4	0	0	0	7.5	0	0	22.1	0
5	0	0	0.7525	0	53.99	0	0	29.07	0	0	0	16.94	0
5	0	0	0.7525	0	83.06	0	0	0	0	0	0	16.94	0
5	0	0	0.7525	0	83.06	0	0	0	0	0	0	16.94	0
5	0	0	0.5766	0	70.45	0	0	0	7.44	0	0	22.11	0
5	0	0	0.5766	0	70.45	0	0	0	7.44	0	0	22.11	0
5	0	0	0.7525	0	53.99	0	0	0	0	29.07	0	16.94	0
5	0	0	0.7525	29.07	53.99	0	0	0	0	0	0	16.94	0
5	0.2188	0	0.7525	0	53.99	0	0	0	0	0	0	16.94	29.07
5	0	0.2188	0.7525	0	53.99	0	0	0	0	0	0	16.94	29.07
5	0	0	0.7525	0	53.99	29.07	0	0	0	0	0	16.94	0
5	0	0	0.5807	0	69.95	0	0	0	0	0	8.09	21.95	0
5	0	0	0.6213	0	65.39	0	14.08	0	0	0	0	20.52	0
5	0	0	0	0	0	0	0	0	0	0	0	0	0
6	0	0	0.6275	0	79.68	0	0	0	0	0	0	20.32	0
6	0	0	0.7525	16.61	66.45	0	0	0	0	0	0	16.94	0
6	0	0	0.6522	0	76.66	0	0	0	3.79	0	0	19.55	0
6	0	0	0.7525	0	66.45	0	0	16.61	0	0	0	16.94	0
6	0	0	0.7525	0	83.06	0	0	0	0	0	0	16.94	0
6	0	0	0.7525	0	83.06	0	0	0	0	0	0	16.94	0
6	0	0	0.652	0	76.69	0	0	0	3.76	0	0	19.56	0
6	0	0	0.652	0	76.69	0	0	0	3.76	0	0	19.56	0
6	0	0	0.7525	0	66.45	0	0	0	0	16.61	0	16.94	0
6	0	0	0.7525	16.61	66.45	0	0	0	0	0	0	16.94	0
6	0.125	0	0.7525	0	66.45	0	0	0	0	0	0	16.94	16.61
6	0	0.125	0.7525	0	66.45	0	0	0	0	0	0	16.94	16.61
6	0	0	0.7525	0	66.45	16.61	0	0	0	0	0	16.94	0
6	0	0	0.6544	0	76.41	0	0	0	0	0	4.1	19.48	0
6	0	0	0.6775	0	73.8	0	7.38	0	0	0	0	18.82	0
6	0	0	0	0	0	0	0	0	0	0	0	0	0
7	0	0	0.1522	0	0	0	0	0	16.24	0	0	83.76	0
7	0	0	0.6522	0	76.66	0	0	0	3.79	0	0	19.55	0
7	0	0	0.6522	76.66	0	0	0	0	3.79	0	0	19.55	0
7	0	0	0.6522	0	0	0	0	76.66	3.79	0	0	19.55	0
7	0	0	0.6522	0	76.66	0	0	0	3.79	0	0	19.55	0
7	0	0	0.6522	0	76.66	0	0	0	3.79	0	0	19.55	0
7	0	0	0.2502	0	0	0	0	0	49.05	0	0	50.95	0
7	0	0	0.2502	0	0	0	0	0	49.05	0	0	50.95	0
7	0	0	0.6522	0	0	0	0	0	3.79	76.66	0	19.55	0
7	0	0	0.6522	76.66	0	0	0	0	3.79	0	0	19.55	0
7	0.5	0	0.6522	0	0	0	0	0	3.79	0	0	19.55	76.66
7	0	0.5	0.6522	0	0	0	0	0	3.79	0	0	19.55	76.66
7	0	0	0.6522	0	0	76.66	0	0	3.79	0	0	19.55	0
7	0	0	0.2596	0	0	0	0	0	9.52	0	41.37	49.11	0
7	0	0	0.3522	0	0	0	56.78	0	7.02	0	0	36.2	0
7	0	0	0.1275	0	0	0	0	0	0	0	0	100	0
8	0	0	0.1708	0	0	0	0	0	25.34	0	0	74.66	0
8	0	0	0.577	0	70.4	0	0	0	7.5	0	0	22.1	0
8	0	0	0.577	70.4	0	0	0	0	7.5	0	0	22.1	0
8	0	0	0.577	0	0	0	0	70.4	7.5	0	0	22.1	0
8	0	0	0.577	0	70.4	0	0	0	7.5	0	0	22.1	0
8	0	0	0.577	0	70.4	0	0	0	7.5	0	0	22.1	0
8	0	0	0.2504	0	0	0	0	0	49.08	0	0	50.92	0
8	0	0	0.2504	0	0	0	0	0	49.08	0	0	50.92	0
8	0	0	0.577	0	0	0	0	0	7.5	70.4	0	22.1	0
8	0	0	0.577	70.4	0	0	0	0	7.5	0	0	22.1	0
8	0.4063	0	0.577	0	0	0	0	0	7.5	0	0	22.1	70.4
8	0	0.4063	0.577	0	0	0	0	0	7.5	0	0	22.1	70.4
8	0	0	0.577	0	0	70.4	0	0	7.5	0	0	22.1	0
8	0	0	0.258	0	0	0	0	0	16.77	0	33.82	49.41	0
8	0	0	0.333	0	0	0	48.76	0	12.98	0	0	38.26	0
8	0	0	0	0	0	0	0	0	0	0	0	0	0
9	0	0	0.1893	0	0	0	0	0	32.65	0	0	67.35	0
9	0	0	0.5018	0	62.27	0	0	0	12.32	0	0	25.41	0
9	0	0	0.5018	62.27	0	0	0	0	12.32	0	0	25.41	0
9	0	0	0.5018	0	0	0	0	62.27	12.32	0	0	25.41	0
9	0	0	0.5018	0	62.27	0	0	0	12.32	0	0	25.41	0
9	0	0	0.5018	0	62.27	0	0	0	12.32	0	0	25.41	0
9	0	0	0.2506	0	0	0	0	0	49.11	0	0	50.89	0
9	0	0	0.2506	0	0	0	0	0	49.11	0	0	50.89	0
9	0	0	0.5018	0	0	0	0	0	12.32	62.27	0	25.41	0
9	0	0	0.5018	62.27	0	0	0	0	12.32	0	0	25.41	0
9	0.3125	0	0.5018	0	0	0	0	0	12.32	0	0	25.41	62.27
9	0	0.3125	0.5018	0	0	0	0	0	12.32	0	0	25.41	62.27
9	0	0	0.5018	0	0	62.27	0	0	12.32	0	0	25.41	0
9	0	0	0.2564	0	0	0	0	0	24.1	0	26.18	49.72	0
9	0	0	0.3143	0	0	0	39.77	0	19.67	0	0	40.56	0
9	0	0	0	0	0	0	0	0	0	0	0	0	0
10	0	0	0.2079	0	0	0	0	0	38.66	0	0	61.34	0
10	0	0	0.4266	0	51.28	0	0	0	18.84	0	0	29.89	0
10	0	0	0.4266	51.28	0	0	0	0	18.84	0	0	29.89	0
10	0	0	0.4266	0	0	0	0	51.28	18.84	0	0	29.89	0
10	0	0	0.4266	0	51.28	0	0	0	18.84	0	0	29.89	0
10	0	0	0.4266	0	51.28	0	0	0	18.84	0	0	29.89	0
10	0	0	0.2507	0	0	0	0	0	49.15	0	0	50.85	0
10	0	0	0.2507	0	0	0	0	0	49.15	0	0	50.85	0
10	0	0	0.4266	0	0	0	0	0	18.84	51.28	0	29.89	0
10	0	0	0.4266	51.28	0	0	0	0	18.84	0	0	29.89	0
10	0.2188	0	0.4266	0	0	0	0	0	18.84	0	0	29.89	51.28
10	0	0.2188	0.4266	0	0	0	0	0	18.84	0	0	29.89	51.28
10	0	0	0.4266	0	0	51.28	0	0	18.84	0	0	29.89	0
10	0	0	0.2548	0	0	0	0	0	31.53	0	18.44	50.03	0
10	0	0	0.2954	0	0	0	29.63	0	27.21	0	0	43.17	0
10	0	0	0.1275	0	0	0	0	0	0	0	0	100	0
11	0	0	0.2264	0	0	0	0	0	43.68	0	0	56.32	0
11	0	0	0.3514	0	35.57	0	0	0	28.14	0	0	36.28	0
11	0	0	0.3514	35.57	0	0	0	0	28.14	0	0	36.28	0
11	0	0	0.3514	0	0	0	0	35.57	28.14	0	0	36.28	0
11	0	0	0.3514	0	35.57	0	0	0	28.14	0	0	36.28	0
11	0	0	0.3514	0	35.57	0	0	0	28.14	0	0	36.28	0
11	0	0	0.2509	0	0	0	0	0	49.18	0	0	50.82	0
11	0	0	0.2509	0	0	0	0	0	49.18	0	0	50.82	0
11	0	0	0.3514	0	0	0	0	0	28.14	35.57	0	36.28	0
11	0	0	0.3514	35.57	0	0	0	0	28.14	0	0	36.28	0
11	0.125	0	0.3514	0	0	0	0	0	28.14	0	0	36.28	35.57
11	0	0.125	0.3514	0	0	0	0	0	28.14	0	0	36.28	35.57
11	0	0	0.3514	0	0	35.57	0	0	28.14	0	0	36.28	0
11	0	0	0.2533	0	0	0	0	0	39.05	0	10.6	50.35	0
11	0	0	0.2764	0	0	0	18.09	0	35.78	0	0	46.13	0
11	0	0	0	0	0	0	0	0	0	0	0	0	0
12	0	0	0.2525	0	0	0	0	49.5	0	0	0	50.5	0
12	0	0	0.7525	0	66.45	0	0	16.61	0	0	0	16.94	0
12	0	0	0.3514	0	0	0	0	35.57	28.14	0	0	36.28	0
12	0	0	0.7525	66.45	0	0	0	16.61	0	0	0	16.94	0
12	0	0	0.7525	0	66.45	0	0	16.61	0	0	0	16.94	0
12	0	0	0.7525	0	66.45	0	0	16.61	0	0	0	16.94	0
12	0	0	0.3505	0	0	0	0	35.66	27.96	0	0	36.38	0
12	0	0	0.3505	0	0	0	0	35.66	27.96	0	0	36.38	0
12	0	0	0.7525	0	0	0	0	16.61	0	66.45	0	16.94	0
12	0	0	0.7525	66.45	0	0	0	16.61	0	0	0	16.94	0
12	0.5	0	0.7525	0	0	0	0	16.61	0	0	0	16.94	66.45
12	0	0.5	0.7525	0	0	0	0	16.61	0	0	0	16.94	66.45
12	0	0	0.7525	0	0	66.45	0	16.61	5	0	0	16.94	0
12	0	0	0.3599	0	0	0	0	34.73	0	0	29.84	35.43	0
12	0	0	0.4525	0	0	0	44.2	27.62	0	0	0	28.18	0
12	0	0	0	0	0	0	0	0	0	0	0	0	0
13	0	0	0.3463	0	0	0	0	63.18	0	0	0	36.82	0
13	0	0	0.7525	0	53.99	0	0	29.07	0	0	0	16.94	0
13	0	0	0.4266	0	0	0	0	51.28	18.84	0	0	29.89	0
13	0	0	0.7525	53.99	0	0	0	29.07	0	0	0	16.94	0
13	0	0	0.7525	0	53.99	0	0	29.07	0	0	0	16.94	0
13	0	0	0.7525	0	53.99	0	0	29.07	0	0	0	16.94	0
13	0	0	0.4259	0	0	0	0	51.36	18.7	0	0	29.94	0
13	0	0	0.4259	0	0	0	0	51.36	18.7	0	0	29.94	0
13	0	0	0.7525	0	0	0	0	29.07	0	53.99	0	16.94	0
13	0	0	0.7525	53.99	0	0	0	29.07	0	0	0	16.94	0
13	0.4063	0	0.7525	0	0	0	0	29.07	0	0	0	16.94	53.99
13	0	0.4063	0.7525	0	0	0	0	29.07	0	0	0	16.94	53.99
13	0	0	0.7525	0	0	53.99	0	29.07	0	0	0	16.94	0
13	0	0	0.4335	0	0	0	0	50.46	0	0	20.13	29.41	0
13	0	0	0.5088	0	0	0	31.94	43	0	0	0	25.06	0
13	0	0	0.1275	0	0	0	0	0	0	0	0	100	0
14	0	0	0.44	0	0	0	0	71.02	0	0	0	28.98	0
14	0	0	0.7525	0	41.53	0	0	41.53	0	0	0	16.94	0
14	0	0	0.5018	0	0	0	0	62.27	12.32	0	0	25.41	0
14	0	0	0.7525	41.53	0	0	0	41.53	0	0	0	16.94	0
14	0	0	0.7525	0	41.53	0	0	41.53	0	0	0	16.94	0
14	0	0	0.7525	0	41.53	0	0	41.53	0	0	0	16.94	0
14	0	0	0.5013	0	0	0	0	62.34	12.22	0	0	25.44	0
14	0	0	0.5013	0	0	0	0	62.34	12.22	0	0	25.44	0
14	0	0	0.7525	0	0	0	0	41.53	0	41.53	0	16.94	0
14	0	0	0.7525	41.53	0	0	0	41.53	0	0	0	16.94	0
14	0.3125	0	0.7525	0	0	0	0	41.53	0	0	0	16.94	41.53
14	0	0.3125	0.7525	0	0	0	0	41.53	0	0	0	16.94	41.53
14	0	0	0.7525	0	0	41.53	0	41.53	0	0	0	16.94	0
14	0	0	0.5071	0	0	0	0	61.62	0	0	13.24	25.14	0
14	0	0	0.565	0	0	0	22.12	55.31	0	0	0	22.57	0
14	0	0	0	0	0	0	0	0	0	0	0	0	0
15	0	0	0.5338	0	0	0	0	76.11	0	0	0	23.89	0
15	0	0	0.7525	0	29.07	0	0	53.99	0	0	0	16.94	0
15	0	0	0.577	0	0	0	0	70.4	7.5	0	0	22.1	0
15	0	0	0.7525	29.07	0	0	0	53.99	0	0	0	16.94	0
15	0	0	0.7525	0	29.07	0	0	53.99	0	0	0	16.94	0
15	0	0	0.7525	0	29.07	0	0	53.99	0	0	0	16.94	0
15	0	0	0.5766	0	0	0	0	70.45	7.44	0	0	22.11	0
15	0	0	0.5766	0	0	0	0	70.45	7.44	0	0	22.11	0
15	0	0	0.7525	0	0	0	0	53.99	0	29.07	0	16.94	0
15	0	0	0.7525	29.07	0	0	0	53.99	0	0	0	16.94	0
15	0.2188	0	0.7525	0	0	0	0	53.99	0	0	0	16.94	29.07
15	0	0.2188	0.7525	0	0	0	0	53.99	0	0	0	16.94	29.07
15	0	0	0.7525	0	0	29.07	0	53.99	0	0	0	16.94	0
15	0	0	0.5807	0	0	0	0	69.95	0	0	8.09	21.95	0
15	0	0	0.6213	0	0	0	14.08	65.39	0	0	0	20.52	0
15	0	0	0	0	0	0	0	0	0	0	0	0	0
16	0	0	0.6275	0	0	0	0	79.68	0	0	0	20.32	0
16	0	0	0.7525	0	16.61	0	0	66.45	0	0	0	16.94	0
16	0	0	0.6522	0	0	0	0	76.66	3.79	0	0	19.55	0
16	0	0	0.7525	16.61	0	0	0	66.45	0	0	0	16.94	0
16	0	0	0.7525	0	16.61	0	0	66.45	0	0	0	16.94	0
16	0	0	0.7525	0	16.61	0	0	66.45	0	0	0	16.94	0
16	0	0	0.652	0	0	0	0	76.69	3.76	0	0	19.56	0
16	0	0	0.652	0	0	0	0	76.69	3.76	0	0	19.56	0
16	0	0	0.7525	0	0	0	0	66.45	0	16.61	0	16.94	0
16	0	0	0.7525	16.61	0	0	0	66.45	0	0	0	16.94	0
16	0.125	0	0.7525	0	0	0	0	66.45	0	0	0	16.94	16.61
16	0	0.125	0.7525	0	0	0	0	66.45	0	0	0	16.94	16.61
16	0	0	0.7525	0	0	16.61	0	66.45	0	0	0	16.94	0
16	0	0	0.6544	0	0	0	0	76.41	0	0	4.1	19.48	0
16	0	0	0.6775	0	0	0	7.38	73.8	0	0	0	18.82	0
16	0	0	0.1275	0	0	0	0	0	0	0	0	100	0

[0278]

TABLE II
							Pt2.5%/		shift2—
R	C	COCONV	H2OCONV	CO2PROD	CO2PERPROD	CH4PROD	ZrO2_std	PtNH32NO22	std
real	real	real	real	real	real	real	real	real	real
Temperature:
200 C.
1	1	5.8854	7.1324	0.334	12.4611	0.0591	0.384	0	0
1	2	−0.6933	1.7113	0.0121	0.4524	0.0112	0	0	0
1	3	−1.0879	−0.033	0.0156	0.5835	0.0099	0	0	0
1	4	8.4959	6.4002	0.3047	11.3709	0.0443	0	0	0.768
1	5	−0.2835	0.6389	0.0083	0.3103	0.0042	0	0	0
1	6	−0.0255	1.131	−0.0073	−0.2728	0.0001	0	0	0
1	7	16.8595	11.8588	0.5807	21.6685	0.0759	0.384	0	0
1	8	0.5792	1.6555	−0.0166	−0.6207	−0.0015	0	0	0
1	9	0.5058	−0.1249	−0.0251	−0.9379	−0.0006	0	0	0
1	10	2.462	0.2771	0.0413	1.541	0.0092	0	0	0.768
1	11	0.0019	−1.3951	−0.0192	−0.7182	0.0002	0	0	0
1	12	0.2469	−0.1814	−0.0266	−0.9942	−0.0021	0	0	0
1	13	11.9953	8.0254	0.352	13.1329	0.044	0.384	0	0
1	14	−0.2562	−2.7011	−0.0114	−0.4265	0.0037	0	0	0
1	15	0.6886	−0.0929	−0.0235	−0.8767	−0.0026	0	0	0
1	16	2.2755	−0.5365	0.0631	2.3544	0.0118	0	0	0.768
2	1	1.6292	1.7918	0.0235	0.8778	0.0007	0	0.1275	0
2	2	1.0595	0.9687	−0.0202	−0.752	−0.0051	0	0.1275	0
2	3	3.1871	2.0235	0.0769	2.8696	0.0072	0	0.1275	0
2	4	11.3379	8.344	0.3126	11.6649	0.0345	0	0.1275	0
2	5	7.334	4.6193	0.1933	7.2111	0.0233	0	0.1275	0
2	6	16.1807	10.5884	0.5103	19.0429	0.0638	0	0.1275	0
2	7	13.3218	8.6946	0.3821	14.2574	0.0468	0	0.1275	0
2	8	13.8451	8.4363	0.4407	16.4438	0.0555	0	0.1275	0
2	9	3.7336	1.8779	0.076	2.8349	0.0082	0	0.1275	0
2	10	3.7611	2.5358	0.0642	2.3968	0.0066	0	0.1275	0
2	11	9.6508	6.4773	0.2773	10.347	0.035	0	0.1275	0
2	12	9.1424	6.1475	0.2521	9.4059	0.0294	0	0.1275	0
2	13	5.5133	3.6401	0.155	5.7829	0.0203	0	0.1275	0
2	14	4.9192	2.3616	0.1071	3.9974	0.014	0	0.1275	0
2	15	3.2245	1.7666	0.0897	3.3488	0.0134	0	0.1275	0
2	16	0.0898	−0.5096	−0.0063	−0.2341	0.001	0	0	0
3	1	6.9984	4.7277	0.1921	7.1687	0.0208	0	0.1148	0
3	2	1.7067	0.9785	0.0029	0.108	−0.0017	0	0.1148	0
3	3	2.6544	1.9617	0.0481	1.7934	0.0045	0	0.1148	0
3	4	12.8291	8.3823	0.3884	14.4943	0.0479	0	0.1148	0
3	5	7.3563	5.392	0.2102	7.8432	0.025	0	0.1148	0
3	6	16.2779	11.5339	0.4914	18.3342	0.0591	0	0.1148	0
3	7	14.8045	9.8506	0.4449	16.6026	0.0553	0	0.1148	0
3	8	11.2329	7.7728	0.3309	12.3461	0.0385	0	0.1148	0
3	9	2.866	2.3243	0.048	1.7899	0.0045	0	0.1148	0
3	10	4.7888	4.0416	0.0856	3.1937	0.0072	0	0.1148	0
3	11	7.5704	6.3606	0.2386	8.9027	0.0272	0	0.1148	0
3	12	8.8338	8.1131	0.241	8.9937	0.0242	0	0.1148	0
3	13	5.5254	3.9512	0.1376	5.1339	0.0154	0	0.1148	0
3	14	6.1987	4.2911	0.1741	6.4953	0.0195	0	0.1148	0
3	15	3.654	2.1732	0.0701	2.6141	0.0056	0	0.1148	0
3	16	0.3139	−0.4382	−0.0103	−0.3839	−0.002	0	0	0
4	1	8.1372	6.051	0.2684	10.0162	0.0285	0	0.102	0
4	2	1.4135	−1.0921	−0.0019	−0.0694	0.0006	0	0.102	0
4	3	2.3694	2.3665	0.05	1.8672	0.0016	0	0.102	0
4	4	12.8778	10.2102	0.3982	14.858	0.0416	0	0.102	0
4	5	6.8789	5.4193	0.218	8.1354	0.0221	0	0.102	0
4	6	17.1121	11.1844	0.5742	21.4257	0.0656	0	0.102	0
4	7	15.2253	7.4374	0.5006	18.6802	0.0634	0	0.102	0
4	8	12.1072	6.9574	0.3621	13.5097	0.0421	0	0.102	0
4	9	3.0168	2.3445	0.0559	2.0868	0.0029	0	0.102	0
4	10	3.4366	2.6695	0.0827	3.0869	0.0059	0	0.102	0
4	11	9.3273	8.1068	0.2694	10.0512	0.0274	0	0.102	0
4	12	8.2623	5.7824	0.2401	8.9601	0.0264	0	0.102	0
4	13	6.4459	5.7408	0.1696	6.3286	0.0159	0	0.102	0
4	14	7.5269	4.4391	0.2096	7.8207	0.0229	0	0.102	0
4	15	2.3665	3.2131	0.1135	4.2368	0.0107	0	0.102	0
4	16	14.955	9.0888	0.4741	17.6909	0.0576	0.384	0	0
5	1	7.255	5.6173	0.2393	8.929	0.0219	0	0.0893	0
5	2	1.2894	1.2279	−0.0083	−0.3084	−0.0072	0	0.0893	0
5	3	2.7038	3.3448	0.0437	1.6316	−0.0003	0	0.0893	0
5	4	11.707	8.2569	0.3623	13.517	0.0367	0	0.0893	0
5	5	7.6925	6.1121	0.2125	7.9274	0.0185	0	0.0893	0
5	6	17.0142	12.7392	0.5131	19.1465	0.0602	0	0.0893	0
5	7	14.8949	11.3697	0.4646	17.3347	0.0527	0	0.0893	0
5	8	9.7274	5.9642	0.3049	11.3767	0.0342	0	0.0893	0
5	9	3.4389	3.1002	0.0582	2.1723	0.0038	0	0.0893	0
5	10	3.1194	2.1123	0.0777	2.8988	0.007	0	0.0893	0
5	11	9.8621	7.5832	0.2728	10.1805	0.0278	0	0.0893	0
5	12	7.0266	5.2932	0.1915	7.1464	0.0207	0	0.0893	0
5	13	5.7354	4.6583	0.155	5.7842	0.0157	0	0.0893	0
5	14	5.5119	4.962	0.1327	4.952	0.0106	0	0.0893	0
5	15	2.8173	1.2279	0.0802	2.993	0.004	0	0.0893	0
5	16	0.8239	1.9962	0.0239	0.8909	−0.0001	0	0	0
6	1	4.7196	3.0755	0.1686	6.2918	0.018	0	0.0765	0
6	2	0.6723	0.5379	0.0114	0.4248	−0.001	0	0.0765	0
6	3	1.5179	1.911	0.0258	0.9622	−0.0024	0	0.0765	0
6	4	11.4899	6.8245	0.3774	14.0835	0.0427	0	0.0765	0
6	5	7.2343	5.5992	0.2075	7.7439	0.0214	0	0.0765	0
6	6	16.1946	11.0902	0.5277	19.6917	0.062	0	0.0765	0
6	7	14.3055	10.2177	0.4469	16.6766	0.0505	0	0.0765	0
6	8	8.3454	6.6475	0.2423	9.0418	0.0238	0	0.0765	0
6	9	4.5897	2.8387	0.0804	3.0009	0.0145	0	0.0765	0
6	10	3.5258	2.9589	0.0899	3.3528	0.0069	0	0.0765	0
6	11	9.6292	7.4338	0.3058	11.4104	0.0348	0	0.0765	0
6	12	5.4461	4.774	0.14	5.2242	0.0095	0	0.0765	0
6	13	5.2789	3.9957	0.1742	6.4996	0.0198	0	0.0765	0
6	14	6.0234	3.1388	0.208	7.7595	0.023	0	0.0765	0
6	15	2.7153	2.6186	0.0572	2.1344	0.0026	0	0.0765	0
6	16	0.6172	0.881	−0.0048	−0.1782	−0.006	0	0	0
7	1	3.6058	2.8177	0.1122	4.1848	0.0114	0	0.0638	0
7	2	1.5457	1.1415	−0.0046	−0.1727	−0.0077	0	0.0638	0
7	3	1.1265	1.8421	0.0513	1.9154	0.0017	0	0.0638	0
7	4	10.9458	6.7214	0.3327	12.4157	0.0389	0	0.0638	0
7	5	7.3704	6.6413	0.2192	8.18	0.0202	0	0.0638	0
7	6	16.5168	12.5524	0.5112	19.0738	0.0567	0	0.0638	0
7	7	14.124	9.8009	0.4529	16.8982	0.0533	0	0.0638	0
7	8	8.0466	6.418	0.2665	9.9439	0.0279	0	0.0638	0
7	9	4.9159	1.9763	0.102	3.8056	0.021	0	0.0638	0
7	10	3.921	1.5095	0.0817	3.0486	0.0055	0	0.0638	0
7	11	9.7833	6.8289	0.3095	11.5499	0.0353	0	0.0638	0
7	12	5.7437	4.0574	0.1866	6.9609	0.0216	0	0.0638	0
7	13	5.4086	4.6319	0.1686	6.2897	0.0153	0	0.0638	0
7	14	4.7264	2.9579	0.1463	5.4578	0.0098	0	0.0638	0
7	15	2.2359	1.425	0.0541	2.0176	0.003	0	0.0638	0
7	16	1.905	−0.5369	0.0559	2.0863	0.0028	0	0	0.768
8	1	1.8516	1.7327	0.0497	1.8541	−0.001	0	0.051	0
8	2	0.7246	−0.2854	0.0085	0.3172	−0.0044	0	0.051	0
8	3	2.2172	1.0419	0.0055	0.2056	−0.0051	0	0.051	0
8	4	8.5881	6.1691	0.2633	9.8264	0.031	0	0.051	0
8	5	6.9155	5.1078	0.1919	7.1608	0.0186	0	0.051	0
8	6	13.6231	8.8606	0.4319	16.1142	0.0489	0	0.051	0
8	7	12.7013	7.6084	0.3755	14.013	0.0421	0	0.051	0
8	8	5.7321	3.3144	0.1554	5.7994	0.0148	0	0.051	0
8	9	6.1461	1.113	0.0847	3.1618	0.0264	0	0.051	0
8	10	3.0168	1.2432	0.0668	2.491	0.003	0	0.051	0
8	11	7.9516	3.9932	0.2353	8.7787	0.0247	0	0.051	0
8	12	4.5547	2.22	0.1059	3.9517	0.0094	0	0.051	0
8	13	5.4421	2.2227	0.1712	6.3866	0.0179	0	0.051	0
8	14	2.9709	1.2529	0.0884	3.2997	0.0058	0	0.051	0
8	15	2.0502	0.6577	0.053	1.9778	0.0016	0	0.051	0
8	16	1.0942	−0.5602	−0.0087	−0.3263	−0.0082	0	0	0
9	1	3.6525	0.857	0.0654	2.4413	0.0008	0	0.0383	0
9	2	0.9979	0.3153	0.0037	0.1389	−0.0052	0	0.0383	0
9	3	1.7466	−0.0553	0.0132	0.492	−0.004	0	0.0383	0
9	4	8.1388	6.6606	0.2396	8.9397	0.0239	0	0.0383	0
9	5	6.3048	3.5229	0.1519	5.6663	0.0115	0	0.0383	0
9	6	11.8358	7.3317	0.3738	13.9486	0.044	0	0.0383	0
9	7	12.0946	6.9223	0.3836	14.3153	0.0431	0	0.0383	0
9	8	4.5013	2.4933	0.127	4.7393	0.0114	0	0.0383	0
9	9	5.5653	−1.5672	0.0994	3.7081	0.0371	0	0.0383	0
9	10	2.0973	−0.2551	0.0556	2.0746	0.0051	0	0.0383	0
9	11	6.2072	3.3304	0.1879	7.0119	0.0196	0	0.0383	0
9	12	3.6564	2.9811	0.0776	2.8969	0.004	0	0.0383	0
9	13	5.2299	1.9964	0.1531	5.7131	0.0156	0	0.0383	0
9	14	1.9393	0.5427	0.0483	1.8011	0.0018	0	0.0383	0
9	15	1.6602	0.2685	0.0303	1.1291	0.0009	0	0.0383	0
9	16	−0.3094	−1.3702	0.0051	0.1919	−0.0023	0	0	0
10	1	1.2902	−0.2919	−0.0046	−0.1733	−0.005	0	0.1275	0
10	2	0.5013	−0.0646	0.0015	0.055	−0.0023	0	0.1275	0
10	3	6.4947	3.5233	0.2062	7.6942	0.0238	0	0.1275	0
10	4	4.8095	1.6288	0.1367	5.0991	0.0131	0	0.1275	0
10	5	11.2766	6.8521	0.3728	13.9092	0.04	0	0.1275	0
10	6	6.4291	3.2734	0.2109	7.8701	0.0235	0	0.1275	0
10	7	5.8614	3.204	0.1874	6.9938	0.0213	0	0.1275	0
10	8	3.9022	−0.0952	0.1469	5.4801	0.0167	0	0.1275	0
10	9	5.9845	3.8381	0.1724	6.4326	0.0186	0	0.1275	0
10	10	6.3544	3.1325	0.1996	7.4459	0.0201	0	0.1275	0
10	11	4.2593	1.9552	0.1068	3.9844	0.009	0	0.1275	0
10	12	11.8549	4.3493	0.4371	16.3114	0.0553	0	0.1275	0
10	13	3.4944	1.347	0.0565	2.1073	0.0007	0	0.1275	0
10	14	1.6799	−1.1032	0.0339	1.2643	0.0015	0	0.1275	0
10	15	1.2201	0.118	0.0146	0.5448	−0.0033	0	0.1275	0
10	16	13.1891	7.744	0.4607	17.19	0.0567	0.384	0	0
11	1	0.4697	−0.9386	0.0209	0.7815	−0.0002	0	0.1126	0
11	2	0.3137	−0.3079	0.0152	0.5655	−0.0038	0	0.1126	0
11	3	3.7312	3.0925	0.1295	4.8339	0.0116	0	0.1126	0
11	4	4.2947	4.1725	0.1258	4.6927	0.0118	0	0.1126	0
11	5	8.2513	4.6606	0.2639	9.848	0.0294	0	0.1126	0
11	6	7.7794	6.0534	0.2575	9.6078	0.0255	0	0.1126	0
11	7	7.1211	4.9645	0.2168	8.0891	0.0217	0	0.1126	0
11	8	6.6894	3.5982	0.2513	9.3781	0.0253	0	0.1126	0
11	9	5.7623	1.227	0.1774	6.6189	0.0215	0	0.1126	0
11	10	3.9535	3.5594	0.1199	4.4725	0.0085	0	0.1126	0
11	11	2.9585	1.468	0.1075	4.0128	0.0071	0	0.1126	0
11	12	10.8769	7.5198	0.371	13.8434	0.0424	0	0.1126	0
11	13	2.5558	1.6142	0.0798	2.9792	0.0034	0	0.1126	0
11	14	0.9894	0.2057	0.0325	1.2133	0.0006	0	0.1126	0
11	15	−0.1651	−0.5824	0.0225	0.8396	0.0003	0	0.1126	0
11	16	0.2312	−0.1398	0.0419	1.5619	0.0035	0	0	0
12	1	0.1745	−0.7789	0.0282	1.0504	−0.0007	0	0.0978	0
12	2	0.1358	−0.938	0.0123	0.4577	−0.0028	0	0.0978	0
12	3	2.687	2.3049	0.1171	4.3697	0.0094	0	0.0978	0
12	4	2.7011	2.3219	0.0919	3.43	0.0055	0	0.0978	0
12	5	7.2214	3.1868	0.2524	9.4194	0.0269	0	0.0978	0
12	6	5.2931	1.7052	0.2034	7.5887	0.0227	0	0.0978	0
12	7	5.7915	3.2059	0.1832	6.8371	0.015	0	0.0978	0
12	8	1.223	−0.5999	0.053	1.9777	0.0048	0	0.0978	0
12	9	4.3277	1.446	0.1789	6.6748	0.0204	0	0.0978	0
12	10	2.3611	−1.6069	0.0943	3.5182	0.0118	0	0.0978	0
12	11	1.217	1.2973	0.0636	2.3728	0.0026	0	0.0978	0
12	12	9.4921	6.357	0.3144	11.7329	0.0336	0	0.0978	0
12	13	1.1195	−0.1983	0.051	1.9028	0.0019	0	0.0978	0
12	14	−0.4284	−1.8025	0.0316	1.1789	0.004	0	0.0978	0
12	15	−0.3772	−1.2476	0.0263	0.9816	−0.0008	0	0.0978	0
12	16	−0.6263	−0.7525	0.0219	0.8183	−0.0027	0	0	0
13	1	−0.2044	−0.3108	0.0233	0.869	−0.001	0	0.0829	0
13	2	−0.0357	−1.5987	0.0196	0.731	−0.0015	0	0.0829	0
13	3	2.5404	2.3681	0.0759	2.8308	0.0035	0	0.0829	0
13	4	2.9681	1.1781	0.1095	4.0842	0.009	0	0.0829	0
13	5	4.7412	2.8854	0.1519	5.6697	0.0123	0	0.0829	0
13	6	4.056	3.1404	0.1425	5.3155	0.0122	0	0.0829	0
13	7	3.445	3.976	0.1125	4.1961	0.0064	0	0.0829	0
13	8	2.1923	2.6039	0.0689	2.5713	0.0029	0	0.0829	0
13	9	3.6921	2.839	0.1493	5.5723	0.0156	0	0.0829	0
13	10	1.9985	1.0455	0.0943	3.5184	0.0065	0	0.0829	0
13	11	1.8485	1.7993	0.0648	2.4165	0.001	0	0.0829	0
13	12	7.3772	4.858	0.2612	9.7459	0.0272	0	0.0829	0
13	13	0.67	−0.7364	0.0509	1.8995	0.0036	0	0.0829	0
13	14	−0.1545	−0.1684	0.04	1.4918	0.0027	0	0.0829	0
13	15	−0.2342	−1.9441	0.0301	1.1244	0.0022	0	0.0829	0
13	16	1.0182	−0.222	0.0635	2.3688	0.0043	0	0	0.768
14	1	0.0925	0.2319	0.0233	0.8681	−0.0031	0	0.068	0
14	2	−0.3296	1.4585	0.019	0.7088	−0.0031	0	0.068	0
14	3	1.1002	0.2941	0.0694	2.5909	0.0068	0	0.068	0
14	4	0.2831	0.151	0.054	2.0157	0.0033	0	0.068	0
14	5	3.0444	2.2158	0.1301	4.8563	0.0105	0	0.068	0
14	6	0.0907	−1.4912	0.0607	2.2642	0.0081	0	0.068	0
14	7	1.4092	0.7998	0.0648	2.4188	0.0046	0	0.068	0
14	8	0.6786	0.7924	0.041	1.5316	0.0021	0	0.068	0
14	9	2.5503	0.8249	0.1115	4.1607	0.0105	0	0.068	0
14	10	0.8956	−0.2159	0.066	2.4626	0.0059	0	0.068	0
14	11	0.524	0.8305	0.0497	1.8557	0.0015	0	0.068	0
14	12	2.3834	0.0805	0.1461	5.4498	0.0132	0	0.068	0
14	13	0.7037	−0.6285	0.0416	1.5519	0.0023	0	0.068	0
14	14	−0.8416	−2.9099	0.0431	1.6083	0.0049	0	0.068	0
14	15	−0.5009	−2.4335	0.0188	0.7005	0.0002	0	0.068	0
14	16	−0.5344	1.0228	0.0124	0.4625	−0.0053	0	0	0
15	1	−0.7531	−0.171	0.0264	0.9837	0.0003	0	0.0531	0
15	2	−0.0408	0.6254	0.0184	0.6852	−0.0028	0	0.0531	0
15	3	0.8082	0.4025	0.0618	2.3061	0.0107	0	0.0531	0
15	4	1.2594	1.0454	0.0358	1.3359	−0.001	0	0.0531	0
15	5	2.5885	0.4231	0.0623	2.3251	0.0048	0	0.0531	0
15	6	2.0805	1.313	0.0715	2.6661	0.0026	0	0.0531	0
15	7	1.2853	−0.982	0.0166	0.619	−0.0002	0	0.0531	0
15	8	1.379	0.7764	0.051	1.9016	−0.0004	0	0.0531	0
15	9	2.5418	1.2534	0.1081	4.0346	0.0103	0	0.0531	0
15	10	1.0685	−0.8601	0.0743	2.7741	0.0064	0	0.0531	0
15	11	1.164	−0.8841	0.0493	1.838	0.0024	0	0.0531	0
15	12	3.2541	0.4687	0.0978	3.6488	0.0107	0	0.0531	0
15	13	0.7229	−1.7297	0.0427	1.5935	0.0043	0	0.0531	0
15	14	−0.147	−2.0863	0.0308	1.1508	0.0011	0	0.0531	0
15	15	−0.4081	−1.1644	0.0228	0.8506	−0.0018	0	0.0531	0
15	16	−1.3762	−0.7377	0.0187	0.6978	−0.0005	0	0	0
16	1	−0.3238	−1.8866	0.0223	0.8307	0.0022	0	0.0383	0
16	2	−0.737	−2.0712	0.0255	0.9531	0.0029	0	0.0383	0
16	3	0.5162	−0.8854	0.0618	2.3044	0.0068	0	0.0383	0
16	4	−0.2988	−2.786	0.0518	1.9344	0.0068	0	0.0383	0
16	5	0.2181	−2.0545	0.046	1.7167	0.0031	0	0.0383	0
16	6	1.0602	−0.8314	0.0728	2.7146	0.0079	0	0.0383	0
16	7	0.0957	−0.6392	0.0297	1.1082	0	0	0.0383	0
16	8	0.0204	1.6265	0.035	1.3063	0.0005	0	0.0383	0
16	9	1.0716	−0.778	0.1026	3.827	0.012	0	0.0383	0
16	10	0.8362	−0.3843	0.0627	2.3403	0.0051	0	0.0383	0
16	11	−0.1288	−1.9691	0.0497	1.8532	0.002	0	0.0383	0
16	12	0.1343	−1.5044	0.055	2.0541	0.0049	0	0.0383	0
16	13	0.429	−2.01	0.0785	2.9277	0.0085	0	0.0383	0
16	14	−1.0174	−1.6418	0.0537	2.005	0.0049	0	0.0383	0
16	15	1.8432	0.7481	0.122	4.5536	0.0109	0	0.0383	0
16	16	2.6729	0.281	0.1635	6.1005	0.0213	0.384	0	0
Temperature:
230 C.
1	1	20.5122	11.752	0.7383	27.1989	0.0999	0.384	0	0
1	2	−0.5534	−1.2706	0.0115	0.4228	0.0074	0	0	0
1	3	−0.3862	−1.1153	−0.0091	−0.3362	0.0007	0	0	0
1	4	20.3694	11.7741	0.7182	26.4567	0.0968	0	0	0.768
1	5	0.5126	0.9775	0.0005	0.0193	−0.0007	0	0	0
1	6	0.538	−0.273	−0.0138	−0.5092	−0.002	0	0	0
1	7	30.5533	19.0026	1.0333	38.0659	0.1385	0.384	0	0
1	8	−0.0401	−0.0595	0.0032	0.1164	0.0012	0	0	0
1	9	−0.1373	−0.8776	−0.024	−0.8845	−0.001	0	0	0
1	10	6.5067	3.4452	0.1909	7.0333	0.0238	0	0	0.768
1	11	0.077	−0.4121	−0.0292	−1.0749	−0.0048	0	0	0
1	12	−0.3715	−0.8872	−0.0219	−0.8077	−0.004	0	0	0
1	13	26.1724	16.1062	0.8511	31.3551	0.1126	0.384	0	0
1	14	0.0813	0.1564	−0.0053	−0.1965	0.0013	0	0	0
1	15	−0.6823	0.1234	−0.0145	−0.5342	−0.0002	0	0	0
1	16	6.0422	3.4535	0.1841	6.7836	0.0224	0	0	0.768
2	1	3.4848	2.1816	0.1088	4.009	0.0136	0	0.1275	0
2	2	0.5403	2.0682	0.0138	0.507	−0.0002	0	0.1275	0
2	3	10.2899	7.8458	0.3465	12.7641	0.0425	0	0.1275	0
2	4	21.3326	14.5433	0.7146	26.3272	0.0931	0	0.1275	0
2	5	13.0906	9.73	0.4281	15.7709	0.0531	0	0.1275	0
2	6	25.9089	17.7979	0.8414	30.9982	0.1067	0	0.1275	0
2	7	19.5485	14.2096	0.6102	22.4782	0.08	0	0.1275	0
2	8	27.4426	18.9183	0.8632	31.7987	0.1139	0	0.1275	0
2	9	11.071	7.6374	0.3388	12.4807	0.0416	0	0.1275	0
2	10	7.8063	6.711	0.2101	7.7386	0.0232	0	0.1275	0
2	11	21.9836	15.8925	0.7133	26.2767	0.0923	0	0.1275	0
2	12	21.4248	14.9353	0.6819	25.1197	0.088	0	0.1275	0
2	13	13.9332	10.1621	0.4422	16.2904	0.0516	0	0.1275	0
2	14	12.1357	9.0183	0.403	14.8477	0.0497	0	0.1275	0
2	15	10.1205	7.3514	0.3359	12.3746	0.0422	0	0.1275	0
2	16	−0.1813	−0.1996	−0.0083	−0.3052	−0.0008	0	0	0
3	1	14.6192	9.6539	0.477	17.5727	0.0598	0	0.1148	0
3	2	3.5237	1.6063	0.1056	3.8917	0.0137	0	0.1148	0
3	3	7.5414	5.7472	0.2505	9.2275	0.0293	0	0.1148	0
3	4	25.6608	16.2436	0.8269	30.4612	0.1087	0	0.1148	0
3	5	13.2052	9.4936	0.4538	16.7197	0.0568	0	0.1148	0
3	6	25.3315	16.7131	0.8179	30.1312	0.1061	0	0.1148	0
3	7	21.3268	13.9191	0.682	25.1235	0.0887	0	0.1148	0
3	8	24.7757	17.4515	0.7954	29.301	0.1012	0	0.1148	0
3	9	8.4714	6.7116	0.2707	9.9741	0.032	0	0.1148	0
3	10	11.8838	8.5049	0.3571	13.1539	0.0407	0	0.1148	0
3	11	20.031	14.4004	0.6352	23.402	0.0805	0	0.1148	0
3	12	19.8788	14.2811	0.6381	23.5091	0.0788	0	0.1148	0
3	13	12.9699	9.8171	0.4046	14.9042	0.0477	0	0.1148	0
3	14	17.4726	12.8596	0.582	21.4404	0.0711	0	0.1148	0
3	15	9.2964	6.3491	0.287	10.574	0.0339	0	0.1148	0
3	16	0.0039	0.2785	−0.0092	−0.3384	−0.0048	0	0	0
4	1	17.3609	12.5782	0.6049	22.2858	0.072	0	0.102	0
4	2	3.8887	3.9128	0.0902	3.3222	0.0077	0	0.102	0
4	3	7.8741	7.2509	0.2413	8.8886	0.0267	0	0.102	0
4	4	24.9061	17.8056	0.7889	29.0621	0.0992	0	0.102	0
4	5	13.5943	11.0916	0.4332	15.9588	0.05	0	0.102	0
4	6	25.7929	19.6971	0.8186	30.1556	0.1001	0	0.102	0
4	7	21.072	14.4215	0.6748	24.8609	0.0869	0	0.102	0
4	8	26.0921	18.743	0.8103	29.8516	0.1023	0	0.102	0
4	9	9.0667	6.8545	0.3023	11.1355	0.0361	0	0.102	0
4	10	9.9682	9.0867	0.3095	11.4025	0.0375	0	0.102	0
4	11	22.5703	17.6942	0.7028	25.892	0.0881	0	0.102	0
4	12	17.6725	13.6191	0.5819	21.4383	0.072	0	0.102	0
4	13	13.3204	11.7478	0.4371	16.1046	0.0501	0	0.102	0
4	14	18.8588	14.1349	0.626	23.0617	0.0749	0	0.102	0
4	15	10.9773	9.4417	0.3661	13.4881	0.0434	0	0.102	0
4	16	25.5043	16.3074	0.8602	31.6906	0.1124	0.384	0	0
5	1	15.726	10.879	0.5349	19.706	0.0654	0	0.0893	0
5	2	1.2361	2.1554	0.0379	1.395	0.0012	0	0.0893	0
5	3	8.2732	7.1702	0.2632	9.6977	0.0305	0	0.0893	0
5	4	23.479	17.3054	0.7815	28.7895	0.0978	0	0.0893	0
5	5	13.4611	8.7548	0.4398	16.2013	0.0532	0	0.0893	0
5	6	24.6516	18.1881	0.8117	29.9015	0.1024	0	0.0893	0
5	7	20.6256	15.1295	0.6933	25.5417	0.0834	0	0.0893	0
5	8	22.0706	16.9093	0.728	26.8185	0.0934	0	0.0893	0
5	9	9.5062	8.3409	0.2942	10.8373	0.036	0	0.0893	0
5	10	9.7534	6.8249	0.3242	11.9447	0.0406	0	0.0893	0
5	11	23.0838	17.321	0.7228	26.6283	0.0902	0	0.0893	0
5	12	13.0683	10.718	0.4431	16.3235	0.0529	0	0.0893	0
5	13	12.4403	9.1189	0.408	15.0297	0.0501	0	0.0893	0
5	14	15.6144	11.8708	0.5015	18.4747	0.0598	0	0.0893	0
5	15	8.013	6.9957	0.2667	9.8269	0.0321	0	0.0893	0
5	16	1.5841	3.1393	0.0592	2.1826	0.0038	0	0	0
6	1	11.9181	7.529	0.4121	15.1809	0.0515	0	0.0765	0
6	2	2.6337	2.1059	0.0447	1.6457	0.0033	0	0.0765	0
6	3	5.4951	5.1434	0.1607	5.9193	0.0161	0	0.0765	0
6	4	23.8763	15.5411	0.7888	29.0607	0.0966	0	0.0765	0
6	5	12.93	10.1219	0.3818	14.0649	0.045	0	0.0765	0
6	6	23.5796	15.9125	0.7649	28.1784	0.0973	0	0.0765	0
6	7	18.9005	15.2143	0.6468	23.829	0.077	0	0.0765	0
6	8	20.3497	13.5583	0.6825	25.1424	0.0825	0	0.0765	0
6	9	11.2224	6.8155	0.3486	12.8407	0.0488	0	0.0765	0
6	10	10.2035	7.9968	0.3412	12.5707	0.0409	0	0.0765	0
6	11	23.4001	17.0529	0.7491	27.5961	0.0963	0	0.0765	0
6	12	9.7991	8.2616	0.3252	11.9814	0.0374	0	0.0765	0
6	13	11.7581	8.3105	0.4047	14.9078	0.0515	0	0.0765	0
6	14	18.0336	13.0945	0.6005	22.1227	0.0726	0	0.0765	0
6	15	7.911	4.3785	0.2682	9.8789	0.0312	0	0.0765	0
6	16	−0.6688	1.4355	−0.0035	−0.1305	−0.0019	0	0	0
7	1	8.2588	5.3884	0.2833	10.4355	0.0335	0	0.0638	0
7	2	0.8857	1.2193	0.0252	0.9302	0.0016	0	0.0638	0
7	3	6.6639	4.2553	0.2108	7.7677	0.0263	0	0.0638	0
7	4	22.5348	14.4689	0.7837	28.8734	0.0978	0	0.0638	0
7	5	12.3747	10.2625	0.4082	15.037	0.0518	0	0.0638	0
7	6	24.0886	16.8609	0.7789	28.6964	0.0959	0	0.0638	0
7	7	19.4243	13.7709	0.6285	23.1531	0.076	0	0.0638	0
7	8	20.9167	14.354	0.6951	25.6082	0.0874	0	0.0638	0
7	9	11.0085	7.0474	0.3181	11.7196	0.0506	0	0.0638	0
7	10	9.8927	8.1601	0.2841	10.4662	0.0307	0	0.0638	0
7	11	22.9498	15.5482	0.7494	27.6082	0.0971	0	0.0638	0
7	12	10.8518	7.6716	0.3566	13.1386	0.0428	0	0.0638	0
7	13	11.1438	7.8195	0.3629	13.3706	0.0434	0	0.0638	0
7	14	13.8746	9.9693	0.4684	17.2575	0.0579	0	0.0638	0
7	15	6.983	6.1175	0.2213	8.1545	0.0244	0	0.0638	0
7	16	5.3562	3.5355	0.2036	7.5023	0.025	0	0	0.768
8	1	5.1472	4.2085	0.1241	4.5708	0.0114	0	0.051	0
8	2	2.6812	0.6825	0.0185	0.6825	−0.0028	0	0.051	0
8	3	4.8568	3.4396	0.1483	5.4617	0.0157	0	0.051	0
8	4	19.2612	15.3513	0.6197	22.8294	0.0741	0	0.051	0
8	5	11.2913	10.0059	0.3626	13.3581	0.0399	0	0.051	0
8	6	20.5183	14.6059	0.6588	24.2717	0.0798	0	0.051	0
8	7	16.4533	12.6987	0.5352	19.7185	0.0653	0	0.051	0
8	8	15.0048	11.2762	0.4823	17.7662	0.0569	0	0.051	0
8	9	13.9254	8.7784	0.3288	12.1131	0.0683	0	0.051	0
8	10	7.8726	7.4388	0.2396	8.8259	0.0244	0	0.051	0
8	11	19.82	15.1827	0.6372	23.4739	0.0765	0	0.051	0
8	12	7.605	6.8751	0.2285	8.4184	0.0281	0	0.051	0
8	13	10.7449	8.7771	0.3532	13.0108	0.0437	0	0.051	0
8	14	9.4537	7.0641	0.335	12.3405	0.0432	0	0.051	0
8	15	4.9948	4.1176	0.165	6.0799	0.0191	0	0.051	0
8	16	0.039	1.3054	0.0022	0.0814	−0.0018	0	0	0
9	1	5.4948	5.2568	0.1619	5.9632	0.0172	0	0.0383	0
9	2	1.2957	1.792	0.0246	0.9071	0.0007	0	0.0383	0
9	3	4.561	3.4219	0.1167	4.3001	0.0112	0	0.0383	0
9	4	18.1494	12.2628	0.6027	22.2032	0.0759	0	0.0383	0
9	5	9.3792	7.0297	0.3096	11.4063	0.0375	0	0.0383	0
9	6	18.4118	12.8378	0.6302	23.2159	0.0763	0	0.0383	0
9	7	16.3053	13.3828	0.5228	19.2604	0.0596	0	0.0383	0
9	8	11.9275	10.3345	0.3942	14.5228	0.0464	0	0.0383	0
9	9	13.8245	7.7844	0.3136	11.5513	0.0738	0	0.0383	0
9	10	5.9945	6.2382	0.161	5.9323	0.0148	0	0.0383	0
9	11	16.467	12.1554	0.5233	19.2796	0.0638	0	0.0383	0
9	12	4.8586	6.0202	0.1535	5.6534	0.0137	0	0.0383	0
9	13	8.9256	6.8906	0.3084	11.3617	0.0373	0	0.0383	0
9	14	6.5689	5.4424	0.1857	6.8397	0.02	0	0.0383	0
9	15	4.0595	3.9488	0.1149	4.2325	0.012	0	0.0383	0
9	16	0.1737	−0.0654	−0.0123	−0.4528	−0.0033	0	0	0
10	1	1.5477	2.4162	0.0571	2.1025	0.0057	0	0.1275	0
10	2	0.7481	0.278	0.0266	0.9802	0.0042	0	0.1275	0
10	3	17.9789	12.2101	0.6266	23.0845	0.0773	0	0.1275	0
10	4	15.7177	12.2677	0.4832	17.8	0.0563	0	0.1275	0
10	5	23.4232	17.8043	0.7802	28.7411	0.0932	0	0.1275	0
10	6	18.8559	14.0032	0.644	23.7233	0.0803	0	0.1275	0
10	7	16.6936	12.534	0.5444	20.0565	0.0655	0	0.1275	0
10	8	15.7358	12.1987	0.5156	18.9943	0.0626	0	0.1275	0
10	9	19.5604	13.1002	0.7006	25.8091	0.0879	0	0.1275	0
10	10	18.0579	13.0064	0.5957	21.9464	0.074	0	0.1275	0
10	11	14.3925	10.1347	0.4699	17.3093	0.0581	0	0.1275	0
10	12	23.9347	15.9894	0.8104	29.854	0.1014	0	0.1275	0
10	13	9.5428	6.0585	0.3205	11.8074	0.0415	0	0.1275	0
10	14	6.0412	4.3478	0.216	7.9578	0.0244	0	0.1275	0
10	15	2.0188	2.7553	0.0713	2.6262	0.0092	0	0.1275	0
10	16	23.9818	15.3099	0.8173	30.1102	0.1051	0.384	0	0
11	1	1.6265	−0.4393	0.0572	2.1077	0.0082	0	0.1126	0
11	2	0.7512	0.0655	0.0158	0.5811	−0.0006	0	0.1126	0
11	3	11.6267	7.1062	0.4011	14.7754	0.0508	0	0.1126	0
11	4	14.9632	10.2139	0.512	18.8615	0.0629	0	0.1126	0
11	5	20.7287	14.0712	0.6984	25.728	0.0888	0	0.1126	0
11	6	22.2788	15.4473	0.7325	26.9837	0.0899	0	0.1126	0
11	7	18.3124	13.0396	0.6421	23.6548	0.0789	0	0.1126	0
11	8	22.0934	15.6671	0.7274	26.7979	0.0885	0	0.1126	0
11	9	22.0321	14.1023	0.7675	28.2737	0.1001	0	0.1126	0
11	10	13.3746	7.6722	0.473	17.424	0.0603	0	0.1126	0
11	11	11.8485	8.1997	0.4037	14.8713	0.0501	0	0.1126	0
11	12	21.6762	14.7974	0.7674	28.2709	0.095	0	0.1126	0
11	13	9.6066	6.771	0.3198	11.7825	0.041	0	0.1126	0
11	14	5.2261	3.1774	0.1451	5.3441	0.0182	0	0.1126	0
11	15	1.1397	1.4718	0.029	1.068	0.0045	0	0.1126	0
11	16	1.7146	−0.1881	0.06	2.2093	0.007	0	0	0
12	1	0.7424	−0.8795	0.0693	2.5545	0.0111	0	0.0978	0
12	2	0.3751	0.6279	0.0316	1.1642	0.0022	0	0.0978	0
12	3	10.7908	6.692	0.3558	13.1083	0.0449	0	0.0978	0
12	4	9.0282	8.0275	0.3374	12.4281	0.0429	0	0.0978	0
12	5	17.5272	11.6688	0.6128	22.5774	0.0768	0	0.0978	0
12	6	16.7422	11.3782	0.5685	20.9454	0.0738	0	0.0978	0
12	7	15.061	11.2786	0.5101	18.7911	0.0642	0	0.0978	0
12	8	7.3694	5.1322	0.2558	9.4242	0.0332	0	0.0978	0
12	9	21.793	14.3754	0.7334	27.018	0.0954	0	0.0978	0
12	10	8.735	5.3347	0.3294	12.1334	0.0442	0	0.0978	0
12	11	6.8362	3.8479	0.2586	9.5255	0.0346	0	0.0978	0
12	12	19.758	12.0896	0.6949	25.5986	0.0882	0	0.0978	0
12	13	4.91	2.0226	0.1761	6.4864	0.0235	0	0.0978	0
12	14	2.3397	1.3074	0.074	2.7266	0.0117	0	0.0978	0
12	15	−0.0988	−1.055	0.028	1.0331	0.0057	0	0.0978	0
12	16	−0.6493	−1.8142	0.0031	0.1125	0.0042	0	0	0
13	1	0.4429	0.1915	0.0431	1.5867	0.0084	0	0.0829	0
13	2	0.7285	−0.4527	0.0242	0.8909	0.0045	0	0.0829	0
13	3	7.4333	3.9871	0.2548	9.3868	0.0323	0	0.0829	0
13	4	10.9401	6.7321	0.404	14.883	0.0536	0	0.0829	0
13	5	14.4732	9.4042	0.4872	17.9486	0.0633	0	0.0829	0
13	6	14.7593	9.7152	0.4959	18.27	0.0626	0	0.0829	0
13	7	11.6134	5.9928	0.4019	14.8073	0.0498	0	0.0829	0
13	8	9.8226	7.3952	0.3336	12.2913	0.0402	0	0.0829	0
13	9	19.1421	12.2144	0.6691	24.6503	0.0908	0	0.0829	0
13	10	8.7276	5.9972	0.2896	10.6673	0.0366	0	0.0829	0
13	11	6.8431	3.0277	0.2592	9.5503	0.0335	0	0.0829	0
13	12	16.1712	11.1574	0.5535	20.3907	0.0686	0	0.0829	0
13	13	4.6027	2.533	0.1557	5.7347	0.0213	0	0.0829	0
13	14	2.6175	2.1368	0.109	4.0151	0.0134	0	0.0829	0
13	15	0.1712	0.1937	0.0256	0.9427	0.0015	0	0.0829	0
13	16	5.2254	3.6667	0.2167	7.9825	0.026	0	0	0.768
14	1	−0.6129	−0.7022	0.0256	0.943	0.0061	0	0.068	0
14	2	−0.0825	0.1999	0.017	0.6261	0.0049	0	0.068	0
14	3	5.4052	6.7553	0.1725	6.3547	0.0192	0	0.068	0
14	4	4.5583	2.1299	0.158	5.8214	0.0202	0	0.068	0
14	5	10.1192	7.5886	0.3644	13.4249	0.0467	0	0.068	0
14	6	4.2773	4.269	0.1697	6.2535	0.0232	0	0.068	0
14	7	5.8243	4.2454	0.206	7.5899	0.0279	0	0.068	0
14	8	4.5156	3.7194	0.166	6.1153	0.0207	0	0.068	0
14	9	15.8111	11.2165	0.5256	19.3644	0.0737	0	0.068	0
14	10	5.4062	3.196	0.1896	6.985	0.0244	0	0.068	0
14	11	3.7866	1.825	0.1438	5.2965	0.0222	0	0.068	0
14	12	7.7545	4.1296	0.2784	10.2559	0.0368	0	0.068	0
14	13	2.8508	2.631	0.1214	4.4727	0.0154	0	0.068	0
14	14	0.5309	−1.0896	0.0675	2.4849	0.0099	0	0.068	0
14	15	0.1398	−1.9674	0.0158	0.5813	0.0012	0	0.068	0
14	16	−0.3316	0.0358	0.01	0.3687	0.0004	0	0	0
15	1	−0.1148	0.1922	0.0092	0.3376	0.0008	0	0.0531	0
15	2	0.1079	0.1039	0.0042	0.1541	0.0032	0	0.0531	0
15	3	3.5717	2.2496	0.1406	5.1802	0.0221	0	0.0531	0
15	4	4.6567	1.8374	0.1474	5.4311	0.0196	0	0.0531	0
15	5	6.8308	3.9469	0.2744	10.1092	0.0376	0	0.0531	0
15	6	7.5086	3.6352	0.2419	8.911	0.0314	0	0.0531	0
15	7	3.6177	2.7378	0.0881	3.2446	0.0122	0	0.0531	0
15	8	6.3617	3.1726	0.1952	7.1899	0.0269	0	0.0531	0
15	9	13.9802	8.5923	0.4839	17.826	0.0689	0	0.0531	0
15	10	4.8923	3.9039	0.1737	6.4005	0.023	0	0.0531	0
15	11	5.59	3.4292	0.1956	7.2047	0.0283	0	0.0531	0
15	12	6.8024	5.5785	0.2192	8.0763	0.0294	0	0.0531	0
15	13	3.7607	2.3756	0.121	4.4593	0.0166	0	0.0531	0
15	14	0.937	1.5442	0.0699	2.5762	0.0097	0	0.0531	0
15	15	0.2832	0.3246	0.02	0.7379	0.0033	0	0.0531	0
15	16	−0.7225	−0.2893	0.0016	0.0571	−0.0006	0	0	0
16	1	−0.0142	−1.1024	0.0215	0.7913	0.0057	0	0.0383	0
16	2	0.4952	−0.4098	0.0194	0.7148	0.0058	0	0.0383	0
16	3	3.2579	1.3122	0.1477	5.4418	0.0221	0	0.0383	0
16	4	1.625	−0.1101	0.1214	4.4707	0.0211	0	0.0383	0
16	5	1.8652	0.6067	0.0939	3.4593	0.0153	0	0.0383	0
16	6	4.8965	3.555	0.1734	6.3862	0.0233	0	0.0383	0
16	7	0.5706	−0.0127	0.0426	1.5679	0.0079	0	0.0383	0
16	8	1.5788	1.8244	0.0682	2.5118	0.0091	0	0.0383	0
16	9	7.3237	3.5992	0.2614	9.63	0.0399	0	0.0383	0
16	10	3.4023	0.894	0.1499	5.5241	0.0224	0	0.0383	0
16	11	1.8143	−0.758	0.0668	2.4619	0.0101	0	0.0383	0
16	12	0.8507	0.6985	0.052	1.9172	0.0098	0	0.0383	0
16	13	3.0836	3.6579	0.1369	5.0426	0.0179	0	0.0383	0
16	14	0.8053	−0.2459	0.0311	1.1471	0.0073	0	0.0383	0
16	15	5.3415	3.7713	0.2488	9.1666	0.0341	0	0.0383	0
16	16	9.4755	5.5863	0.3659	13.4784	0.0487	0.384	0	0
Temperature:
260 C.
1	1	23.9548	12.5586	0.792	28.945	0.1185	0.384	0	0
1	2	−0.1251	−1.1682	0.0079	0.2905	0.0029	0	0	0
1	3	−0.2445	−1.2984	−0.0091	−0.3313	0.0016	0	0	0
1	4	26.223	16.8044	0.8614	31.4805	0.1117	0	0	0.768
1	5	0.5935	1.5609	0.0111	0.4048	0.0008	0	0	0
1	6	0.3452	−0.5656	−0.0202	−0.7401	−0.002	0	0	0
1	7	33.6381	20.613	1.115	40.751	0.161	0.384	0	0
1	8	0.3663	0.721	0.0118	0.4304	0.0043	0	0	0
1	9	−0.3414	0.3286	−0.0389	−1.4226	−0.0089	0	0	0
1	10	16.1672	9.9936	0.5479	20.0238	0.0714	0	0	0.768
1	11	−0.1542	−0.1519	−0.03	−1.095	−0.0036	0	0	0
1	12	−0.706	−0.9411	−0.0392	−1.4334	−0.0032	0	0	0
1	13	31.908	19.6537	1.0424	38.0961	0.1437	0.384	0	0
1	14	0.5711	−0.2625	−0.0125	−0.4566	−0.0012	0	0	0
1	15	−0.5994	−1.1609	−0.025	−0.9131	−0.0045	0	0	0
1	16	13.0157	7.0184	0.4715	17.2323	0.0599	0	0	0.768
2	1	7.6165	4.4571	0.249	9.0986	0.0316	0	0.1275	0
2	2	2.04	1.7045	0.0513	1.8735	0.0074	0	0.1275	0
2	3	19.8301	14.357	0.6798	24.8446	0.0858	0	0.1275	0
2	4	25.5767	16.9766	0.8497	31.0534	0.1122	0	0.1275	0
2	5	19.6461	12.5711	0.6752	24.6783	0.0908	0	0.1275	0
2	6	29.3737	20.6255	0.9524	34.8088	0.1251	0	0.1275	0
2	7	25.3081	17.3872	0.7934	28.9974	0.1065	0	0.1275	0
2	8	31.2784	20.4979	0.9823	35.9021	0.1389	0	0.1275	0
2	9	19.8631	13.7444	0.6352	23.2152	0.0763	0	0.1275	0
2	10	10.4121	7.8726	0.3241	11.845	0.0384	0	0.1275	0
2	11	28.2753	19.8643	0.8954	32.7261	0.116	0	0.1275	0
2	12	28.388	19.6094	0.888	32.4551	0.1133	0	0.1275	0
2	13	21.9441	15.5641	0.6867	25.0976	0.0849	0	0.1275	0
2	14	21.0969	15.4875	0.6762	24.712	0.0815	0	0.1275	0
2	15	17.2387	11.7114	0.5678	20.7519	0.0707	0	0.1275	0
2	16	0.3495	−0.3711	0.005	0.1841	0.0007	0	0	0
3	1	20.2367	13.2497	0.6915	25.2741	0.0869	0	0.1148	0
3	2	8.9669	5.9386	0.2877	10.5137	0.0347	0	0.1148	0
3	3	16.7768	10.897	0.565	20.6503	0.0706	0	0.1148	0
3	4	27.777	18.2759	0.9351	34.1766	0.1287	0	0.1148	0
3	5	20.3263	13.9316	0.6648	24.2965	0.0839	0	0.1148	0
3	6	28.7316	18.8028	0.9427	34.4528	0.1245	0	0.1148	0
3	7	25.4654	18.4277	0.8264	30.2015	0.1095	0	0.1148	0
3	8	29.6117	21.6329	0.9545	34.8833	0.126	0	0.1148	0
3	9	17.2418	12.6896	0.5857	21.4042	0.0712	0	0.1148	0
3	10	19.8929	14.3675	0.6554	23.9547	0.081	0	0.1148	0
3	11	28.1629	17.7133	0.9147	33.4316	0.1189	0	0.1148	0
3	12	25.2171	16.6791	0.7977	29.1554	0.102	0	0.1148	0
3	13	19.4575	14.7466	0.6586	24.0702	0.0828	0	0.1148	0
3	14	26.4424	17.3168	0.8888	32.4841	0.1138	0	0.1148	0
3	15	16.101	11.3039	0.5812	21.2404	0.0742	0	0.1148	0
3	16	−0.023	1.4313	−0.0247	−0.9042	−0.0064	0	0	0
4	1	21.7975	15.4921	0.7711	28.1812	0.0932	0	0.102	0
4	2	10.7163	8.3886	0.3262	11.9235	0.0386	0	0.102	0
4	3	17.1487	14.3548	0.5793	21.1714	0.07	0	0.102	0
4	4	27.6901	18.0677	0.9147	33.4286	0.1231	0	0.102	0
4	5	19.834	14.4675	0.6659	24.3388	0.0858	0	0.102	0
4	6	28.4061	20.4494	0.9351	34.1766	0.1216	0	0.102	0
4	7	25.0251	19.0757	0.8051	29.4259	0.1044	0	0.102	0
4	8	30.1323	21.8658	0.9545	34.8849	0.1285	0	0.102	0
4	9	17.4353	13.7445	0.5888	21.5204	0.0724	0	0.102	0
4	10	18.5879	14.8039	0.6274	22.9309	0.0756	0	0.102	0
4	11	28.8642	21.4484	0.9293	33.9638	0.122	0	0.102	0
4	12	21.4072	15.6073	0.7437	27.1816	0.0938	0	0.102	0
4	13	20.4004	15.2176	0.6641	24.2712	0.084	0	0.102	0
4	14	26.9082	18.8	0.8724	31.8854	0.1143	0	0.102	0
4	15	19.1005	13.9277	0.6384	23.3336	0.0811	0	0.102	0
4	16	29.0091	17.9895	0.9619	35.1545	0.142	0.384	0	0
5	1	19.6008	14.7724	0.6977	25.4997	0.0863	0	0.0893	0
5	2	4.4591	5.8398	0.1267	4.6297	0.0115	0	0.0893	0
5	3	17.4615	13.2093	0.5716	20.8904	0.0684	0	0.0893	0
5	4	27.191	17.9075	0.9098	33.2513	0.121	0	0.0893	0
5	5	19.0595	15.5605	0.6287	22.9776	0.0753	0	0.0893	0
5	6	27.8708	19.2272	0.8978	32.8131	0.1167	0	0.0893	0
5	7	24.4016	19.1467	0.8152	29.7949	0.1021	0	0.0893	0
5	8	27.9965	21.5105	0.9029	32.9989	0.1173	0	0.0893	0
5	9	17.2513	13.7436	0.5629	20.5717	0.0705	0	0.0893	0
5	10	18.4671	13.4843	0.6255	22.8613	0.0758	0	0.0893	0
5	11	29.3804	21.3425	0.9532	34.8381	0.1229	0	0.0893	0
5	12	16.4671	14.1712	0.5223	19.0903	0.0603	0	0.0893	0
5	13	18.5408	14.4036	0.6009	21.9625	0.074	0	0.0893	0
5	14	25.0803	18.6587	0.8426	30.7933	0.1019	0	0.0893	0
5	15	16.054	10.8572	0.5467	19.9812	0.0675	0	0.0893	0
5	16	2.21	2.6719	0.0893	3.2654	0.0093	0	0	0
6	1	17.2143	10.5925	0.5785	21.1428	0.0704	0	0.0765	0
6	2	6.5615	3.8939	0.2245	8.204	0.0283	0	0.0765	0
6	3	14.665	10.1505	0.4705	17.1975	0.0571	0	0.0765	0
6	4	26.914	18.4424	0.9031	33.008	0.1147	0	0.0765	0
6	5	18.3107	13.344	0.6235	22.7882	0.0779	0	0.0765	0
6	6	26.6766	18.1581	0.9136	33.3883	0.1139	0	0.0765	0
6	7	23.7003	15.7944	0.8064	29.4712	0.1026	0	0.0765	0
6	8	26.7761	17.0647	0.8747	31.9669	0.1173	0	0.0765	0
6	9	16.1131	11.9414	0.5207	19.0297	0.0642	0	0.0765	0
6	10	18.9129	14.7068	0.6221	22.7361	0.0735	0	0.0765	0
6	11	29.0675	19.5103	0.9635	35.2139	0.129	0	0.0765	0
6	12	11.7426	10.2734	0.3717	13.5833	0.0422	0	0.0765	0
6	13	16.8626	11.5965	0.5855	21.3985	0.0773	0	0.0765	0
6	14	26.4065	19.0014	0.8963	32.7585	0.1118	0	0.0765	0
6	15	14.603	10.4082	0.4617	16.8728	0.0553	0	0.0765	0
6	16	−0.7718	−0.9228	−0.0099	−0.3607	0.0007	0	0	0
7	1	13.0412	9.5302	0.4162	15.2125	0.0503	0	0.0638	0
7	2	3.8611	2.4286	0.0928	3.392	0.0105	0	0.0638	0
7	3	15.3005	10.0224	0.5176	18.9172	0.0635	0	0.0638	0
7	4	25.9965	17.958	0.8622	31.5124	0.1085	0	0.0638	0
7	5	18.203	14.3266	0.6071	22.1899	0.0739	0	0.0638	0
7	6	26.4572	19.5242	0.898	32.8198	0.1116	0	0.0638	0
7	7	22.8328	16.0377	0.7813	28.5553	0.0978	0	0.0638	0
7	8	26.6147	20.0129	0.8716	31.8557	0.1132	0	0.0638	0
7	9	14.1961	12.1463	0.4578	16.7301	0.0582	0	0.0638	0
7	10	17.8887	13.1344	0.6076	22.2047	0.0718	0	0.0638	0
7	11	29.3	20.7004	0.9421	34.4302	0.1256	0	0.0638	0
7	12	12.7912	9.683	0.3949	14.434	0.0473	0	0.0638	0
7	13	16.1059	10.337	0.5525	20.1938	0.0715	0	0.0638	0
7	14	23.9848	17.1651	0.7971	29.1323	0.0995	0	0.0638	0
7	15	10.2355	6.3735	0.355	12.9727	0.0462	0	0.0638	0
7	16	13.7951	9.0124	0.478	17.4709	0.0607	0	0	0.768
8	1	8.7108	7.6478	0.278	10.1604	0.0318	0	0.051	0
8	2	5.6619	3.0544	0.1607	5.8731	0.0182	0	0.051	0
8	3	12.7243	8.2404	0.4297	15.7034	0.0548	0	0.051	0
8	4	23.1824	15.3102	0.7818	28.5718	0.1032	0	0.051	0
8	5	16.8934	12.5464	0.5477	20.0177	0.0693	0	0.051	0
8	6	23.0844	16.8013	0.786	28.7276	0.0972	0	0.051	0
8	7	21.1268	13.7292	0.7006	25.6053	0.0886	0	0.051	0
8	8	21.8373	14.2275	0.7572	27.6751	0.096	0	0.051	0
8	9	13.5928	9.6006	0.4328	15.8191	0.058	0	0.051	0
8	10	14.5523	10.281	0.4839	17.6837	0.0618	0	0.051	0
8	11	26.6525	18.3392	0.9016	32.9501	0.1139	0	0.051	0
8	12	8.5309	7.1825	0.2649	9.683	0.0303	0	0.051	0
8	13	15.3085	10.76	0.5211	19.0435	0.0676	0	0.051	0
8	14	18.6343	14.2101	0.616	22.5118	0.0767	0	0.051	0
8	15	8.4219	5.8283	0.2782	10.1692	0.0344	0	0.051	0
8	16	−0.0515	0.4898	0.0128	0.4665	0.0006	0	0	0
9	1	7.3166	5.319	0.2691	9.8339	0.0316	0	0.0383	0
9	2	4.4987	1.546	0.1044	3.8148	0.0146	0	0.0383	0
9	3	10.2033	7.0123	0.3423	12.51	0.0448	0	0.0383	0
9	4	21.9197	15.8941	0.7279	26.6038	0.0945	0	0.0383	0
9	5	13.7404	10.7958	0.4389	16.0401	0.0523	0	0.0383	0
9	6	22.0391	16.325	0.7157	26.1572	0.0859	0	0.0383	0
9	7	19.6992	14.7156	0.6399	23.3875	0.0796	0	0.0383	0
9	8	18.8782	13.41	0.6389	23.3487	0.0825	0	0.0383	0
9	9	11.5326	8.0541	0.3741	13.6723	0.0512	0	0.0383	0
9	10	11.4588	7.9653	0.3912	14.2987	0.0499	0	0.0383	0
9	11	24.0261	16.4691	0.8098	29.5975	0.1024	0	0.0383	0
9	12	5.2417	5.2691	0.138	5.0443	0.0148	0	0.0383	0
9	13	13.6632	9.0008	0.4457	16.2885	0.0596	0	0.0383	0
9	14	13.958	10.1125	0.4726	17.2727	0.0588	0	0.0383	0
9	15	7.3577	5.1203	0.2531	9.2493	0.0314	0	0.0383	0
9	16	−0.6656	−0.3365	−0.0192	−0.7029	−0.0013	0	0	0
10	1	4.1613	3.3032	0.1544	5.6446	0.0193	0	0.1275	0
10	2	2.503	1.9852	0.0794	2.9011	0.0086	0	0.1275	0
10	3	22.5185	16.2252	0.777	28.3968	0.0938	0	0.1275	0
10	4	21.9249	17.4869	0.7138	26.0883	0.0819	0	0.1275	0
10	5	25.2635	18.8907	0.8754	31.9941	0.1044	0	0.1275	0
10	6	25.3786	19.7077	0.8305	30.3522	0.0992	0	0.1275	0
10	7	23.279	18.1733	0.7584	27.7191	0.0891	0	0.1275	0
10	8	23.9911	18.2144	0.795	29.0572	0.0985	0	0.1275	0
10	9	27.1738	19.0835	0.9247	33.7964	0.1169	0	0.1275	0
10	10	24.9585	18.3458	0.8669	31.6823	0.1061	0	0.1275	0
10	11	23.4382	17.1163	0.7984	29.1814	0.1007	0	0.1275	0
10	12	27.0826	19.1195	0.8924	32.6135	0.1125	0	0.1275	0
10	13	18.4256	12.7535	0.6262	22.8872	0.0811	0	0.1275	0
10	14	15.4756	10.6861	0.5085	18.5857	0.0641	0	0.1275	0
10	15	5.8605	5.3508	0.2013	7.3589	0.0255	0	0.1275	0
10	16	26.4434	15.6699	0.9053	33.0873	0.1296	0.384	0	0
11	1	3.3631	2.4086	0.1301	4.755	0.0163	0	0.1126	0
11	2	1.1385	1.5047	0.0639	2.3355	0.0058	0	0.1126	0
11	3	18.1923	12.056	0.6322	23.1046	0.0768	0	0.1126	0
11	4	20.8536	14.0326	0.7301	26.6842	0.0894	0	0.1126	0
11	5	25.2787	19.0321	0.8169	29.8542	0.0984	0	0.1126	0
11	6	26.5724	19.0476	0.8949	32.7054	0.1104	0	0.1126	0
11	7	23.8679	17.1511	0.8261	30.1927	0.1024	0	0.1126	0
11	8	27.0578	20.7184	0.9008	32.9204	0.1104	0	0.1126	0
11	9	28.3897	19.3393	0.9733	35.5716	0.1218	0	0.1126	0
11	10	21.8095	15.8474	0.7866	28.7469	0.0975	0	0.1126	0
11	11	21.1677	16.0245	0.7546	27.5785	0.0913	0	0.1126	0
11	12	26.6583	19.4333	0.9012	32.9382	0.1129	0	0.1126	0
11	13	19.2461	13.9305	0.6446	23.5598	0.0791	0	0.1126	0
11	14	13.3117	9.1142	0.4767	17.4229	0.0596	0	0.1126	0
11	15	3.338	4.4882	0.1241	4.5368	0.0112	0	0.1126	0
11	16	1.6855	2.0504	0.0688	2.5135	0.006	0	0	0
12	1	2.9708	2.5243	0.1413	5.1644	0.0173	0	0.0978	0
12	2	2.1159	3.2147	0.0729	2.6644	0.006	0	0.0978	0
12	3	16.9197	12.3294	0.5601	20.4707	0.0661	0	0.0978	0
12	4	16.8097	12.7361	0.5719	20.901	0.0701	0	0.0978	0
12	5	20.7869	17.0843	0.7264	26.5499	0.0844	0	0.0978	0
12	6	22.5089	17.2645	0.7643	27.9321	0.0911	0	0.0978	0
12	7	20.3063	13.5884	0.7135	26.0775	0.0877	0	0.0978	0
12	8	16.2687	11.1505	0.5577	20.3839	0.0703	0	0.0978	0
12	9	26.0301	16.9468	0.8731	31.9104	0.1108	0	0.0978	0
12	10	17.4285	11.5132	0.607	22.186	0.0766	0	0.0978	0
12	11	15.8306	10.5339	0.5491	20.0671	0.069	0	0.0978	0
12	12	22.7247	14.7061	0.7955	29.074	0.0971	0	0.0978	0
12	13	11.2534	7.305	0.4058	14.8324	0.051	0	0.0978	0
12	14	7.4166	3.4671	0.2736	9.9978	0.0337	0	0.0978	0
12	15	1.307	0.3938	0.0689	2.5194	0.0082	0	0.0978	0
12	16	−1.2094	−1.9329	−0.0041	−0.1501	−0.0003	0	0	0
13	1	2.9967	3.7384	0.0553	2.0203	0.0022	0	0.0829	0
13	2	1.7052	1.3563	0.0398	1.4543	0.0027	0	0.0829	0
13	3	13.0887	9.6959	0.4612	16.8547	0.0549	0	0.0829	0
13	4	17.0868	13.3998	0.5915	21.6191	0.0696	0	0.0829	0
13	5	19.7818	15.0495	0.6769	24.7406	0.0833	0	0.0829	0
13	6	21.0147	15.0505	0.716	26.168	0.0861	0	0.0829	0
13	7	18.0319	14.6478	0.6107	22.3182	0.0712	0	0.0829	0
13	8	18.7202	14.921	0.6192	22.63	0.0741	0	0.0829	0
13	9	24.5564	17.2349	0.8727	31.8947	0.1135	0	0.0829	0
13	10	16.4168	13.0312	0.5761	21.0552	0.068	0	0.0829	0
13	11	16.6658	11.451	0.5704	20.8485	0.0687	0	0.0829	0
13	12	19.9683	13.87	0.7112	25.9917	0.0867	0	0.0829	0
13	13	10.9425	8.5671	0.4247	15.5217	0.0556	0	0.0829	0
13	14	9.7737	8.0718	0.3096	11.3139	0.036	0	0.0829	0
13	15	1.7288	1.0718	0.0759	2.7725	0.0082	0	0.0829	0
13	16	10.952	6.7668	0.393	14.3637	0.0488	0	0	0.768
14	1	0.859	0.8081	0.0661	2.4145	0.0076	0	0.068	0
14	2	1.2176	2.4624	0.0396	1.4476	0.0025	0	0.068	0
14	3	10.267	8.591	0.3654	13.3559	0.0408	0	0.068	0
14	4	10.9361	8.2471	0.3609	13.1888	0.0394	0	0.068	0
14	5	15.763	12.2528	0.5463	19.9672	0.0631	0	0.068	0
14	6	12.2511	9.7701	0.4074	14.8894	0.0458	0	0.068	0
14	7	12.7569	8.9769	0.4403	16.0909	0.0523	0	0.068	0
14	8	11.771	10.0769	0.4011	14.6594	0.0473	0	0.068	0
14	9	20.4667	13.9256	0.7145	26.1126	0.0934	0	0.068	0
14	10	11.2785	7.3023	0.4152	15.1763	0.0536	0	0.068	0
14	11	10.3127	6.1338	0.3609	13.1915	0.0461	0	0.068	0
14	12	10.1414	8.3737	0.3548	12.9684	0.0414	0	0.068	0
14	13	7.4485	5.7711	0.2732	9.9858	0.0317	0	0.068	0
14	14	4.6897	3.6728	0.1896	6.9291	0.0206	0	0.068	0
14	15	0.4469	0.4157	0.0425	1.5524	0.0066	0	0.068	0
14	16	0.0205	0.2191	0.0325	1.1895	0.0045	0	0	0
15	1	0.1326	1.2014	0.0213	0.7772	−0.0014	0	0.0531	0
15	2	0.5446	2.0595	0.029	1.0596	−0.0016	0	0.0531	0
15	3	6.4394	4.0672	0.2646	9.6705	0.0317	0	0.0531	0
15	4	8.7498	6.8198	0.3376	12.3395	0.0412	0	0.0531	0
15	5	12.8715	8.7415	0.4617	16.8745	0.0557	0	0.0531	0
15	6	13.4066	9.3322	0.4526	16.5409	0.0568	0	0.0531	0
15	7	8.1085	6.4379	0.237	8.6612	0.0266	0	0.0531	0
15	8	12.9214	9.0713	0.4624	16.9008	0.0559	0	0.0531	0
15	9	19.1264	13.1011	0.6567	23.9995	0.0828	0	0.0531	0
15	10	10.2178	8.3832	0.3465	12.6635	0.0409	0	0.0531	0
15	11	12.0399	9.5234	0.4507	16.4738	0.0536	0	0.0531	0
15	12	9.1992	6.9676	0.3338	12.1989	0.0394	0	0.0531	0
15	13	7.5413	6.3157	0.2885	10.544	0.0368	0	0.0531	0
15	14	4.7466	3.9707	0.2032	7.4265	0.0238	0	0.0531	0
15	15	1.2498	1.3505	0.0593	2.1676	0.0065	0	0.0531	0
15	16	−1.2496	−0.3611	−0.0064	−0.2348	0.0003	0	0	0
16	1	0.2469	0.431	0.0311	1.1382	0.0048	0	0.0383	0
16	2	1.1204	2.4401	0.0624	2.2793	0.0026	0	0.0383	0
16	3	5.6729	3.8623	0.2177	7.9579	0.0269	0	0.0383	0
16	4	5.1165	3.5211	0.2607	9.5268	0.0327	0	0.0383	0
16	5	6.9249	4.6954	0.2462	8.9973	0.0286	0	0.0383	0
16	6	9.5123	6.7076	0.3377	12.3415	0.0392	0	0.0383	0
16	7	3.3103	3.062	0.1141	4.169	0.015	0	0.0383	0
16	8	5.5678	4.0843	0.2158	7.8876	0.0249	0	0.0383	0
16	9	13.2231	9.6653	0.4812	17.5857	0.0603	0	0.0383	0
16	10	6.6341	4.1143	0.2436	8.9035	0.029	0	0.0383	0
16	11	4.5017	2.0396	0.1675	6.1202	0.0201	0	0.0383	0
16	12	0.5165	1.8075	0.0714	2.6096	0.0084	0	0.0383	0
16	13	5.834	2.5756	0.2576	9.4154	0.0338	0	0.0383	0
16	14	1.9456	0.638	0.1291	4.7172	0.0188	0	0.0383	0
16	15	8.6195	6.634	0.3572	13.0562	0.0472	0	0.0383	0
16	16	14.4734	8.8212	0.5143	18.7981	0.0652	0.384	0	0
	CeNO33	CoNO32	FeNO33	HAuNO34	LaNO33	NH42MoO4	NaOH	PdNH32NO22	SUM-
R	real	real	real	real	real	real	real	real	micromols
Temperature
200 C.
1	0	0	0	0	0	0	0	0	0.384
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.768
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.384
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.768
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.384
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.768
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0.125	0	0	0	0	0	0	0.2525
2	0	0	0.125	0	0	0	0	0	0.2525
2	0.125	0	0	0	0	0	0	0	0.2525
2	0	0	0	0	0	0.125	0	0	0.2525
2	0	0	0	0	0	0	0	0.0235	0.151
2	0	0	0	0	0.125	0	0	0	0.2525
2	0	0	0	0.2	0	0	0	0	0.3275
2	0	0	0	0	0	0	0	0	0
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0.1964	0	0	0	0	0	0	0.3112
3	0	0	0.1964	0	0	0	0	0	0.3112
3	0.1964	0	0	0	0	0	0	0	0.3112
3	0	0	0	0	0	0.1964	0	0	0.3112
3	0	0	0	0	0	0	0	0.0369	0.1517
3	0	0	0	0	0.1964	0	0	0	0.3112
3	0	0	0	0.2	0	0	0	0	0.3148
3	0	0	0	0	0	0	0	0	0
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0.2679	0	0	0	0	0	0	0.3699
4	0	0	0.2679	0	0	0	0	0	0.3699
4	0.2679	0	0	0	0	0	0	0	0.3699
4	0	0	0	0	0	0.2679	0	0	0.3699
4	0	0	0	0	0	0	0	0.0504	0.1524
4	0	0	0	0	0.2679	0	0	0	0.3699
4	0	0	0	0.2	0	0	0	0	0.302
4	0	0	0	0	0	0	0	0	0.384
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0.3393	0	0	0	0	0	0	0.4285
5	0	0	0.3393	0	0	0	0	0	0.4285
5	0.3393	0	0	0	0	0	0	0	0.4285
5	0	0	0	0	0	0.3393	0	0	0.4285
5	0	0	0	0	0	0	0	0.0638	0.153
5	0	0	0	0	0.3393	0	0	0	0.4285
5	0	0	0	0.2	0	0	0	0	0.2893
5	0	0	0	0	0	0	0	0	0
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0.4107	0	0	0	0	0	0	0.4872
6	0	0	0.4107	0	0	0	0	0	0.4872
6	0.4107	0	0	0	0	0	0	0	0.4872
6	0	0	0	0	0	0.4107	0	0	0.4872
6	0	0	0	0	0	0	0	0.0772	0.1537
6	0	0	0	0	0.4107	0	0	0	0.4872
6	0	0	0	0.2	0	0	0	0	0.2765
6	0	0	0	0	0	0	0	0	0
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0.4821	0	0	0	0	0	0	0.5459
7	0	0	0.4821	0	0	0	0	0	0.5459
7	0.4821	0	0	0	0	0	0	0	0.5459
7	0	0	0	0	0	0.4821	0	0	0.5459
7	0	0	0	0	0	0	0	0.0906	0.1544
7	0	0	0	0	0.4821	0	0	0	0.5459
7	0	0	0	0.2	0	0	0	0	0.2638
7	0	0	0	0	0	0	0	0	0.768
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0.5536	0	0	0	0	0	0	0.6046
8	0	0	0.5536	0	0	0	0	0	0.6046
8	0.5536	0	0	0	0	0	0	0	0.6046
8	0	0	0	0	0	0.5536	0	0	0.6046
8	0	0	0	0	0	0	0	0.1041	0.1551
8	0	0	0	0	0.5536	0	0	0	0.6046
8	0	0	0	0.2	0	0	0	0	0.251
8	0	0	0	0	0	0	0	0	0
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0.625	0	0	0	0	0	0	0.6633
9	0	0	0.625	0	0	0	0	0	0.6633
9	0.625	0	0	0	0	0	0	0	0.6633
9	0	0	0	0	0	0.625	0	0	0.6633
9	0	0	0	0	0	0	0	0.1175	0.1558
9	0	0	0	0	0.625	0	0	0	0.6633
9	0	0	0	0.2	0	0	0	0	0.2383
9	0	0	0	0	0	0	0	0	0
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0.125	0	0	0	0	1.25	0	1.5025
10	0	0	0.125	0	0	0	1.25	0	1.5025
10	0.125	0	0	0	0	0	1.25	0	1.5025
10	0	0	0	0	0	0.125	1.25	0	1.5025
10	0	0	0	0	0	0	1.25	0.0235	1.401
10	0	0	0	0	0.125	0	1.25	0	1.5025
10	0	0	0	0.2	0	0	1.25	0	1.5775
10	0	0	0	0	0	0	0	0	0.384
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0.2083	0	0	0	0	1.25	0	1.571
11	0	0	0.2083	0	0	0	1.25	0	1.571
11	0.2083	0	0	0	0	0	1.25	0	1.571
11	0	0	0	0	0	0.2083	1.25	0	1.571
11	0	0	0	0	0	0	1.25	0.0392	1.4018
11	0	0	0	0	0.2083	0	1.25	0	1.571
11	0	0	0	0.2	0	0	1.25	0	1.5626
11	0	0	0	0	0	0	0	0	0
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0.2917	0	0	0	0	1.25	0	1.6394
12	0	0	0.2917	0	0	0	1.25	0	1.6394
12	0.2917	0	0	0	0	0	1.25	0	1.6394
12	0	0	0	0	0	0.2917	1.25	0	1.6394
12	0	0	0	0	0	0	1.25	0.0548	1.4026
12	0	0	0	0	0.2917	0	1.25	0	1.6394
12	0	0	0	0.2	0	0	1.25	0	1.5478
12	0	0	0	0	0	0	0	0	0
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0.375	0	0	0	0	1.25	0	1.7079
13	0	0	0.375	0	0	0	1.25	0	1.7079
13	0.375	0	0	0	0	0	1.25	0	1.7079
13	0	0	0	0	0	0.375	1.25	0	1.7079
13	0	0	0	0	0	0	1.25	0.0705	1.4034
13	0	0	0	0	0.375	0	1.25	0	1.7079
13	0	0	0	0.2	0	0	1.25	0	1.5329
13	0	0	0	0	0	0	0	0	0.768
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0.4583	0	0	0	0	1.25	0	1.7763
14	0	0	0.4583	0	0	0	1.25	0	1.7763
14	0.4583	0	0	0	0	0	1.25	0	1.7763
14	0	0	0	0	0	0.4583	1.25	0	1.7763
14	0	0	0	0	0	0	1.25	0.0862	1.4042
14	0	0	0	0	0.4583	0	1.25	0	1.7763
14	0	0	0	0.2	0	0	1.25	0	1.518
14	0	0	0	0	0	0	0	0	0
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0.5417	0	0	0	0	1.25	0	1.8448
15	0	0	0.5417	0	0	0	1.25	0	1.8448
15	0.5417	0	0	0	0	0	1.25	0	1.8448
15	0	0	0	0	0	0.5417	1.25	0	1.8448
15	0	0	0	0	0	0	1.25	0.1018	1.405
15	0	0	0	0	0.5417	0	1.25	0	1.8448
15	0	0	0	0.2	0	0	1.25	0	1.5031
15	0	0	0	0	0	0	0	0	0
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0.625	0	0	0	0	1.25	0	1.9133
16	0	0	0.625	0	0	0	1.25	0	1.9133
16	0.625	0	0	0	0	0	1.25	0	1.9133
16	0	0	0	0	0	0.625	1.25	0	1.9133
16	0	0	0	0	0	0	1.25	0.1175	1.4058
16	0	0	0	0	0.625	0	1.25	0	1.9133
16	0	0	0	0.2	0	0	1.25	0	1.4883
16	0	0	0	0	0	0	0	0	0.384
Temperature
230 C.
1	0	0	0	0	0	0	0	0	0.384
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.768
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.384
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.768
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.384
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.768
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0.125	0	0	0	0	0	0	0.2525
2	0	0	0.125	0	0	0	0	0	0.2525
2	0.125	0	0	0	0	0	0	0	0.2525
2	0	0	0	0	0	0.125	0	0	0.2525
2	0	0	0	0	0	0	0	0.0235	0.151
2	0	0	0	0	0.125	0	0	0	0.2525
2	0	0	0	0.2	0	0	0	0	0.3275
2	0	0	0	0	0	0	0	0	0
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0.1964	0	0	0	0	0	0	0.3112
3	0	0	0.1964	0	0	0	0	0	0.3112
3	0.1964	0	0	0	0	0	0	0	0.3112
3	0	0	0	0	0	0.1964	0	0	0.3112
3	0	0	0	0	0	0	0	0.0369	0.1517
3	0	0	0	0	0.1964	0	0	0	0.3112
3	0	0	0	0.2	0	0	0	0	0.3148
3	0	0	0	0	0	0	0	0	0
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0.2679	0	0	0	0	0	0	0.3699
4	0	0	0.2679	0	0	0	0	0	0.3699
4	0.2679	0	0	0	0	0	0	0	0.3699
4	0	0	0	0	0	0.2679	0	0	0.3699
4	0	0	0	0	0	0	0	0.0504	0.1524
4	0	0	0	0	0.2679	0	0	0	0.3699
4	0	0	0	0.2	0	0	0	0	0.302
4	0	0	0	0	0	0	0	0	0.384
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0.3393	0	0	0	0	0	0	0.4285
5	0	0	0.3393	0	0	0	0	0	0.4285
5	0.3393	0	0	0	0	0	0	0	0.4285
5	0	0	0	0	0	0.3393	0	0	0.4285
5	0	0	0	0	0	0	0	0.0638	0.153
5	0	0	0	0	0.3393	0	0	0	0.4285
5	0	0	0	0.2	0	0	0	0	0.2893
5	0	0	0	0	0	0	0	0	0
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0.4107	0	0	0	0	0	0	0.4872
6	0	0	0.4107	0	0	0	0	0	0.4872
6	0.4107	0	0	0	0	0	0	0	0.4872
6	0	0	0	0	0	0.4107	0	0	0.4872
6	0	0	0	0	0	0	0	0.0772	0.1537
6	0	0	0	0	0.4107	0	0	0	0.4872
6	0	0	0	0.2	0	0	0	0	0.2765
6	0	0	0	0	0	0	0	0	0
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0.4821	0	0	0	0	0	0	0.5459
7	0	0	0.4821	0	0	0	0	0	0.5459
7	0.4821	0	0	0	0	0	0	0	0.5459
7	0	0	0	0	0	0.4821	0	0	0.5459
7	0	0	0	0	0	0	0	0.0906	0.1544
7	0	0	0	0	0.4821	0	0	0	0.5459
7	0	0	0	0.2	0	0	0	0	0.2638
7	0	0	0	0	0	0	0	0	0.768
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0.5536	0	0	0	0	0	0	0.6046
8	0	0	0.5536	0	0	0	0	0	0.6046
8	0.5536	0	0	0	0	0	0	0	0.6046
8	0	0	0	0	0	0.5536	0	0	0.6046
8	0	0	0	0	0	0	0	0.1041	0.1551
8	0	0	0	0	0.5536	0	0	0	0.6046
8	0	0	0	0.2	0	0	0	0	0.251
8	0	0	0	0	0	0	0	0	0
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0.625	0	0	0	0	0	0	0.6633
9	0	0	0.625	0	0	0	0	0	0.6633
9	0.625	0	0	0	0	0	0	0	0.6633
9	0	0	0	0	0	0.625	0	0	0.6633
9	0	0	0	0	0	0	0	0.1175	0.1558
9	0	0	0	0	0.625	0	0	0	0.6633
9	0	0	0	0.2	0	0	0	0	0.2383
9	0	0	0	0	0	0	0	0	0
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0.125	0	0	0	0	1.25	0	1.5025
10	0	0	0.125	0	0	0	1.25	0	1.5025
10	0.125	0	0	0	0	0	1.25	0	1.5025
10	0	0	0	0	0	0.125	1.25	0	1.5025
10	0	0	0	0	0	0	1.25	0.0235	1.401
10	0	0	0	0	0.125	0	1.25	0	1.5025
10	0	0	0	0.2	0	0	1.25	0	1.5775
10	0	0	0	0	0	0	0	0	0.384
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0.2083	0	0	0	0	1.25	0	1.571
11	0	0	0.2083	0	0	0	1.25	0	1.571
11	0.2083	0	0	0	0	0	1.25	0	1.571
11	0	0	0	0	0	0.2083	1.25	0	1.571
11	0	0	0	0	0	0	1.25	0.0392	1.4018
11	0	0	0	0	0.2083	0	1.25	0	1.571
11	0	0	0	0.2	0	0	1.25	0	1.5626
11	0	0	0	0	0	0	0	0	0
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0.2917	0	0	0	0	1.25	0	1.6394
12	0	0	0.2917	0	0	0	1.25	0	1.6394
12	0.2917	0	0	0	0	0	1.25	0	1.6394
12	0	0	0	0	0	0.2917	1.25	0	1.6394
12	0	0	0	0	0	0	1.25	0.0548	1.4026
12	0	0	0	0	0.2917	0	1.25	0	1.6394
12	0	0	0	0.2	0	0	1.25	0	1.5478
12	0	0	0	0	0	0	0	0	0
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0.375	0	0	0	0	1.25	0	1.7079
13	0	0	0.375	0	0	0	1.25	0	1.7079
13	0.375	0	0	0	0	0	1.25	0	1.7079
13	0	0	0	0	0	0.375	1.25	0	1.7079
13	0	0	0	0	0	0	1.25	0.0705	1.4034
13	0	0	0	0	0.375	0	1.25	0	1.7079
13	0	0	0	0.2	0	0	1.25	0	1.5329
13	0	0	0	0	0	0	0	0	0.768
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0.4583	0	0	0	0	1.25	0	1.7763
14	0	0	0.4583	0	0	0	1.25	0	1.7763
14	0.4583	0	0	0	0	0	1.25	0	1.7763
14	0	0	0	0	0	0.4583	1.25	0	1.7763
14	0	0	0	0	0	0	1.25	0.0862	1.4042
14	0	0	0	0	0.4583	0	1.25	0	1.7763
14	0	0	0	0.2	0	0	1.25	0	1.518
14	0	0	0	0	0	0	0	0	0
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0.5417	0	0	0	0	1.25	0	1.8448
15	0	0	0.5417	0	0	0	1.25	0	1.8448
15	0.5417	0	0	0	0	0	1.25	0	1.8448
15	0	0	0	0	0	0.5417	1.25	0	1.8448
15	0	0	0	0	0	0	1.25	0.1018	1.405
15	0	0	0	0	0.5417	0	1.25	0	1.8448
15	0	0	0	0.2	0	0	1.25	0	1.5031
15	0	0	0	0	0	0	0	0	0
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0.625	0	0	0	0	1.25	0	1.9133
16	0	0	0.625	0	0	0	1.25	0	1.9133
16	0.625	0	0	0	0	0	1.25	0	1.9133
16	0	0	0	0	0	0.625	1.25	0	1.9133
16	0	0	0	0	0	0	1.25	0.1175	1.4058
16	0	0	0	0	0.625	0	1.25	0	1.9133
16	0	0	0	0.2	0	0	1.25	0	1.4883
16	0	0	0	0	0	0	0	0	0.384
Temperature
260 C.
1	0	0	0	0	0	0	0	0	0.384
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.768
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.384
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.768
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.384
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0.768
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0	0	0	0	0	0	0	0.1275
2	0	0.125	0	0	0	0	0	0	0.2525
2	0	0	0.125	0	0	0	0	0	0.2525
2	0.125	0	0	0	0	0	0	0	0.2525
2	0	0	0	0	0	0.125	0	0	0.2525
2	0	0	0	0	0	0	0	0.0235	0.151
2	0	0	0	0	0.125	0	0	0	0.2525
2	0	0	0	0.2	0	0	0	0	0.3275
2	0	0	0	0	0	0	0	0	0
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0	0	0	0	0	0	0	0.1148
3	0	0.1964	0	0	0	0	0	0	0.3112
3	0	0	0.1964	0	0	0	0	0	0.3112
3	0.1964	0	0	0	0	0	0	0	0.3112
3	0	0	0	0	0	0.1964	0	0	0.3112
3	0	0	0	0	0	0	0	0.0369	0.1517
3	0	0	0	0	0.1964	0	0	0	0.3112
3	0	0	0	0.2	0	0	0	0	0.3148
3	0	0	0	0	0	0	0	0	0
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0	0	0	0	0	0	0	0.102
4	0	0.2679	0	0	0	0	0	0	0.3699
4	0	0	0.2679	0	0	0	0	0	0.3699
4	0.2679	0	0	0	0	0	0	0	0.3699
4	0	0	0	0	0	0.2679	0	0	0.3699
4	0	0	0	0	0	0	0	0.0504	0.1524
4	0	0	0	0	0.2679	0	0	0	0.3699
4	0	0	0	0.2	0	0	0	0	0.302
4	0	0	0	0	0	0	0	0	0.384
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0	0	0	0	0	0	0	0.0893
5	0	0.3393	0	0	0	0	0	0	0.4285
5	0	0	0.3393	0	0	0	0	0	0.4285
5	0.3393	0	0	0	0	0	0	0	0.4285
5	0	0	0	0	0	0.3393	0	0	0.4285
5	0	0	0	0	0	0	0	0.0638	0.153
5	0	0	0	0	0.3393	0	0	0	0.4285
5	0	0	0	0.2	0	0	0	0	0.2893
5	0	0	0	0	0	0	0	0	0
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0	0	0	0	0	0	0	0.0765
6	0	0.4107	0	0	0	0	0	0	0.4872
6	0	0	0.4107	0	0	0	0	0	0.4872
6	0.4107	0	0	0	0	0	0	0	0.4872
6	0	0	0	0	0	0.4107	0	0	0.4872
6	0	0	0	0	0	0	0	0.0772	0.1537
6	0	0	0	0	0.4107	0	0	0	0.4872
6	0	0	0	0.2	0	0	0	0	0.2765
6	0	0	0	0	0	0	0	0	0
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0	0	0	0	0	0	0	0.0638
7	0	0.4821	0	0	0	0	0	0	0.5459
7	0	0	0.4821	0	0	0	0	0	0.5459
7	0.4821	0	0	0	0	0	0	0	0.5459
7	0	0	0	0	0	0.4821	0	0	0.5459
7	0	0	0	0	0	0	0	0.0906	0.1544
7	0	0	0	0	0.4821	0	0	0	0.5459
7	0	0	0	0.2	0	0	0	0	0.2638
7	0	0	0	0	0	0	0	0	0.768
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0	0	0	0	0	0	0	0.051
8	0	0.5536	0	0	0	0	0	0	0.6046
8	0	0	0.5536	0	0	0	0	0	0.6046
8	0.5536	0	0	0	0	0	0	0	0.6046
8	0	0	0	0	0	0.5536	0	0	0.6046
8	0	0	0	0	0	0	0	0.1041	0.1551
8	0	0	0	0	0.5536	0	0	0	0.6046
8	0	0	0	0.2	0	0	0	0	0.251
8	0	0	0	0	0	0	0	0	0
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0	0	0	0	0	0	0	0.0383
9	0	0.625	0	0	0	0	0	0	0.6633
9	0	0	0.625	0	0	0	0	0	0.6633
9	0.625	0	0	0	0	0	0	0	0.6633
9	0	0	0	0	0	0.625	0	0	0.6633
9	0	0	0	0	0	0	0	0.1175	0.1558
9	0	0	0	0	0.625	0	0	0	0.6633
9	0	0	0	0.2	0	0	0	0	0.2383
9	0	0	0	0	0	0	0	0	0
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0	0	0	0	0	1.25	0	1.3775
10	0	0.125	0	0	0	0	1.25	0	1.5025
10	0	0	0.125	0	0	0	1.25	0	1.5025
10	0.125	0	0	0	0	0	1.25	0	1.5025
10	0	0	0	0	0	0.125	1.25	0	1.5025
10	0	0	0	0	0	0	1.25	0.0235	1.401
10	0	0	0	0	0.125	0	1.25	0	1.5025
10	0	0	0	0.2	0	0	1.25	0	1.5775
10	0	0	0	0	0	0	0	0	0.384
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0	0	0	0	0	1.25	0	1.3626
11	0	0.2083	0	0	0	0	1.25	0	1.571
11	0	0	0.2083	0	0	0	1.25	0	1.571
11	0.2083	0	0	0	0	0	1.25	0	1.571
11	0	0	0	0	0	0.2083	1.25	0	1.571
11	0	0	0	0	0	0	1.25	0.0392	1.4018
11	0	0	0	0	0.2083	0	1.25	0	1.571
11	0	0	0	0.2	0	0	1.25	0	1.5626
11	0	0	0	0	0	0	0	0	0
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0	0	0	0	0	1.25	0	1.3478
12	0	0.2917	0	0	0	0	1.25	0	1.6394
12	0	0	0.2917	0	0	0	1.25	0	1.6394
12	0.2917	0	0	0	0	0	1.25	0	1.6394
12	0	0	0	0	0	0.2917	1.25	0	1.6394
12	0	0	0	0	0	0	1.25	0.0548	1.4026
12	0	0	0	0	0.2917	0	1.25	0	1.6394
12	0	0	0	0.2	0	0	1.25	0	1.5478
12	0	0	0	0	0	0	0	0	0
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0	0	0	0	0	1.25	0	1.3329
13	0	0.375	0	0	0	0	1.25	0	1.7079
13	0	0	0.375	0	0	0	1.25	0	1.7079
13	0.375	0	0	0	0	0	1.25	0	1.7079
13	0	0	0	0	0	0.375	1.25	0	1.7079
13	0	0	0	0	0	0	1.25	0.0705	1.4034
13	0	0	0	0	0.375	0	1.25	0	1.7079
13	0	0	0	0.2	0	0	1.25	0	1.5329
13	0	0	0	0	0	0	0	0	0.768
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0	0	0	0	0	1.25	0	1.318
14	0	0.4583	0	0	0	0	1.25	0	1.7763
14	0	0	0.4583	0	0	0	1.25	0	1.7763
14	0.4583	0	0	0	0	0	1.25	0	1.7763
14	0	0	0	0	0	0.4583	1.25	0	1.7763
14	0	0	0	0	0	0	1.25	0.0862	1.4042
14	0	0	0	0	0.4583	0	1.25	0	1.7763
14	0	0	0	0.2	0	0	1.25	0	1.518
14	0	0	0	0	0	0	0	0	0
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0	0	0	0	0	1.25	0	1.3031
15	0	0.5417	0	0	0	0	1.25	0	1.8448
15	0	0	0.5417	0	0	0	1.25	0	1.8448
15	0.5417	0	0	0	0	0	1.25	0	1.8448
15	0	0	0	0	0	0.5417	1.25	0	1.8448
15	0	0	0	0	0	0	1.25	0.1018	1.405
15	0	0	0	0	0.5417	0	1.25	0	1.8448
15	0	0	0	0.2	0	0	1.25	0	1.5031
15	0	0	0	0	0	0	0	0	0
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0	0	0	0	0	1.25	0	1.2883
16	0	0.625	0	0	0	0	1.25	0	1.9133
16	0	0	0.625	0	0	0	1.25	0	1.9133
16	0.625	0	0	0	0	0	1.25	0	1.9133
16	0	0	0	0	0	0.625	1.25	0	1.9133
16	0	0	0	0	0	0	1.25	0.1175	1.4058
16	0	0	0	0	0.625	0	1.25	0	1.9133
16	0	0	0	0.2	0	0	1.25	0	1.4883
16	0	0	0	0	0	0	0	0	0.384
	mol %	mol %	mol %	mol %	mol %	mol %	mol %	mol %	mol %	mol %
R	Pt	shift	Ce	Co	Fe	Au	La	Mo	Na	Pd
Temperature
200 C.
1	100	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	100	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	100	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	100	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	100	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	100	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	50.5	0	0	49.5	0	0	0	0	0	0
2	50.5	0	0	0	49.5	0	0	0	0	0
2	50.5	0	49.5	0	0	0	0	0	0	0
2	50.5	0	0	0	0	0	0	49.5	0	0
2	84.44	0	0	0	0	0	0	0	0	15.56
2	50.5	0	0	0	0	0	49.5	0	0	0
2	38.93	0	0	0	0	61.07	0	0	0	0
2	0	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	36.88	0	0	63.12	0	0	0	0	0	0
3	36.88	0	0	0	63.12	0	0	0	0	0
3	36.88	0	63.12	0	0	0	0	0	0	0
3	36.88	0	0	0	0	0	0	63.12	0	0
3	75.65	0	0	0	0	0	0	0	0	24.35
3	36.88	0	0	0	0	0	63.12	0	0	0
3	36.46	0	0	0	0	63.54	0	0	0	0
3	0	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	27.58	0	0	72.42	0	0	0	0	0	0
4	27.58	0	0	0	72.42	0	0	0	0	0
4	27.58	0	72.42	0	0	0	0	0	0	0
4	27.58	0	0	0	0	0	0	72.42	0	0
4	66.95	0	0	0	0	0	0	0	0	33.05
4	27.58	0	0	0	0	0	72.42	0	0	0
4	33.77	0	0	0	0	66.23	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	20.83	0	0	79.17	0	0	0	0	0	0
5	20.83	0	0	0	79.17	0	0	0	0	0
5	20.83	0	79.17	0	0	0	0	0	0	0
5	20.83	0	0	0	0	0	0	79.17	0	0
5	58.32	0	0	0	0	0	0	0	0	41.68
5	20.83	0	0	0	0	0	79.17	0	0	0
5	30.86	0	0	0	0	69.14	0	0	0	0
5	0	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	15.7	0	0	84.3	0	0	0	0	0	0
6	15.7	0	0	0	84.3	0	0	0	0	0
6	15.7	0	84.3	0	0	0	0	0	0	0
6	15.7	0	0	0	0	0	0	84.3	0	0
6	49.77	0	0	0	0	0	0	0	0	50.23
6	15.7	0	0	0	0	0	84.3	0	0	0
6	27.67	0	0	0	0	72.33	0	0	0	0
6	0	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	11.68	0	0	88.32	0	0	0	0	0	0
7	11.68	0	0	0	88.32	0	0	0	0	0
7	11.68	0	88.32	0	0	0	0	0	0	0
7	11.68	0	0	0	0	0	0	88.32	0	0
7	41.29	0	0	0	0	0	0	0	0	58.71
7	11.68	0	0	0	0	0	88.32	0	0	0
7	24.17	0	0	0	0	75.83	0	0	0	0
7	0	100	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	8.44	0	0	91.56	0	0	0	0	0	0
8	8.44	0	0	0	91.56	0	0	0	0	0
8	8.44	0	91.56	0	0	0	0	0	0	0
8	8.44	0	0	0	0	0	0	91.56	0	0
8	32.89	0	0	0	0	0	0	0	0	67.11
8	8.44	0	0	0	0	0	91.56	0	0	0
8	20.32	0	0	0	0	79.68	0	0	0	0
8	0	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	5.77	0	0	94.23	0	0	0	0	0	0
9	5.77	0	0	0	94.23	0	0	0	0	0
9	5.77	0	94.23	0	0	0	0	0	0	0
9	5.77	0	0	0	0	0	0	94.23	0	0
9	24.56	0	0	0	0	0	0	0	0	75.44
9	5.77	0	0	0	0	0	94.23	0	0	0
9	16.05	0	0	0	0	83.95	0	0	0	0
9	0	0	0	0	0	0	0	0	0	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	8.49	0	0	8.32	0	0	0	0	83.19	0
10	8.49	0	0	0	8.32	0	0	0	83.19	0
10	8.49	0	8.32	0	0	0	0	0	83.19	0
10	8.49	0	0	0	0	0	0	8.32	83.19	0
10	9.1	0	0	0	0	0	0	0	89.22	1.68
10	8.49	0	0	0	0	0	8.32	0	83.19	0
10	8.08	0	0	0	0	12.68	0	0	79.24	0
10	100	0	0	0	0	0	0	0	0	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	7.17	0	0	13.26	0	0	0	0	79.57	0
11	7.17	0	0	0	13.26	0	0	0	79.57	0
11	7.17	0	13.26	0	0	0	0	0	79.57	0
11	7.17	0	0	0	0	0	0	13.26	79.57	0
11	8.03	0	0	0	0	0	0	0	89.17	2.79
11	7.17	0	0	0	0	0	13.26	0	79.57	0
11	7.21	0	0	0	0	12.8	0	0	79.99	0
11	0	0	0	0	0	0	0	0	0	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	5.96	0	0	17.79	0	0	0	0	76.25	0
12	5.96	0	0	0	17.79	0	0	0	76.25	0
12	5.96	0	17.79	0	0	0	0	0	76.25	0
12	5.96	0	0	0	0	0	0	17.79	76.25	0
12	6.97	0	0	0	0	0	0	0	89.12	3.91
12	5.96	0	0	0	0	0	17.79	0	76.25	0
12	6.32	0	0	0	0	12.92	0	0	80.76	0
12	0	0	0	0	0	0	0	0	0	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	4.85	0	0	21.96	0	0	0	0	73.19	0
13	4.85	0	0	0	21.96	0	0	0	73.19	0
13	4.85	0	21.96	0	0	0	0	0	73.19	0
13	4.85	0	0	0	0	0	0	21.96	73.19	0
13	5.91	0	0	0	0	0	0	0	89.07	5.02
13	4.85	0	0	0	0	0	21.96	0	73.19	0
13	5.41	0	0	0	0	13.05	0	0	81.55	0
13	0	100	0	0	0	0	0	0	0	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	3.83	0	0	25.8	0	0	0	0	70.37	0
14	3.83	0	0	0	25.8	0	0	0	70.37	0
14	3.83	0	25.8	0	0	0	0	0	70.37	0
14	3.83	0	0	0	0	0	0	25.8	70.37	0
14	4.84	0	0	0	0	0	0	0	89.02	6.14
14	3.83	0	0	0	0	0	25.8	0	70.37	0
14	4.48	0	0	0	0	13.18	0	0	82.35	0
14	0	0	0	0	0	0	0	0	0	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	2.88	0	0	29.36	0	0	0	0	67.76	0
15	2.88	0	0	0	29.36	0	0	0	67.76	0
15	2.88	0	29.36	0	0	0	0	0	67.76	0
15	2.88	0	0	0	0	0	0	29.36	67.76	0
15	3.78	0	0	0	0	0	0	0	88.97	7.25
15	2.88	0	0	0	0	0	29.36	0	67.76	0
15	3.53	0	0	0	0	13.31	0	0	83.16	0
15	0	0	0	0	0	0	0	0	0	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2	0	0	32.67	0	0	0	0	65.33	0
16	2	0	0	0	32.67	0	0	0	65.33	0
16	2	0	32.67	0	0	0	0	0	65.33	0
16	2	0	0	0	0	0	0	32.67	65.33	0
16	2.72	0	0	0	0	0	0	0	88.92	8.36
16	2	0	0	0	0	0	32.67	0	65.33	0
16	2.57	0	0	0	0	13.44	0	0	83.99	0
16	100	0	0	0	0	0	0	0	0	0
Temperature
230 C.
1	100	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	100	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	100	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	100	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	100	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	100	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	50.5	0	0	49.5	0	0	0	0	0	0
2	50.5	0	0	0	49.5	0	0	0	0	0
2	50.5	0	49.5	0	0	0	0	0	0	0
2	50.5	0	0	0	0	0	0	49.5	0	0
2	84.44	0	0	0	0	0	0	0	0	15.56
2	50.5	0	0	0	0	0	49.5	0	0	0
2	38.93	0	0	0	0	61.07	0	0	0	0
2	0	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	36.88	0	0	63.12	0	0	0	0	0	0
3	36.88	0	0	0	63.12	0	0	0	0	0
3	36.88	0	63.12	0	0	0	0	0	0	0
3	36.88	0	0	0	0	0	0	63.12	0	0
3	75.65	0	0	0	0	0	0	0	0	24.35
3	36.88	0	0	0	0	0	63.12	0	0	0
3	36.46	0	0	0	0	63.54	0	0	0	0
3	0	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	27.58	0	0	72.42	0	0	0	0	0	0
4	27.58	0	0	0	72.42	0	0	0	0	0
4	27.58	0	72.42	0	0	0	0	0	0	0
4	27.58	0	0	0	0	0	0	72.42	0	0
4	66.95	0	0	0	0	0	0	0	0	33.05
4	27.58	0	0	0	0	0	72.42	0	0	0
4	33.77	0	0	0	0	66.23	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	20.83	0	0	79.17	0	0	0	0	0	0
5	20.83	0	0	0	79.17	0	0	0	0	0
5	20.83	0	79.17	0	0	0	0	0	0	0
5	20.83	0	0	0	0	0	0	79.17	0	0
5	58.32	0	0	0	0	0	0	0	0	41.68
5	20.83	0	0	0	0	0	79.17	0	0	0
5	30.86	0	0	0	0	69.14	0	0	0	0
5	0	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	15.7	0	0	84.3	0	0	0	0	0	0
6	15.7	0	0	0	84.3	0	0	0	0	0
6	15.7	0	84.3	0	0	0	0	0	0	0
6	15.7	0	0	0	0	0	0	84.3	0	0
6	49.77	0	0	0	0	0	0	0	0	50.23
6	15.7	0	0	0	0	0	84.3	0	0	0
6	27.67	0	0	0	0	72.33	0	0	0	0
6	0	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	11.68	0	0	88.32	0	0	0	0	0	0
7	11.68	0	0	0	88.32	0	0	0	0	0
7	11.68	0	88.32	0	0	0	0	0	0	0
7	11.68	0	0	0	0	0	0	88.32	0	0
7	41.29	0	0	0	0	0	0	0	0	58.71
7	11.68	0	0	0	0	0	88.32	0	0	0
7	24.17	0	0	0	0	75.83	0	0	0	0
7	0	100	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	8.44	0	0	91.56	0	0	0	0	0	0
8	8.44	0	0	0	91.56	0	0	0	0	0
8	8.44	0	91.56	0	0	0	0	0	0	0
8	8.44	0	0	0	0	0	0	91.56	0	0
8	32.89	0	0	0	0	0	0	0	0	67.11
8	8.44	0	0	0	0	0	91.56	0	0	0
8	20.32	0	0	0	0	79.68	0	0	0	0
8	0	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	5.77	0	0	94.23	0	0	0	0	0	0
9	5.77	0	0	0	94.23	0	0	0	0	0
9	5.77	0	94.23	0	0	0	0	0	0	0
9	5.77	0	0	0	0	0	0	94.23	0	0
9	24.56	0	0	0	0	0	0	0	0	75.44
9	5.77	0	0	0	0	0	94.23	0	0	0
9	16.05	0	0	0	0	83.95	0	0	0	0
9	0	0	0	0	0	0	0	0	0	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	8.49	0	0	8.32	0	0	0	0	83.19	0
10	8.49	0	0	0	8.32	0	0	0	83.19	0
10	8.49	0	8.32	0	0	0	0	0	83.19	0
10	8.49	0	0	0	0	0	0	8.32	83.19	0
10	9.1	0	0	0	0	0	0	0	89.22	1.68
10	8.49	0	0	0	0	0	8.32	0	83.19	0
10	8.08	0	0	0	0	12.68	0	0	79.24	0
10	100	0	0	0	0	0	0	0	0	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	7.17	0	0	13.26	0	0	0	0	79.57	0
11	7.17	0	0	0	13.26	0	0	0	79.57	0
11	7.17	0	13.26	0	0	0	0	0	79.57	0
11	7.17	0	0	0	0	0	0	13.26	79.57	0
11	8.03	0	0	0	0	0	0	0	89.17	2.79
11	7.17	0	0	0	0	0	13.26	0	79.57	0
11	7.21	0	0	0	0	12.8	0	0	79.99	0
11	0	0	0	0	0	0	0	0	0	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	5.96	0	0	17.79	0	0	0	0	76.25	0
12	5.96	0	0	0	17.79	0	0	0	76.25	0
12	5.96	0	17.79	0	0	0	0	0	76.25	0
12	5.96	0	0	0	0	0	0	17.79	76.25	0
12	6.97	0	0	0	0	0	0	0	89.12	3.91
12	5.96	0	0	0	0	0	17.79	0	76.25	0
12	6.32	0	0	0	0	12.92	0	0	80.76	0
12	0	0	0	0	0	0	0	0	0	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	4.85	0	0	21.96	0	0	0	0	73.19	0
13	4.85	0	0	0	21.96	0	0	0	73.19	0
13	4.85	0	21.96	0	0	0	0	0	73.19	0
13	4.85	0	0	0	0	0	0	21.96	73.19	0
13	5.91	0	0	0	0	0	0	0	89.07	5.02
13	4.85	0	0	0	0	0	21.96	0	73.19	0
13	5.41	0	0	0	0	13.05	0	0	81.55	0
13	0	100	0	0	0	0	0	0	0	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	3.83	0	0	25.8	0	0	0	0	70.37	0
14	3.83	0	0	0	25.8	0	0	0	70.37	0
14	3.83	0	25.8	0	0	0	0	0	70.37	0
14	3.83	0	0	0	0	0	0	25.8	70.37	0
14	4.84	0	0	0	0	0	0	0	89.02	6.14
14	3.83	0	0	0	0	0	25.8	0	70.37	0
14	4.48	0	0	0	0	13.18	0	0	82.35	0
14	0	0	0	0	0	0	0	0	0	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	2.88	0	0	29.36	0	0	0	0	67.76	0
15	2.88	0	0	0	29.36	0	0	0	67.76	0
15	2.88	0	29.36	0	0	0	0	0	67.76	0
15	2.88	0	0	0	0	0	0	29.36	67.76	0
15	3.78	0	0	0	0	0	0	0	88.97	7.25
15	2.88	0	0	0	0	0	29.36	0	67.76	0
15	3.53	0	0	0	0	13.31	0	0	83.16	0
15	0	0	0	0	0	0	0	0	0	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2	0	0	32.67	0	0	0	0	65.33	0
16	2	0	0	0	32.67	0	0	0	65.33	0
16	2	0	32.67	0	0	0	0	0	65.33	0
16	2	0	0	0	0	0	0	32.67	65.33	0
16	2.72	0	0	0	0	0	0	0	88.92	8.36
16	2	0	0	0	0	0	32.67	0	65.33	0
16	2.57	0	0	0	0	13.44	0	0	83.99	0
16	100	0	0	0	0	0	0	0	0	0
Temperature
260 C.
1	100	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	100	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	100	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	100	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	100	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	0	0	0	0	0	0	0	0	0
1	0	100	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	100	0	0	0	0	0	0	0	0	0
2	50.5	0	0	49.5	0	0	0	0	0	0
2	50.5	0	0	0	49.5	0	0	0	0	0
2	50.5	0	49.5	0	0	0	0	0	0	0
2	50.5	0	0	0	0	0	0	49.5	0	0
2	84.44	0	0	0	0	0	0	0	0	15.56
2	50.5	0	0	0	0	0	49.5	0	0	0
2	38.93	0	0	0	0	61.07	0	0	0	0
2	0	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	100	0	0	0	0	0	0	0	0	0
3	36.88	0	0	63.12	0	0	0	0	0	0
3	36.88	0	0	0	63.12	0	0	0	0	0
3	36.88	0	63.12	0	0	0	0	0	0	0
3	36.88	0	0	0	0	0	0	63.12	0	0
3	75.65	0	0	0	0	0	0	0	0	24.35
3	36.88	0	0	0	0	0	63.12	0	0	0
3	36.46	0	0	0	0	63.54	0	0	0	0
3	0	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
4	27.58	0	0	72.42	0	0	0	0	0	0
4	27.58	0	0	0	72.42	0	0	0	0	0
4	27.58	0	72.42	0	0	0	0	0	0	0
4	27.58	0	0	0	0	0	0	72.42	0	0
4	66.95	0	0	0	0	0	0	0	0	33.05
4	27.58	0	0	0	0	0	72.42	0	0	0
4	33.77	0	0	0	0	66.23	0	0	0	0
4	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	100	0	0	0	0	0	0	0	0	0
5	20.83	0	0	79.17	0	0	0	0	0	0
5	20.83	0	0	0	79.17	0	0	0	0	0
5	20.83	0	79.17	0	0	0	0	0	0	0
5	20.83	0	0	0	0	0	0	79.17	0	0
5	58.32	0	0	0	0	0	0	0	0	41.68
5	20.83	0	0	0	0	0	79.17	0	0	0
5	30.86	0	0	0	0	69.14	0	0	0	0
5	0	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	100	0	0	0	0	0	0	0	0	0
6	15.7	0	0	84.3	0	0	0	0	0	0
6	15.7	0	0	0	84.3	0	0	0	0	0
6	15.7	0	84.3	0	0	0	0	0	0	0
6	15.7	0	0	0	0	0	0	84.3	0	0
6	49.77	0	0	0	0	0	0	0	0	50.23
6	15.7	0	0	0	0	0	84.3	0	0	0
6	27.67	0	0	0	0	72.33	0	0	0	0
6	0	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	100	0	0	0	0	0	0	0	0	0
7	11.68	0	0	88.32	0	0	0	0	0	0
7	11.68	0	0	0	88.32	0	0	0	0	0
7	11.68	0	88.32	0	0	0	0	0	0	0
7	11.68	0	0	0	0	0	0	88.32	0	0
7	41.29	0	0	0	0	0	0	0	0	58.71
7	11.68	0	0	0	0	0	88.32	0	0	0
7	24.17	0	0	0	0	75.83	0	0	0	0
7	0	100	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	100	0	0	0	0	0	0	0	0	0
8	8.44	0	0	91.56	0	0	0	0	0	0
8	8.44	0	0	0	91.56	0	0	0	0	0
8	8.44	0	91.56	0	0	0	0	0	0	0
8	8.44	0	0	0	0	0	0	91.56	0	0
8	32.89	0	0	0	0	0	0	0	0	67.11
8	8.44	0	0	0	0	0	91.56	0	0	0
8	20.32	0	0	0	0	79.68	0	0	0	0
8	0	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	100	0	0	0	0	0	0	0	0	0
9	5.77	0	0	94.23	0	0	0	0	0	0
9	5.77	0	0	0	94.23	0	0	0	0	0
9	5.77	0	94.23	0	0	0	0	0	0	0
9	5.77	0	0	0	0	0	0	94.23	0	0
9	24.56	0	0	0	0	0	0	0	0	75.44
9	5.77	0	0	0	0	0	94.23	0	0	0
9	16.05	0	0	0	0	83.95	0	0	0	0
9	0	0	0	0	0	0	0	0	0	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	9.26	0	0	0	0	0	0	0	90.74	0
10	8.49	0	0	8.32	0	0	0	0	83.19	0
10	8.49	0	0	0	8.32	0	0	0	83.19	0
10	8.49	0	8.32	0	0	0	0	0	83.19	0
10	8.49	0	0	0	0	0	0	8.32	83.19	0
10	9.1	0	0	0	0	0	0	0	89.22	1.68
10	8.49	0	0	0	0	0	8.32	0	83.19	0
10	8.08	0	0	0	0	12.68	0	0	79.24	0
10	100	0	0	0	0	0	0	0	0	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	8.27	0	0	0	0	0	0	0	91.73	0
11	7.17	0	0	13.26	0	0	0	0	79.57	0
11	7.17	0	0	0	13.26	0	0	0	79.57	0
11	7.17	0	13.26	0	0	0	0	0	79.57	0
11	7.17	0	0	0	0	0	0	13.26	79.57	0
11	8.03	0	0	0	0	0	0	0	89.17	2.79
11	7.17	0	0	0	0	0	13.26	0	79.57	0
11	7.21	0	0	0	0	12.8	0	0	79.99	0
11	0	0	0	0	0	0	0	0	0	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	7.25	0	0	0	0	0	0	0	92.75	0
12	5.96	0	0	17.79	0	0	0	0	76.25	0
12	5.96	0	0	0	17.79	0	0	0	76.25	0
12	5.96	0	17.79	0	0	0	0	0	76.25	0
12	5.96	0	0	0	0	0	0	17.79	76.25	0
12	6.97	0	0	0	0	0	0	0	89.12	3.91
12	5.96	0	0	0	0	0	17.79	0	76.25	0
12	6.32	0	0	0	0	12.92	0	0	80.76	0
12	0	0	0	0	0	0	0	0	0	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	6.22	0	0	0	0	0	0	0	93.78	0
13	4.85	0	0	21.96	0	0	0	0	73.19	0
13	4.85	0	0	0	21.96	0	0	0	73.19	0
13	4.85	0	21.96	0	0	0	0	0	73.19	0
13	4.85	0	0	0	0	0	0	21.96	73.19	0
13	5.91	0	0	0	0	0	0	0	89.07	5.02
13	4.85	0	0	0	0	0	21.96	0	73.19	0
13	5.41	0	0	0	0	13.05	0	0	81.55	0
13	0	100	0	0	0	0	0	0	0	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	5.16	0	0	0	0	0	0	0	94.84	0
14	3.83	0	0	25.8	0	0	0	0	70.37	0
14	3.83	0	0	0	25.8	0	0	0	70.37	0
14	3.83	0	25.8	0	0	0	0	0	70.37	0
14	3.83	0	0	0	0	0	0	25.8	70.37	0
14	4.84	0	0	0	0	0	0	0	89.02	6.14
14	3.83	0	0	0	0	0	25.8	0	70.37	0
14	4.48	0	0	0	0	13.18	0	0	82.35	0
14	0	0	0	0	0	0	0	0	0	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	4.08	0	0	0	0	0	0	0	95.92	0
15	2.88	0	0	29.36	0	0	0	0	67.76	0
15	2.88	0	0	0	29.36	0	0	0	67.76	0
15	2.88	0	29.36	0	0	0	0	0	67.76	0
15	2.88	0	0	0	0	0	0	29.36	67.76	0
15	3.78	0	0	0	0	0	0	0	88.97	7.25
15	2.88	0	0	0	0	0	29.36	0	67.76	0
15	3.53	0	0	0	0	13.31	0	0	83.16	0
15	0	0	0	0	0	0	0	0	0	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2.97	0	0	0	0	0	0	0	97.03	0
16	2	0	0	32.67	0	0	0	0	65.33	0
16	2	0	0	0	32.67	0	0	0	65.33	0
16	2	0	32.67	0	0	0	0	0	65.33	0
16	2	0	0	0	0	0	0	32.67	65.33	0
16	2.72	0	0	0	0	0	0	0	88.92	8.36
16	2	0	0	0	0	0	32.67	0	65.33	0
16	2.57	0	0	0	0	13.44	0	0	83.99	0
16	100	0	0	0	0	0	0	0	0	0

[0279]

TABLE III
							Pt1.0%/ZrO2—
R	C	COCONV	H2OCONV	CO2PROD	CO2PERPROD	CH4PROD	std	LaNO33	PtNH32NO22	ZrONO32			mol %
real	real	real	real	real	real	real	real	real	real	real	SUM_micromols	mol % La	Pt	mol % Zr
Temperature:
250 C.
1	1	24.0554	20.3567	1.0059	36.8713	0.1785	0.1275	0	0	0	0.1275	0	100	0
1	2	−1.7201	3.3539	0.049	1.7972	0.0067	0	0	0	0	0	0	0	0
1	3	−1.3278	2.2499	0.0009	0.0315	−0.0026	0	0	0	0	0	0	0	0
1	4	−1.208	2.4958	0.005	0.1823	−0.0038	0	0	0	0	0	0	0	0
1	5	−1.3966	−0.6647	0.0138	0.5067	−0.0024	0	0	0	0	0	0	0	0
1	6	−0.857	−0.806	0.0089	0.3249	−0.0058	0	0	0	0	0	0	0	0
1	7	26.8747	16.7142	0.9416	34.513	0.151	0.1275	0	0	0	0.1275	0	100	0
1	8	−0.1762	0.0001	0.0106	0.3868	−0.0076	0	0	0	0	0	0	0	0
1	9	−0.605	−1.4054	0.0016	0.0598	−0.0081	0	0	0	0	0	0	0	0
1	10	−0.1705	5.1803	−0.0005	−0.0171	−0.0108	0	0	0	0	0	0	0	0
1	11	0.0287	−2.3403	−0.0261	−0.9568	−0.0134	0	0	0	0	0	0	0	0
1	12	−0.3619	−2.3753	−0.0191	−0.6997	−0.0107	0	0	0	0	0	0	0	0
1	13	26.9134	15.6985	0.9206	33.7449	0.1456	0.1275	0	0	0	0.1275	0	100	0
1	14	0.2866	−1.4436	0.0104	0.3794	−0.0009	0	0	0	0	0	0	0	0
1	15	−0.2691	−2.5021	−0.0098	−0.3592	−0.0125	0	0	0	0	0	0	0	0
1	16	26.3015	15.0776	0.9071	33.2485	0.1422	0.1275	0	0	0	0.1275	0	100	0
2	1	10.3797	7.5635	0.2714	9.9469	0.0465	0	0	0.0319	0	0.0319	0	100	0
2	2	22.2742	13.6256	0.7038	25.7961	0.1014	0	0	0.0319	0	0.0319	0	100	0
2	3	20.1518	11.8043	0.6181	22.6557	0.0925	0	0	0.0319	0	0.0319	0	100	0
2	4	14.7068	7.5278	0.4396	16.1127	0.074	0	0	0.0319	0	0.0319	0	100	0
2	5	12.5748	6.9812	0.3538	12.9691	0.0619	0	0	0.0319	0	0.0319	0	100	0
2	6	12.5733	7.5902	0.3721	13.6375	0.065	0	0	0.0319	0	0.0319	0	100	0
2	7	3.9682	1.1157	0.1053	3.861	0.0291	0	0	0.0319	0	0.0319	0	100	0
2	8	4.2902	1.5276	0.1017	3.728	0.0316	0	0	0.0319	0	0.0319	0	100	0
2	9	17.5859	9.8527	0.5611	20.5685	0.0868	0	0	0.0319	0	0.0319	0	100	0
2	10	4.0056	0.7967	0.1073	3.9343	0.0337	0	0	0.0319	0	0.0319	0	100	0
2	11	0.4511	−1.4852	−0.0262	−0.9611	0.0142	0	0	0.0319	0	0.0319	0	100	0
2	12	8.7515	3.1358	0.2704	9.9096	0.0534	0	0	0.0319	0	0.0319	0	100	0
2	13	1.1667	−0.4291	0.0028	0.1022	0.0172	0	0	0.0319	0	0.0319	0	100	0
2	14	5.3788	3.039	0.1661	6.0891	0.0402	0	0	0.0319	0.625	0.6569	0	4.85	95.15
2	15	13.8175	7.9862	0.4538	16.6329	0.0753	0	0.625	0.0319	0	0.6569	95.15	4.85	0
2	16	0.5892	0.0397	−0.0171	−0.6274	−0.0021	0	0	0	0	0	0	0	0
3	1	23.0341	14.9411	0.7335	26.8867	0.1082	0	0	0.0387	0	0.0387	0	100	0
3	2	24.8268	16.0912	0.7611	27.8973	0.108	0	0	0.0387	0	0.0387	0	100	0
3	3	21.0312	12.2163	0.6617	24.2545	0.0974	0	0	0.0387	0	0.0387	0	100	0
3	4	15.3062	8.5994	0.4563	16.7247	0.0714	0	0	0.0387	0	0.0387	0	100	0
3	5	13.1818	6.4699	0.3775	13.8381	0.0651	0	0	0.0387	0	0.0387	0	100	0
3	6	14.4778	9.2713	0.4241	15.5437	0.0643	0	0	0.0387	0	0.0387	0	100	0
3	7	5.5717	3.3425	0.1029	3.772	0.0251	0	0	0.0387	0	0.0387	0	100	0
3	8	6.8228	1.6923	0.1521	5.5733	0.0283	0	0	0.0387	0	0.0387	0	100	0
3	9	18.2423	12.1678	0.5606	20.5468	0.0831	0	0	0.0387	0	0.0387	0	100	0
3	10	6.7011	5.5857	0.1612	5.907	0.033	0	0	0.0387	0	0.0387	0	100	0
3	11	1.3529	1.3312	−0.0328	−1.2024	0.0065	0	0	0.0387	0	0.0387	0	100	0
3	12	8.988	6.9454	0.2544	9.3233	0.0421	0	0	0.0387	0	0.0387	0	100	0
3	13	1.9882	1.6201	−0.0124	−0.4561	0.0102	0	0	0.0387	0	0.0387	0	100	0
3	14	6.7207	4.8802	0.1283	4.7036	0.0288	0	0	0.0387	0.625	0.6637	0	5.83	94.17
3	15	13.1254	7.8413	0.4144	15.1912	0.0623	0	0.625	0.0387	0	0.6637	94.17	5.83	0
3	16	1.6968	−0.6116	−0.0065	−0.238	0.007	0	0	0	0	0	0	0	0
4	1	25.6701	19.5197	0.7514	27.5411	0.0986	0	0	0.0455	0	0.0455	0	100	0
4	2	23.653	16.9227	0.7928	29.0607	0.0984	0	0	0.0455	0	0.0455	0	100	0
4	3	22.8118	16.1844	0.6593	24.168	0.0919	0	0	0.0455	0	0.0455	0	100	0
4	4	16.4182	10.7873	0.4837	17.731	0.0754	0	0	0.0455	0	0.0455	0	100	0
4	5	14.5564	7.5137	0.4146	15.1965	0.0579	0	0	0.0455	0	0.0455	0	100	0
4	6	15.7933	9.8273	0.453	16.6027	0.0657	0	0	0.0455	0	0.0455	0	100	0
4	7	6.1716	5.3192	0.1362	4.9935	0.0244	0	0	0.0455	0	0.0455	0	100	0
4	8	7.1386	3.6867	0.1822	6.6787	0.0338	0	0	0.0455	0	0.0455	0	100	0
4	9	20.7303	13.3734	0.6248	22.9033	0.0886	0	0	0.0455	0	0.0455	0	100	0
4	10	8.9131	3.194	0.1982	7.2642	0.0334	0	0	0.0455	0	0.0455	0	100	0
4	11	1.6189	1.2404	−0.0525	−1.926	−0.0002	0	0	0.0455	0	0.0455	0	100	0
4	12	10.7432	5.782	0.2838	10.4022	0.045	0	0	0.0455	0	0.0455	0	100	0
4	13	1.5884	0.8166	−0.0105	−0.3833	0.0101	0	0	0.0455	0	0.0455	0	100	0
4	14	6.4031	3.2336	0.1734	6.3554	0.0362	0	0	0.0455	0.625	0.6705	0	6.79	93.21
4	15	15.6125	10.3811	0.4713	17.2763	0.0703	0	0.625	0.0455	0	0.6705	93.21	6.79	0
4	16	27.9195	15.9998	0.8541	31.3081	0.1277	0.1275	0	0	0	0.1275	0	100	0
5	1	23.5648	16.7387	0.7605	27.8743	0.1008	0	0	0.0524	0	0.0524	0	100	0
5	2	24.3053	17.3486	0.7802	28.5962	0.1046	0	0	0.0524	0	0.0524	0	100	0
5	3	22.341	15.7024	0.7107	26.0515	0.1019	0	0	0.0524	0	0.0524	0	100	0
5	4	17.6158	11.8733	0.5469	20.0479	0.0791	0	0	0.0524	0	0.0524	0	100	0
5	5	14.2387	10.1452	0.4049	14.8406	0.0574	0	0	0.0524	0	0.0524	0	100	0
5	6	15.1152	10.7747	0.4328	15.8622	0.0615	0	0	0.0524	0	0.0524	0	100	0
5	7	6.2094	5.1538	0.1363	4.9969	0.0249	0	0	0.0524	0	0.0524	0	100	0
5	8	7.6993	4.4249	0.2079	7.6192	0.0348	0	0	0.0524	0	0.0524	0	100	0
5	9	20.3032	12.9878	0.6687	24.5092	0.091	0	0	0.0524	0	0.0524	0	100	0
5	10	10.467	7.0359	0.2642	9.6824	0.0427	0	0	0.0524	0	0.0524	0	100	0
5	11	2.8488	0.9928	−0.0496	−1.8191	−0.0034	0	0	0.0524	0	0.0524	0	100	0
5	12	8.6081	4.7427	0.2975	10.9032	0.0379	0	0	0.0524	0	0.0524	0	100	0
5	13	2.4786	0.2441	−0.0353	−1.2925	0.0105	0	0	0.0524	0	0.0524	0	100	0
5	14	5.1083	3.0311	0.1416	5.192	0.0285	0	0	0.0524	0.625	0.6774	0	7.73	92.27
5	15	11.8585	7.5495	0.3716	13.62	0.0576	0	0.625	0.0524	0	0.6774	92.27	7.73	0
5	16	0.172	0.0674	−0.0092	−0.3389	0.01	0	0	0	0	0	0	0	0
6	1	22.8548	15.2481	0.7655	28.0601	0.1096	0	0	0.0592	0	0.0592	0	100	0
6	2	25.4205	16.425	0.8006	29.3446	0.11	0	0	0.0592	0	0.0592	0	100	0
6	3	25.0359	16.7118	0.7742	28.379	0.1081	0	0	0.0592	0	0.0592	0	100	0
6	4	19.8242	13.56	0.6037	22.1285	0.0864	0	0	0.0592	0	0.0592	0	100	0
6	5	15.5667	10.9252	0.4506	16.5181	0.0668	0	0	0.0592	0	0.0592	0	100	0
6	6	14.9248	9.1668	0.4848	17.7684	0.0716	0	0	0.0592	0	0.0592	0	100	0
6	7	6.2748	4.0969	0.1824	6.6868	0.0317	0	0	0.0592	0	0.0592	0	100	0
6	8	8.4858	5.8883	0.251	9.2019	0.0404	0	0	0.0592	0	0.0592	0	100	0
6	9	21.0027	12.7923	0.7581	27.7862	0.1015	0	0	0.0592	0	0.0592	0	100	0
6	10	4.1864	1.0991	0.2231	8.177	0.044	0	0	0.0592	0	0.0592	0	100	0
6	11	−1.2373	−1.4393	0.0135	0.4931	0.0092	0	0	0.0592	0	0.0592	0	100	0
6	12	10.6286	6.8786	0.3149	11.5433	0.0492	0	0	0.0592	0	0.0592	0	100	0
6	13	1.0716	0.1767	0.0081	0.2959	0.0131	0	0	0.0592	0	0.0592	0	100	0
6	14	6.6959	4.4786	0.1742	6.3849	0.0291	0	0	0.0592	0.625	0.6842	0	8.65	91.35
6	15	14.9263	8.9373	0.4504	16.5076	0.0691	0	0.625	0.0592	0	0.6842	91.35	8.65	0
6	16	0.9734	0.524	−0.0068	−0.2476	0.0095	0	0	0	0	0	0	0	0
7	1	22.5418	15.4759	0.726	26.6121	0.0978	0	0	0.066	0	0.066	0	100	0
7	2	25.3352	17.1813	0.8109	29.7233	0.1123	0	0	0.066	0	0.066	0	100	0
7	3	25.4575	17.3091	0.7912	29.0012	0.1094	0	0	0.066	0	0.066	0	100	0
7	4	20.6572	14.3391	0.6313	23.1392	0.0896	0	0	0.066	0	0.066	0	100	0
7	5	15.932	11.3449	0.4504	16.51	0.0654	0	0	0.066	0	0.066	0	100	0
7	6	15.7862	11.3444	0.4701	17.2316	0.0672	0	0	0.066	0	0.066	0	100	0
7	7	6.5518	5.4328	0.1609	5.8983	0.0264	0	0	0.066	0	0.066	0	100	0
7	8	8.798	5.7477	0.2274	8.3369	0.0394	0	0	0.066	0	0.066	0	100	0
7	9	23.0075	15.3925	0.6659	24.4074	0.0863	0	0	0.066	0	0.066	0	100	0
7	10	9.2334	7.3996	0.2983	10.934	0.0356	0	0	0.066	0	0.066	0	100	0
7	11	0.7033	0.897	−0.0323	−1.1825	0.0007	0	0	0.066	0	0.066	0	100	0
7	12	9.8812	6.9932	0.3106	11.3832	0.047	0	0	0.066	0	0.066	0	100	0
7	13	1.8315	1.5281	−0.0004	−0.0142	0.0064	0	0	0.066	0	0.066	0	100	0
7	14	5.9233	4.0164	0.1346	4.9347	0.024	0	0	0.066	0.625	0.691	0	9.55	90.45
7	15	11.3981	7.0352	0.3499	12.8255	0.0508	0	0.625	0.066	0	0.691	90.45	9.55	0
7	16	26.5669	16.7815	0.8474	31.0624	0.1182	0.1275	0	0	0	0.1275	0	100	0
8	1	22.7201	15.0948	0.694	25.4388	0.0942	0	0	0.0729	0	0.0729	0	100	0
8	2	25.5968	16.5345	0.8165	29.9286	0.1106	0	0	0.0729	0	0.0729	0	100	0
8	3	26.9015	16.5093	0.8118	29.7556	0.1132	0	0	0.0729	0	0.0729	0	100	0
8	4	22.6912	14.399	0.6735	24.6849	0.0922	0	0	0.0729	0	0.0729	0	100	0
8	5	16.1513	10.0868	0.4873	17.8622	0.0711	0	0	0.0729	0	0.0729	0	100	0
8	6	14.9604	9.3549	0.5104	18.7093	0.0788	0	0	0.0729	0	0.0729	0	100	0
8	7	9.1106	4.8845	0.1351	4.9537	0.0227	0	0	0.0729	0	0.0729	0	100	0
8	8	11.6445	4.2759	0.265	9.7129	0.0431	0	0	0.0729	0	0.0729	0	100	0
8	9	22.1496	13.0101	0.7517	27.5537	0.103	0	0	0.0729	0	0.0729	0	100	0
8	10	10.7574	7.0805	0.323	11.8395	0.0477	0	0	0.0729	0	0.0729	0	100	0
8	11	3.6004	0.9577	0.0383	1.4029	0.0094	0	0	0.0729	0	0.0729	0	100	0
8	12	11.534	7.8883	0.3533	12.9484	0.0508	0	0	0.0729	0	0.0729	0	100	0
8	13	1.3464	0.5169	−0.0012	−0.0457	0.0054	0	0	0.0729	0	0.0729	0	100	0
8	14	6.4094	3.371	0.1695	6.2144	0.0276	0	0	0.0729	0.625	0.6979	0	10.44	89.56
8	15	12.8137	8.3353	0.3838	14.067	0.054	0	0.625	0.0729	0	0.6979	89.56	10.44	0
8	16	0.6005	0.7618	−0.0245	−0.8983	0.0023	0	0	0	0	0	0	0	0
9	1	22.4957	14.7378	0.6826	25.0193	0.0926	0	0	0.0797	0	0.0797	0	100	0
9	2	25.986	17.2218	0.8042	29.4787	0.1075	0	0	0.0797	0	0.0797	0	100	0
9	3	26.7278	17.0659	0.8299	30.4191	0.1155	0	0	0.0797	0	0.0797	0	100	0
9	4	21.7825	14.3953	0.6911	25.3306	0.0965	0	0	0.0797	0	0.0797	0	100	0
9	5	17.2508	11.3087	0.5012	18.3711	0.0717	0	0	0.0797	0	0.0797	0	100	0
9	6	16.9581	10.5872	0.4639	17.0022	0.0651	0	0	0.0797	0	0.0797	0	100	0
9	7	6.3335	4.0566	0.1665	6.1027	0.0326	0	0	0.0797	0	0.0797	0	100	0
9	8	11.9448	6.8015	0.2794	10.2426	0.0347	0	0	0.0797	0	0.0797	0	100	0
9	9	22.3682	14.3068	0.6953	25.4874	0.0927	0	0	0.0797	0	0.0797	0	100	0
9	10	10.6395	6.5727	0.3015	11.0498	0.0426	0	0	0.0797	0	0.0797	0	100	0
9	11	0.7463	−0.5268	−0.0297	−1.0885	0.0037	0	0	0.0797	0	0.0797	0	100	0
9	12	11.6436	6.9032	0.3308	12.1271	0.0465	0	0	0.0797	0	0.0797	0	100	0
9	13	2.2734	1.3731	−0.0036	−0.1307	0.0063	0	0	0.0797	0	0.0797	0	100	0
9	14	5.2473	2.3383	0.133	4.8766	0.0256	0	0	0.0797	0.625	0.7047	0	11.31	88.69
9	15	14.1744	8.1484	0.4386	16.0753	0.0629	0	0.625	0.0797	0	0.7047	88.69	11.31	0
9	16	1.1167	0.6406	−0.0074	−0.2708	0.0074	0	0	0	0	0	0	0	0
10	1	21.0706	14.7112	0.6846	25.0928	0.0968	0	0	0.0865	0	0.0865	0	100	0
10	2	26.8869	17.9825	0.8859	32.4724	0.1184	0	0	0.0865	0	0.0865	0	100	0
10	3	26.6813	16.9521	0.9023	33.0744	0.1263	0	0	0.0865	0	0.0865	0	100	0
10	4	22.8526	14.0275	0.7543	27.65	0.106	0	0	0.0865	0	0.0865	0	100	0
10	5	16.4643	9.638	0.5121	18.772	0.0768	0	0	0.0865	0	0.0865	0	100	0
10	6	16.974	10.2305	0.4989	18.2853	0.0738	0	0	0.0865	0	0.0865	0	100	0
10	7	7.0764	3.7892	0.217	7.954	0.0367	0	0	0.0865	0	0.0865	0	100	0
10	8	10.3301	7.0156	0.3079	11.2846	0.0444	0	0	0.0865	0	0.0865	0	100	0
10	9	22.9265	14.8712	0.7519	27.5603	0.1024	0	0	0.0865	0	0.0865	0	100	0
10	10	12.4677	6.9963	0.3574	13.1014	0.0529	0	0	0.0865	0	0.0865	0	100	0
10	11	0.5969	−0.5299	−0.0215	−0.7876	0.0033	0	0	0.0865	0	0.0865	0	100	0
10	12	13.3324	8.0107	0.3981	14.593	0.0579	0	0	0.0865	0	0.0865	0	100	0
10	13	1.9031	0.5698	0.0129	0.4715	0.0076	0	0	0.0865	0	0.0865	0	100	0
10	14	6.4847	3.7801	0.156	5.7172	0.0292	0	0	0.0865	0.625	0.7115	0	12.16	87.84
10	15	13.3979	8.7146	0.4385	16.0738	0.0621	0	0.625	0.0865	0	0.7115	87.84	12.16	0
10	16	25.4495	16.0477	0.8342	30.5766	0.1176	0.1275	0	0	0	0.1275	0	100	0
11	1	20.1375	13.3902	0.695	25.4752	0.0941	0	0	0.0933	0	0.0933	0	100	0
11	2	27.139	17.1786	0.8841	32.4048	0.1236	0	0	0.0933	0	0.0933	0	100	0
11	3	26.9388	16.683	0.9125	33.4483	0.127	0	0	0.0933	0	0.0933	0	100	0
11	4	24.5762	15.8875	0.789	28.9207	0.1089	0	0	0.0933	0	0.0933	0	100	0
11	5	15.1923	9.882	0.4773	17.4944	0.0718	0	0	0.0933	0	0.0933	0	100	0
11	6	15.7362	10.517	0.4959	18.1782	0.0704	0	0	0.0933	0	0.0933	0	100	0
11	7	6.9524	4.547	0.2149	7.8771	0.0338	0	0	0.0933	0	0.0933	0	100	0
11	8	10.7228	5.8543	0.3063	11.2265	0.0473	0	0	0.0933	0	0.0933	0	100	0
11	9	21.6871	13.7234	0.7381	27.0563	0.1017	0	0	0.0933	0	0.0933	0	100	0
11	10	10.2552	6.749	0.3273	11.9961	0.0462	0	0	0.0933	0	0.0933	0	100	0
11	11	0.1751	−0.8137	−0.0162	−0.5948	0.0093	0	0	0.0933	0	0.0933	0	100	0
11	12	12.9233	7.3461	0.3959	14.5118	0.058	0	0	0.0933	0	0.0933	0	100	0
11	13	2.1161	−0.0461	0.0196	0.7173	0.0121	0	0	0.0933	0	0.0933	0	100	0
11	14	5.318	2.5839	0.1421	5.2076	0.028	0	0	0.0933	0.625	0.7183	0	12.99	87.01
11	15	12.7569	6.3017	0.3941	14.4456	0.0579	0	0.625	0.0933	0	0.7183	87.01	12.99	0
11	16	0.8455	−1.3583	0.0027	0.0985	0.0084	0	0	0	0	0	0	0	0
12	1	15.9884	10.3576	0.5209	19.0939	0.0763	0	0	0.1002	0	0.1002	0	100	0
12	2	27.3984	16.7714	0.9241	33.8719	0.128	0	0	0.1002	0	0.1002	0	100	0
12	3	28.1625	17.4315	0.9325	34.1804	0.1313	0	0	0.1002	0	0.1002	0	100	0
12	4	24.8213	15.2594	0.851	31.1941	0.1246	0	0	0.1002	0	0.1002	0	100	0
12	5	16.5105	9.4519	0.5715	20.9463	0.089	0	0	0.1002	0	0.1002	0	100	0
12	6	16.2367	8.6629	0.5246	19.229	0.0791	0	0	0.1002	0	0.1002	0	100	0
12	7	7.0822	2.7268	0.2494	9.143	0.0433	0	0	0.1002	0	0.1002	0	100	0
12	8	11.1025	6.1665	0.3763	13.7941	0.056	0	0	0.1002	0	0.1002	0	100	0
12	9	23.5429	14.4559	0.8026	29.419	0.1129	0	0	0.1002	0	0.1002	0	100	0
12	10	12.4169	7.2141	0.384	14.0754	0.0576	0	0	0.1002	0	0.1002	0	100	0
12	11	−0.2192	−1.5288	−0.0114	−0.4195	0.0063	0	0	0.1002	0	0.1002	0	100	0
12	12	13.2567	7.0496	0.4182	15.3281	0.0611	0	0	0.1002	0	0.1002	0	100	0
12	13	1.2187	−0.6308	0.0286	1.0496	0.0116	0	0	0.1002	0	0.1002	0	100	0
12	14	5.5276	1.9229	0.1649	6.0426	0.0328	0	0	0.1002	0.625	0.7252	0	13.81	86.19
12	15	13.3469	6.2659	0.4232	15.5137	0.0634	0	0.625	0.1002	0	0.7252	86.19	13.81	0
12	16	1.0083	−0.586	0.011	0.4039	0.0096	0	0	0	0	0	0	0	0
13	1	18.6644	11.2964	0.6506	23.8458	0.0932	0	0	0.107	0	0.107	0	100	0
13	2	27.845	15.9413	0.9392	34.4261	0.1308	0	0	0.107	0	0.107	0	100	0
13	3	27.3697	17.3186	0.9442	34.6097	0.1337	0	0	0.107	0	0.107	0	100	0
13	4	25.678	15.9207	0.8401	30.7915	0.1183	0	0	0.107	0	0.107	0	100	0
13	5	15.7945	10.0005	0.5228	19.164	0.0793	0	0	0.107	0	0.107	0	100	0
13	6	15.3463	9.2398	0.5087	18.6471	0.0765	0	0	0.107	0	0.107	0	100	0
13	7	6.7754	3.6609	0.2308	8.459	0.0396	0	0	0.107	0	0.107	0	100	0
13	8	11.692	6.4553	0.3752	13.7513	0.0561	0	0	0.107	0	0.107	0	100	0
13	9	23.2809	13.521	0.8112	29.7353	0.1124	0	0	0.107	0	0.107	0	100	0
13	10	13.5562	7.5286	0.4302	15.7676	0.0624	0	0	0.107	0	0.107	0	100	0
13	11	1.1357	−1.0497	−0.0258	−0.9457	0.0072	0	0	0.107	0	0.107	0	100	0
13	12	14.0892	7.0847	0.4404	16.1411	0.0683	0	0	0.107	0	0.107	0	100	0
13	13	1.2307	−0.0972	0.0411	1.5048	0.0161	0	0	0.107	0	0.107	0	100	0
13	14	5.0473	1.1814	0.1519	5.5685	0.0306	0	0	0.107	0.625	0.732	0	14.62	85.38
13	15	12.8894	6.9657	0.3932	14.413	0.0574	0	0.625	0.107	0	0.732	85.38	14.62	0
13	16	27.0196	15.8321	0.9126	33.449	0.1349	0.1275	0	0	0	0.1275	0	100	0
14	1	21.6824	14.5808	0.7642	28.0108	0.1054	0	0	0.1138	0	0.1138	0	100	0
14	2	27.9534	18.5673	0.9122	33.4357	0.1269	0	0	0.1138	0	0.1138	0	100	0
14	3	28.3871	17.6025	0.9506	34.8433	0.1361	0	0	0.1138	0	0.1138	0	100	0
14	4	26.5322	15.1329	0.8627	31.6204	0.1283	0	0	0.1138	0	0.1138	0	100	0
14	5	17.27	10.4633	0.5486	20.1091	0.0846	0	0	0.1138	0	0.1138	0	100	0
14	6	16.6826	9.6418	0.5721	20.9704	0.0848	0	0	0.1138	0	0.1138	0	100	0
14	7	7.7667	4.5307	0.2694	9.8752	0.0433	0	0	0.1138	0	0.1138	0	100	0
14	8	13.2575	8.5866	0.4374	16.0317	0.064	0	0	0.1138	0	0.1138	0	100	0
14	9	24.5972	16.2327	0.8255	30.2566	0.1118	0	0	0.1138	0	0.1138	0	100	0
14	10	14.1237	8.1483	0.478	17.5191	0.0713	0	0	0.1138	0	0.1138	0	100	0
14	11	−0.172	−1.5106	−0.0204	−0.7482	0.0089	0	0	0.1138	0	0.1138	0	100	0
14	12	15.8277	8.9664	0.5076	18.6043	0.0706	0	0	0.1138	0	0.1138	0	100	0
14	13	1.0637	−1.0104	0.0444	1.6268	0.0139	0	0	0.1138	0	0.1138	0	100	0
14	14	4.6635	2.3532	0.1677	6.1462	0.0296	0	0	0.1138	0.625	0.7388	0	15.41	84.59
14	15	12.9488	7.3298	0.4296	15.7453	0.0651	0	0.625	0.1138	0	0.7388	84.59	15.41	0
14	16	0.3061	−0.5069	−0.0065	−0.2391	0.0099	0	0	0	0	0	0	0	0
15	1	17.1998	12.0104	0.5755	21.0955	0.0799	0	0	0.1207	0	0.1207	0	100	0
15	2	27.4482	17.526	0.933	34.1967	0.1316	0	0	0.1207	0	0.1207	0	100	0
15	3	28.1178	18.8556	0.9242	33.8763	0.1324	0	0	0.1207	0	0.1207	0	100	0
15	4	26.8701	17.1463	0.856	31.3778	0.1258	0	0	0.1207	0	0.1207	0	100	0
15	5	17.6631	10.9667	0.5845	21.4248	0.0858	0	0	0.1207	0	0.1207	0	100	0
15	6	17.1402	10.8854	0.5425	19.8853	0.0798	0	0	0.1207	0	0.1207	0	100	0
15	7	8.2663	5.3027	0.2441	8.9487	0.0387	0	0	0.1207	0	0.1207	0	100	0
15	8	11.9892	6.7241	0.3904	14.3081	0.0566	0	0	0.1207	0	0.1207	0	100	0
15	9	24.1606	15.639	0.8291	30.3902	0.1118	0	0	0.1207	0	0.1207	0	100	0
15	10	15.0377	10.3936	0.4614	16.9136	0.0638	0	0	0.1207	0	0.1207	0	100	0
15	11	0.2191	−0.9933	−0.0152	−0.558	0.0074	0	0	0.1207	0	0.1207	0	100	0
15	12	16.1138	9.1228	0.5094	18.6707	0.0732	0	0	0.1207	0	0.1207	0	100	0
15	13	2.4821	0.3422	0.0309	1.1317	0.0144	0	0	0.1207	0	0.1207	0	100	0
15	14	5.4454	0.6463	0.189	6.9276	0.035	0	0	0.1207	0.625	0.7457	0	16.18	83.82
15	15	14.0229	7.8558	0.4492	16.4654	0.0681	0	0.625	0.1207	0	0.7457	83.82	16.18	0
15	16	0.4686	−0.7131	0.0197	0.7216	0.01	0	0	0	0	0	0	0	0
16	1	7.4861	4.4402	0.2493	9.1386	0.0401	0	0	0.1275	0	0.1275	0	100	0
16	2	29.0506	17.8613	0.9483	34.7579	0.1412	0	0	0.1275	0	0.1275	0	100	0
16	3	29.4694	17.4993	0.9236	33.8554	0.1479	0	0	0.1275	0	0.1275	0	100	0
16	4	28.4749	16.4322	0.9104	33.3693	0.1531	0	0	0.1275	0	0.1275	0	100	0
16	5	22.0326	12.6858	0.7055	25.8606	0.1115	0	0	0.1275	0	0.1275	0	100	0
16	6	20.0805	12.1402	0.6291	23.0594	0.0943	0	0	0.1275	0	0.1275	0	100	0
16	7	9.0587	5.2161	0.2666	9.7703	0.0461	0	0	0.1275	0	0.1275	0	100	0
16	8	13.983	9.3075	0.4391	16.0948	0.0636	0	0	0.1275	0	0.1275	0	100	0
16	9	26.9905	17.0719	0.877	32.1456	0.1198	0	0	0.1275	0	0.1275	0	100	0
16	10	14.704	8.6762	0.4886	17.9102	0.073	0	0	0.1275	0	0.1275	0	100	0
16	11	0.7191	−1.4742	−0.0041	−0.1519	0.0077	0	0	0.1275	0	0.1275	0	100	0
16	12	19.314	11.1355	0.6495	23.808	0.0899	0	0	0.1275	0	0.1275	0	100	0
16	13	2.4636	0.033	0.0679	2.4886	0.0206	0	0	0.1275	0	0.1275	0	100	0
16	14	11.4461	6.8975	0.3856	14.134	0.0639	0	0	0.1275	0.625	0.7525	0	16.94	83.06
16	15	20.8264	13.1623	0.7	25.6595	0.0961	0	0.625	0.1275	0	0.7525	83.06	16.94	0
16	16	26.7851	15.9945	0.9048	33.1661	0.1319	0.1275	0	0	0	0.1275	0	100	0
Temperature:
300 C.
1	1	26.0412	13.6761	0.7608	27.4327	0.1592	0.1275	0	0	0	0.1275	0	100	0
1	2	1.9716	2.4686	0.0066	0.2386	0.0092	0	0	0	0	0	0	0	0
1	3	0.3229	0.3952	−0.0391	−1.4081	0.0062	0	0	0	0	0	0	0	0
1	4	0.6417	0.8578	−0.0504	−1.8187	−0.0005	0	0	0	0	0	0	0	0
1	5	0.173	0.5233	−0.0449	−1.6183	0.0024	0	0	0	0	0	0	0	0
1	6	0.3624	0.0747	−0.0376	−1.3546	−0.0039	0	0	0	0	0	0	0	0
1	7	26.157	12.3934	0.797	28.7383	0.1699	0.1275	0	0	0	0.1275	0	100	0
1	8	3.5333	0.2801	−0.0585	−2.108	−0.0107	0	0	0	0	0	0	0	0
1	9	−1.8657	−3.8002	−0.0104	−0.375	0.0197	0	0	0	0	0	0	0	0
1	10	2.592	0.129	−0.014	−0.5051	−0.0253	0	0	0	0	0	0	0	0
1	11	−3.1613	−1.397	−0.0273	−0.9858	0.0043	0	0	0	0	0	0	0	0
1	12	−0.5382	−0.741	−0.0195	−0.7042	−0.0352	0	0	0	0	0	0	0	0
1	13	25.293	12.9331	0.8097	29.194	0.1597	0.1275	0	0	0	0.1275	0	100	0
1	14	0.8774	0.3654	−0.018	−0.648	0.0052	0	0	0	0	0	0	0	0
1	15	−1.2793	0.1383	−0.0181	−0.6543	0.0027	0	0	0	0	0	0	0	0
1	16	25.6735	12.143	0.7277	26.2368	0.1566	0.1275	0	0	0	0.1275	0	100	0
2	1	14.8766	10.2106	0.3917	14.1217	0.0524	0	0	0.0319	0	0.0319	0	100	0
2	2	20.4545	14.6181	0.746	26.8969	0.1088	0	0	0.0319	0	0.0319	0	100	0
2	3	19.9352	12.3858	0.6977	25.1579	0.1196	0	0	0.0319	0	0.0319	0	100	0
2	4	16.0396	10.1097	0.6511	23.4768	0.109	0	0	0.0319	0	0.0319	0	100	0
2	5	15.904	10.2101	0.4597	16.5765	0.0626	0	0	0.0319	0	0.0319	0	100	0
2	6	14.9915	9.8692	0.3995	14.4034	0.0662	0	0	0.0319	0	0.0319	0	100	0
2	7	6.2101	5.2473	0.1852	6.6763	0.0252	0	0	0.0319	0	0.0319	0	100	0
2	8	9.4972	5.8339	0.283	10.205	0.0496	0	0	0.0319	0	0.0319	0	100	0
2	9	21.1669	13.9111	0.6435	23.2016	0.0932	0	0	0.0319	0	0.0319	0	100	0
2	10	8.0932	5.8934	0.2958	10.6661	0.0493	0	0	0.0319	0	0.0319	0	100	0
2	11	0.4906	0.3109	−0.0754	−2.7173	0.0004	0	0	0.0319	0	0.0319	0	100	0
2	12	12.7979	8.96	0.445	16.0439	0.0703	0	0	0.0319	0	0.0319	0	100	0
2	13	1.7683	2.1621	0.0286	1.0326	0.0176	0	0	0.0319	0	0.0319	0	100	0
2	14	11.5049	8.9483	0.3603	12.9899	0.0656	0	0	0.0319	0.625	0.6569	0	4.85	95.15
2	15	19.2509	11.5249	0.6541	23.5849	0.0881	0	0.625	0.0319	0	0.6569	95.15	4.85	0
2	16	−2.2275	0.1022	0.0038	0.136	0.001	0	0	0	0	0	0	0	0
3	1	19.5625	13.7405	0.7553	27.2322	0.1169	0	0	0.0387	0	0.0387	0	100	0
3	2	23.3448	16.4986	0.7782	28.0599	0.1055	0	0	0.0387	0	0.0387	0	100	0
3	3	20.2746	14.4888	0.7447	26.8513	0.1236	0	0	0.0387	0	0.0387	0	100	0
3	4	21.042	14.6567	0.5975	21.5435	0.0868	0	0	0.0387	0	0.0387	0	100	0
3	5	15.227	11.3009	0.5184	18.6931	0.0896	0	0	0.0387	0	0.0387	0	100	0
3	6	16.2981	13.1574	0.4916	17.7266	0.0804	0	0	0.0387	0	0.0387	0	100	0
3	7	7.5318	7.7146	0.2177	7.8495	0.0364	0	0	0.0387	0	0.0387	0	100	0
3	8	14.1025	10.9954	0.419	15.1061	0.0628	0	0	0.0387	0	0.0387	0	100	0
3	9	20.9253	15.3432	0.7024	25.3266	0.1019	0	0	0.0387	0	0.0387	0	100	0
3	10	13.728	11.1605	0.4466	16.1033	0.0679	0	0	0.0387	0	0.0387	0	100	0
3	11	−1.0656	0.7638	−0.03	−1.0824	−0.001	0	0	0.0387	0	0.0387	0	100	0
3	12	12.0316	9.0087	0.4143	14.9372	0.064	0	0	0.0387	0	0.0387	0	100	0
3	13	2.3735	2.427	0.0472	1.7003	0.0158	0	0	0.0387	0	0.0387	0	100	0
3	14	10.011	6.6184	0.4321	15.5784	0.078	0	0	0.0387	0.625	0.6637	0	5.83	94.17
3	15	17.1288	11.9418	0.6936	25.0081	0.1016	0	0.625	0.0387	0	0.6637	94.17	5.83	0
3	16	−0.0207	−0.0056	0.0564	2.0341	−0.003	0	0	0	0	0	0	0	0
4	1	23.9972	15.9845	0.7717	27.8233	0.119	0	0	0.0455	0	0.0455	0	100	0
4	2	24.3635	16.2531	0.7072	25.5007	0.1199	0	0	0.0455	0	0.0455	0	100	0
4	3	21.4425	14.1432	0.7498	27.0362	0.1265	0	0	0.0455	0	0.0455	0	100	0
4	4	19.4479	12.996	0.6822	24.5996	0.107	0	0	0.0455	0	0.0455	0	100	0
4	5	16.0527	11.3163	0.5819	20.98	0.0935	0	0	0.0455	0	0.0455	0	100	0
4	6	17.5309	11.186	0.5671	20.447	0.0842	0	0	0.0455	0	0.0455	0	100	0
4	7	8.0993	5.7381	0.3374	12.166	0.0503	0	0	0.0455	0	0.0455	0	100	0
4	8	14.119	9.8107	0.5489	19.7929	0.0801	0	0	0.0455	0	0.0455	0	100	0
4	9	23.2762	14.9011	0.7786	28.0723	0.1033	0	0	0.0455	0	0.0455	0	100	0
4	10	14.7194	10.4363	0.5718	20.6185	0.08	0	0	0.0455	0	0.0455	0	100	0
4	11	1.1453	0.3882	−0.067	−2.4162	−0.0168	0	0	0.0455	0	0.0455	0	100	0
4	12	12.7656	8.8311	0.4759	17.1582	0.0689	0	0	0.0455	0	0.0455	0	100	0
4	13	4.4502	1.323	0.0072	0.2593	0.0135	0	0	0.0455	0	0.0455	0	100	0
4	14	13.3844	9.4729	0.4141	14.9311	0.0687	0	0	0.0455	0.625	0.6705	0	6.79	93.21
4	15	20.7018	14.4153	0.6795	24.5002	0.0932	0	0.625	0.0455	0	0.6705	93.21	6.79	0
4	16	26.3093	12.5646	0.7405	26.6988	0.1561	0.1275	0	0	0	0.1275	0	100	0
5	1	21.4105	14.4067	0.7125	25.6898	0.11	0	0	0.0524	0	0.0524	0	100	0
5	2	22.1022	14.8036	0.819	29.5304	0.1282	0	0	0.0524	0	0.0524	0	100	0
5	3	22.5933	14.8442	0.7244	26.1201	0.1233	0	0	0.0524	0	0.0524	0	100	0
5	4	21.0057	13.8057	0.6911	24.9201	0.1153	0	0	0.0524	0	0.0524	0	100	0
5	5	17.672	12.2393	0.5728	20.6522	0.0902	0	0	0.0524	0	0.0524	0	100	0
5	6	16.0245	11.7967	0.5902	21.2789	0.0941	0	0	0.0524	0	0.0524	0	100	0
5	7	8.682	6.8022	0.35	12.6185	0.0569	0	0	0.0524	0	0.0524	0	100	0
5	8	16.2047	10.7313	0.5656	20.3921	0.0857	0	0	0.0524	0	0.0524	0	100	0
5	9	21.0729	14.0649	0.7974	28.7515	0.124	0	0	0.0524	0	0.0524	0	100	0
5	10	18.1655	12.1093	0.6249	22.5323	0.094	0	0	0.0524	0	0.0524	0	100	0
5	11	−3.2789	−1.8833	0.0173	0.625	−0.017	0	0	0.0524	0	0.0524	0	100	0
5	12	12.1376	7.6528	0.5085	18.3339	0.0689	0	0	0.0524	0	0.0524	0	100	0
5	13	2.8719	1.6064	0.0398	1.4347	0.0232	0	0	0.0524	0	0.0524	0	100	0
5	14	11.6313	7.1984	0.3756	13.5442	0.064	0	0	0.0524	0.625	0.6774	0	7.73	92.27
5	15	18.7077	12.3422	0.6784	24.4596	0.1017	0	0.625	0.0524	0	0.6774	92.27	7.73	0
5	16	−0.923	0.6423	0.0024	0.0871	−0.0005	0	0	0	0	0	0	0	0
6	1	22.0063	14.1082	0.7772	28.0216	0.121	0	0	0.0592	0	0.0592	0	100	0
6	2	23.7522	14.4251	0.8181	29.4983	0.1363	0	0	0.0592	0	0.0592	0	100	0
6	3	23.7349	12.7968	0.778	28.0518	0.1487	0	0	0.0592	0	0.0592	0	100	0
6	4	21.7688	12.1769	0.7488	27.0006	0.1335	0	0	0.0592	0	0.0592	0	100	0
6	5	18.6185	12.368	0.6292	22.6862	0.1057	0	0	0.0592	0	0.0592	0	100	0
6	6	17.435	11.7025	0.6457	23.2833	0.0997	0	0	0.0592	0	0.0592	0	100	0
6	7	9.5496	7.4033	0.4005	14.4418	0.0656	0	0	0.0592	0	0.0592	0	100	0
6	8	18.8345	12.608	0.602	21.7077	0.0895	0	0	0.0592	0	0.0592	0	100	0
6	9	22.7783	14.5707	0.7858	28.3319	0.1268	0	0	0.0592	0	0.0592	0	100	0
6	10	14.2889	9.3319	0.4808	17.3344	0.0626	0	0	0.0592	0	0.0592	0	100	0
6	11	−1.4423	−3.1898	0.0072	0.2597	−0.0242	0	0	0.0592	0	0.0592	0	100	0
6	12	14.6391	9.1343	0.5169	18.6393	0.0784	0	0	0.0592	0	0.0592	0	100	0
6	13	1.3924	0.1849	0.1067	3.8458	0.0254	0	0	0.0592	0	0.0592	0	100	0
6	14	12.4467	7.9011	0.47	16.947	0.0796	0	0	0.0592	0.625	0.6842	0	8.65	91.35
6	15	20.5551	12.4877	0.7241	26.1085	0.1086	0	0.625	0.0592	0	0.6842	91.35	8.65	0
6	16	1.8224	1.9194	0.0293	1.0577	−0.001	0	0	0	0	0	0	0	0
7	1	20.1793	13.5157	0.7141	25.7483	0.1062	0	0	0.066	0	0.066	0	100	0
7	2	23.9199	15.0715	0.7923	28.5691	0.1334	0	0	0.066	0	0.066	0	100	0
7	3	24.0921	13.8724	0.7704	27.7794	0.1489	0	0	0.066	0	0.066	0	100	0
7	4	22.4883	13.3333	0.7472	26.9401	0.1331	0	0	0.066	0	0.066	0	100	0
7	5	18.3753	10.967	0.6933	24.9964	0.1147	0	0	0.066	0	0.066	0	100	0
7	6	19.1636	11.8882	0.594	21.4179	0.0973	0	0	0.066	0	0.066	0	100	0
7	7	11.6242	8.7829	0.358	12.9075	0.0589	0	0	0.066	0	0.066	0	100	0
7	8	18.9461	11.9304	0.6075	21.9057	0.0865	0	0	0.066	0	0.066	0	100	0
7	9	20.8727	13.268	0.8581	30.9391	0.1366	0	0	0.066	0	0.066	0	100	0
7	10	19.7469	12.533	0.627	22.6084	0.0889	0	0	0.066	0	0.066	0	100	0
7	11	0.2661	−1.0746	−0.0206	−0.7417	−0.0241	0	0	0.066	0	0.066	0	100	0
7	12	14.9635	8.7674	0.5117	18.4485	0.0776	0	0	0.066	0	0.066	0	100	0
7	13	2.473	1.1259	0.0915	3.3004	0.0134	0	0	0.066	0	0.066	0	100	0
7	14	10.4908	6.4436	0.4097	14.774	0.0771	0	0	0.066	0.625	0.691	0	9.55	90.45
7	15	17.9387	11.3159	0.7335	26.449	0.109	0	0.625	0.066	0	0.691	90.45	9.55	0
7	16	24.6649	12.1883	0.7892	28.4564	0.1735	0.1275	0	0	0	0.1275	0	100	0
8	1	20.4072	13.9072	0.7031	25.3521	0.1107	0	0	0.0729	0	0.0729	0	100	0
8	2	23.2299	15.5533	0.8078	29.1272	0.1368	0	0	0.0729	0	0.0729	0	100	0
8	3	24.3029	13.9797	0.7799	28.1203	0.1564	0	0	0.0729	0	0.0729	0	100	0
8	4	22.2113	14.5975	0.7495	27.0256	0.1425	0	0	0.0729	0	0.0729	0	100	0
8	5	18.1577	13.0692	0.6943	25.034	0.1167	0	0	0.0729	0	0.0729	0	100	0
8	6	16.4584	11.241	0.6799	24.5135	0.1128	0	0	0.0729	0	0.0729	0	100	0
8	7	11.3178	9.6452	0.4321	15.5795	0.0596	0	0	0.0729	0	0.0729	0	100	0
8	8	20.8336	14.4605	0.6457	23.2815	0.0922	0	0	0.0729	0	0.0729	0	100	0
8	9	23.346	15.3942	0.8346	30.0941	0.1169	0	0	0.0729	0	0.0729	0	100	0
8	10	20.3283	13.3467	0.6964	25.1102	0.1063	0	0	0.0729	0	0.0729	0	100	0
8	11	6.0017	3.7447	0.2344	8.4523	0.0402	0	0	0.0729	0	0.0729	0	100	0
8	12	14.0669	9.2173	0.572	20.6246	0.0862	0	0	0.0729	0	0.0729	0	100	0
8	13	0.4343	−0.3379	0.1029	3.7103	0.0224	0	0	0.0729	0	0.0729	0	100	0
8	14	12.9196	8.2041	0.4689	16.9054	0.0749	0	0	0.0729	0.625	0.6979	0	10.44	89.56
8	15	20.3025	12.6472	0.6618	23.8639	0.1	0	0.625	0.0729	0	0.6979	89.56	10.44	0
8	16	0.7273	0.7062	−0.0175	−0.63	−0.0087	0	0	0	0	0	0	0	0
9	1	19.0866	13.801	0.6956	25.0805	0.1067	0	0	0.0797	0	0.0797	0	100	0
9	2	23.4011	15.4022	0.8062	29.0677	0.1362	0	0	0.0797	0	0.0797	0	100	0
9	3	24.2636	14.0356	0.8069	29.094	0.1585	0	0	0.0797	0	0.0797	0	100	0
9	4	23.0618	13.7204	0.7603	27.4122	0.137	0	0	0.0797	0	0.0797	0	100	0
9	5	19.2953	12.3324	0.6838	24.6546	0.1191	0	0	0.0797	0	0.0797	0	100	0
9	6	16.4524	11.6941	0.5833	21.033	0.0966	0	0	0.0797	0	0.0797	0	100	0
9	7	8.8155	6.193	0.4081	14.7154	0.0678	0	0	0.0797	0	0.0797	0	100	0
9	8	18.3421	12.4823	0.6492	23.4094	0.095	0	0	0.0797	0	0.0797	0	100	0
9	9	22.5571	15.4221	0.8241	29.7153	0.1201	0	0	0.0797	0	0.0797	0	100	0
9	10	18.2863	13.1397	0.6724	24.2444	0.0988	0	0	0.0797	0	0.0797	0	100	0
9	11	−1.5339	−0.5868	−0.0006	−0.0218	−0.0198	0	0	0.0797	0	0.0797	0	100	0
9	12	13.9602	9.1693	0.5547	20.0022	0.0819	0	0	0.0797	0	0.0797	0	100	0
9	13	1.1827	1.2849	0.1107	3.9916	0.0024	0	0	0.0797	0	0.0797	0	100	0
9	14	10.2757	6.1288	0.3969	14.3106	0.0711	0	0	0.0797	0.625	0.7047	0	11.31	88.69
9	15	19.4095	11.4849	0.732	26.3918	0.1116	0	0.625	0.0797	0	0.7047	88.69	11.31	0
9	16	−0.4746	0.3	0.0649	2.3389	0.0106	0	0	0	0	0	0	0	0
10	1	19.6155	13.2592	0.7151	25.784	0.1137	0	0	0.0865	0	0.0865	0	100	0
10	2	24.4255	14.2114	0.8452	30.474	0.1541	0	0	0.0865	0	0.0865	0	100	0
10	3	25.1167	12.0723	0.8229	29.6706	0.1783	0	0	0.0865	0	0.0865	0	100	0
10	4	23.9367	12.0867	0.8302	29.934	0.1595	0	0	0.0865	0	0.0865	0	100	0
10	5	20.499	11.2772	0.6949	25.0561	0.1257	0	0	0.0865	0	0.0865	0	100	0
10	6	18.4277	10.342	0.652	23.5077	0.1136	0	0	0.0865	0	0.0865	0	100	0
10	7	10.6829	8.2331	0.4943	17.8212	0.0797	0	0	0.0865	0	0.0865	0	100	0
10	8	21.0351	13.5697	0.6934	25.0025	0.1016	0	0	0.0865	0	0.0865	0	100	0
10	9	23.3546	15.5724	0.8319	29.9961	0.1265	0	0	0.0865	0	0.0865	0	100	0
10	10	20.2733	13.206	0.7226	26.0547	0.1094	0	0	0.0865	0	0.0865	0	100	0
10	11	−2.2709	−1.6818	−0.003	−0.1081	−0.0191	0	0	0.0865	0	0.0865	0	100	0
10	12	15.5394	9.154	0.5767	20.7948	0.0875	0	0	0.0865	0	0.0865	0	100	0
10	13	2.338	0.6958	0.1166	4.204	0.0286	0	0	0.0865	0	0.0865	0	100	0
10	14	11.8371	7.0502	0.4485	16.1702	0.0781	0	0	0.0865	0.625	0.7115	0	12.16	87.84
10	15	18.9643	11.9052	0.7159	25.8125	0.1082	0	0.625	0.0865	0	0.7115	87.84	12.16	0
10	16	23.3683	12.0328	0.7792	28.0962	0.1577	0.1275	0	0	0	0.1275	0	100	0
11	1	18.6802	11.5742	0.6796	24.5045	0.1057	0	0	0.0933	0	0.0933	0	100	0
11	2	25.0222	13.9863	0.8039	28.9852	0.1512	0	0	0.0933	0	0.0933	0	100	0
11	3	25.6394	13.1215	0.8122	29.2838	0.1687	0	0	0.0933	0	0.0933	0	100	0
11	4	24.6744	14.5183	0.7802	28.132	0.1536	0	0	0.0933	0	0.0933	0	100	0
11	5	19.3295	12.6135	0.685	24.6995	0.1225	0	0	0.0933	0	0.0933	0	100	0
11	6	18.7665	11.7823	0.6491	23.4044	0.1112	0	0	0.0933	0	0.0933	0	100	0
11	7	12.0459	8.262	0.4669	16.8355	0.0746	0	0	0.0933	0	0.0933	0	100	0
11	8	19.7356	12.2924	0.7225	26.0526	0.1072	0	0	0.0933	0	0.0933	0	100	0
11	9	23.3494	14.4131	0.8518	30.7139	0.1298	0	0	0.0933	0	0.0933	0	100	0
11	10	19.1323	12.6849	0.7094	25.5779	0.105	0	0	0.0933	0	0.0933	0	100	0
11	11	−0.9895	−0.2695	−0.004	−0.1435	−0.0127	0	0	0.0933	0	0.0933	0	100	0
11	12	14.8304	10.1963	0.582	20.9867	0.0899	0	0	0.0933	0	0.0933	0	100	0
11	13	2.208	2.5587	0.1029	3.7107	0.0204	0	0	0.0933	0	0.0933	0	100	0
11	14	10.9763	6.4266	0.3918	14.1258	0.0707	0	0	0.0933	0.625	0.7183	0	12.99	87.01
11	15	18.1906	10.6621	0.698	25.1685	0.106	0	0.625	0.0933	0	0.7183	87.01	12.99	0
11	16	−0.9643	−0.7161	0.0392	1.4143	−0.0048	0	0	0	0	0	0	0	0
12	1	15.4588	10.1833	0.5953	21.4632	0.1001	0	0	0.1002	0	0.1002	0	100	0
12	2	24.7319	13.6012	0.8478	30.5688	0.161	0	0	0.1002	0	0.1002	0	100	0
12	3	26.8912	12.8758	0.8008	28.8754	0.1851	0	0	0.1002	0	0.1002	0	100	0
12	4	24.6558	12.9216	0.8196	29.5504	0.1758	0	0	0.1002	0	0.1002	0	100	0
12	5	20.5267	12.1018	0.7215	26.0139	0.1329	0	0	0.1002	0	0.1002	0	100	0
12	6	18.4287	11.4481	0.6811	24.5589	0.1172	0	0	0.1002	0	0.1002	0	100	0
12	7	13.4393	9.372	0.4909	17.6995	0.0793	0	0	0.1002	0	0.1002	0	100	0
12	8	21.0809	13.9911	0.7512	27.0875	0.111	0	0	0.1002	0	0.1002	0	100	0
12	9	23.772	15.0448	0.8517	30.7084	0.1339	0	0	0.1002	0	0.1002	0	100	0
12	10	19.8095	12.8912	0.7381	26.6137	0.1093	0	0	0.1002	0	0.1002	0	100	0
12	11	−1.4941	−1.399	−0.0134	−0.4846	−0.018	0	0	0.1002	0	0.1002	0	100	0
12	12	16.0743	10.6539	0.5977	21.5507	0.092	0	0	0.1002	0	0.1002	0	100	0
12	13	2.0581	1.6359	0.1105	3.986	0.0298	0	0	0.1002	0	0.1002	0	100	0
12	14	10.744	6.4761	0.4184	15.0852	0.076	0	0	0.1002	0.625	0.7252	0	13.81	86.19
12	15	18.2843	10.3265	0.6975	25.1492	0.112	0	0.625	0.1002	0	0.7252	86.19	13.81	0
12	16	−0.4083	−1.1083	0.0632	2.2805	0.02	0	0	0	0	0	0	0	0
13	1	17.3784	11.3659	0.6531	23.5471	0.1026	0	0	0.107	0	0.107	0	100	0
13	2	24.8735	13.9698	0.8645	31.1714	0.1634	0	0	0.107	0	0.107	0	100	0
13	3	26.731	13.2379	0.8304	29.9397	0.1799	0	0	0.107	0	0.107	0	100	0
13	4	25.0125	13.3208	0.8199	29.5626	0.1706	0	0	0.107	0	0.107	0	100	0
13	5	20.9959	12.5637	0.7	25.2389	0.1263	0	0	0.107	0	0.107	0	100	0
13	6	19.7859	13.0643	0.6384	23.0182	0.1112	0	0	0.107	0	0.107	0	100	0
13	7	12.7701	8.6484	0.4737	17.0786	0.0821	0	0	0.107	0	0.107	0	100	0
13	8	19.9798	12.3643	0.7421	26.7561	0.1113	0	0	0.107	0	0.107	0	100	0
13	9	23.9004	15.4262	0.8368	30.1725	0.1326	0	0	0.107	0	0.107	0	100	0
13	10	20.1688	14.395	0.7685	27.7093	0.1134	0	0	0.107	0	0.107	0	100	0
13	11	−1.5531	−0.2131	0.0003	0.0093	−0.0139	0	0	0.107	0	0.107	0	100	0
13	12	16.261	10.9519	0.6007	21.66	0.0928	0	0	0.107	0	0.107	0	100	0
13	13	2.1579	1.7026	0.1307	4.7131	0.0287	0	0	0.107	0	0.107	0	100	0
13	14	10.3449	7.0881	0.4013	14.4697	0.0725	0	0	0.107	0.625	0.732	0	14.62	85.38
13	15	17.9906	12.3676	0.6892	24.8485	0.1057	0	0.625	0.107	0	0.732	85.38	14.62	0
13	16	24.9296	12.3107	0.7853	28.3135	0.1895	0.1275	0	0	0	0.1275	0	100	0
14	1	19.7006	13.895	0.7196	25.9447	0.1225	0	0	0.1138	0	0.1138	0	100	0
14	2	24.628	13.7864	0.8645	31.1715	0.1715	0	0	0.1138	0	0.1138	0	100	0
14	3	27.0603	12.7211	0.8226	29.6605	0.2007	0	0	0.1138	0	0.1138	0	100	0
14	4	24.9719	12.0514	0.83	29.9259	0.1896	0	0	0.1138	0	0.1138	0	100	0
14	5	20.0669	11.3486	0.7334	26.4431	0.1416	0	0	0.1138	0	0.1138	0	100	0
14	6	19.3148	11.3116	0.7073	25.5033	0.128	0	0	0.1138	0	0.1138	0	100	0
14	7	13.0698	9.2496	0.5178	18.6703	0.0862	0	0	0.1138	0	0.1138	0	100	0
14	8	21.4825	14.0766	0.7634	27.5263	0.1153	0	0	0.1138	0	0.1138	0	100	0
14	9	23.8379	15.3459	0.8607	31.0347	0.1367	0	0	0.1138	0	0.1138	0	100	0
14	10	21.5278	13.8928	0.7851	28.3081	0.1137	0	0	0.1138	0	0.1138	0	100	0
14	11	−2.1621	−1.2165	−0.0091	−0.3271	−0.0078	0	0	0.1138	0	0.1138	0	100	0
14	12	17.3041	11.5725	0.646	23.2923	0.0958	0	0	0.1138	0	0.1138	0	100	0
14	13	1.949	2.0565	0.0896	3.2302	0.028	0	0	0.1138	0	0.1138	0	100	0
14	14	9.3689	6.5087	0.3449	12.4353	0.0636	0	0	0.1138	0.625	0.7388	0	15.41	84.59
14	15	18.4324	12.0276	0.6914	24.9297	0.1067	0	0.625	0.1138	0	0.7388	84.59	15.41	0
14	16	−0.7558	−0.6898	0.0165	0.5934	0.0011	0	0	0	0	0	0	0	0
15	1	18.1472	11.9418	0.6987	25.1939	0.1082	0	0	0.1207	0	0.1207	0	100	0
15	2	24.7631	13.6604	0.8641	31.1563	0.1697	0	0	0.1207	0	0.1207	0	100	0
15	3	26.1211	11.8227	0.834	30.0705	0.2037	0	0	0.1207	0	0.1207	0	100	0
15	4	24.5677	11.9552	0.7923	28.5692	0.1875	0	0	0.1207	0	0.1207	0	100	0
15	5	20.0898	11.474	0.7193	25.9371	0.144	0	0	0.1207	0	0.1207	0	100	0
15	6	19.3675	11.6613	0.6822	24.5972	0.1254	0	0	0.1207	0	0.1207	0	100	0
15	7	12.9911	8.3415	0.5124	18.477	0.0905	0	0	0.1207	0	0.1207	0	100	0
15	8	19.4851	12.9013	0.711	25.6353	0.1146	0	0	0.1207	0	0.1207	0	100	0
15	9	23.6077	14.5462	0.8618	31.074	0.1436	0	0	0.1207	0	0.1207	0	100	0
15	10	21.2589	13.7735	0.7922	28.5624	0.1207	0	0	0.1207	0	0.1207	0	100	0
15	11	−1.3789	−1.3203	0.0019	0.0686	−0.0106	0	0	0.1207	0	0.1207	0	100	0
15	12	16.8366	10.3498	0.6489	23.3953	0.1014	0	0	0.1207	0	0.1207	0	100	0
15	13	2.5374	0.8067	0.138	4.9742	0.0357	0	0	0.1207	0	0.1207	0	100	0
15	14	11.1396	7.0915	0.4088	14.741	0.0773	0	0	0.1207	0.625	0.7457	0	16.18	83.82
15	15	17.5426	10.4944	0.7045	25.4019	0.1136	0	0.625	0.1207	0	0.7457	83.82	16.18	0
15	16	−0.4051	−0.4444	0.0729	2.6294	0.0112	0	0	0	0	0	0	0	0
16	1	15.0725	8.0994	0.5869	21.1613	0.0985	0	0	0.1275	0	0.1275	0	100	0
16	2	24.67	8.6858	0.7009	25.2716	0.2051	0	0	0.1275	0	0.1275	0	100	0
16	3	27.4278	6.3099	0.707	25.4923	0.2645	0	0	0.1275	0	0.1275	0	100	0
16	4	24.8032	6.1186	0.6967	25.1217	0.2372	0	0	0.1275	0	0.1275	0	100	0
16	5	20.9479	7.854	0.6707	24.1843	0.1784	0	0	0.1275	0	0.1275	0	100	0
16	6	19.4346	9.972	0.6893	24.8548	0.1408	0	0	0.1275	0	0.1275	0	100	0
16	7	14.3144	8.9315	0.5183	18.6864	0.0889	0	0	0.1275	0	0.1275	0	100	0
16	8	20.6449	13.6205	0.7023	25.3217	0.1142	0	0	0.1275	0	0.1275	0	100	0
16	9	24.2561	14.785	0.854	30.7919	0.1506	0	0	0.1275	0	0.1275	0	100	0
16	10	21.0486	14.0733	0.6995	25.2209	0.1084	0	0	0.1275	0	0.1275	0	100	0
16	11	−2.2759	−0.0846	0.0413	1.4879	0.024	0	0	0.1275	0	0.1275	0	100	0
16	12	17.1423	10.7518	0.5869	21.1613	0.0898	0	0	0.1275	0	0.1275	0	100	0
16	13	3.0092	2.0883	0.2069	7.4586	0.0432	0	0	0.1275	0	0.1275	0	100	0
16	14	12.8714	7.6083	0.5142	18.5415	0.1069	0	0	0.1275	0.625	0.7525	0	16.94	83.06
16	15	17.5841	9.9481	0.6294	22.6946	0.129	0	0.625	0.1275	0	0.7525	83.06	16.94	0
16	16	25.0686	11.1805	0.8288	29.884	0.1822	0.1275	0	0	0	0.1275	0	100	0

Claims

1. A method for producing a hydrogen-rich gas which comprises: contacting a CO-containing gas with a water gas shift catalyst in the presence of water at a temperature of not more than about 450° C., wherein the water gas shift catalyst comprises: a) Pt, its oxides or mixtures thereof, b) at least one of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, their oxides and mixtures thereof, and c) at least one of Sc, Y, Ti, Zr, V, Nb, Ta, Cr, Mo, W, Mn, Fe, Co, Ir, Ni, Pd, La, Ce, Pr, Nd, Sm, Eu, their oxides and mixtures thereof.

2. The method according to claim 1, wherein the CO-containing gas is a syngas.

3. The method according to claim 1, wherein the water gas shift catalyst comprises at least one of Li, Na, K, their oxides and mixtures thereof.

4. The method according to claim 3, wherein the water gas shift catalyst comprises Fe, its oxides or mixtures thereof.

5. The method according to claim 3, wherein the water gas shift catalyst is selected from the group consisting of Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Zr, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and La, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Y, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Mo, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Mn, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, Zr, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof; and Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof.

6. The method according to claim 1, wherein the water gas shift catalyst is supported in a carrier selected from alumina, zirconia, titania, ceria, magnesia, lanthania, niobia, zeolite, perovskite, silica clay, yttria, iron oxide or mixtures thereof.

7. The method according to claim 6, wherein the water gas shift catalyst comprises at least one of Li, Na, K, their oxides or mixtures thereof.

8. The method according to claim 7, wherein the water gas shift catalyst comprises Fe, its oxides or mixtures thereof.

9. The method according to claim 7, wherein the supported water gas shift catalyst is selected from: Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof and Zr, its oxides or mixtures thereof on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and La, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Y, its oxides or mixtures thereof on Al2O3; Pt, its oxides or mixtures thereof. Na, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof and Mo, its oxides or mixtures thereof on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof. Na, its oxides or mixtures thereof and Co, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof and Mn, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, Zr, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof, on ZrO2; and Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof, on ZrO2.

10. The method according to claim 9, wherein the Al2O3 is γ-Al2O3.

11. The method according to claim 6, wherein the carrier comprises at least one member selected from the group consisting of iron oxide zirconia, titania and ceria.

12. The method according to claim 11, wherein the carrier comprises zirconia.

13. The method according to claim 1, wherein the CO-containing gas is contacted with the water gas shift catalyst at a temperature ranging from about 150° C. to about 450° C.

14. The method according to claim 13, wherein the CO-containing gas is contacted with a water gas shift catalyst at a temperature ranging from more than about 350° C. to up to about 450° C.

15. The method according to claim 13, wherein the CO-containing gas is contacted with a water gas shift catalyst at a temperature ranging from about 250° C. to up to about 350° C.

16. The method according to claim 13, wherein the CO-containing gas is contacted with a water gas shift catalyst at a temperature ranging from about 150° C. to up to about 250° C.

17. The method according to claim 1, wherein the CO-containing gas is contacted with the water gas shift catalyst at a pressure of no more than about 75 bar.

18. The method according to claim 17, wherein the CO-containing gas is contacted with the water gas shift catalyst at a pressure of no more than about 50 bar.

19. The method according to claim 17, wherein the CO-containing gas is contacted with the water gas shift catalyst at a pressure of no more than about 15 bar.

20. The method according to claim 17, wherein the CO-containing gas is contacted with the water gas shift catalyst at a pressure of no more than about 1 bar.

21. The method according to claim 1, wherein the water gas shift catalyst comprises about 0.01 wt. % to about 10 wt. %, with respect to the total weight of all catalyst components plus the support material, of each Group 8, 9 or 10 element present in the water gas shift catalyst.

22. The method according to claim 21, wherein the water gas shift catalyst comprises about 0.01 wt. % to about 2 wt. % of each Group 8, 9 or 10 element present in the water gas shift catalyst.

23. The method according to claim 22, wherein the water gas shift catalyst comprises about 0.05 wt. % to about 0.5 wt. % of each Group 8, 9 or 10 element present in the water gas shift catalyst.

24. The method according to claim 1, wherein the water gas shift catalyst comprises about 0.05 wt. % to about 20 wt. %, with respect to the total weight of all catalyst components plus the support material, of each lanthanide element present in the water gas shift catalyst.

25. A catalyst for catalyzing the water gas shift reaction comprising: a) Pt, its oxides or mixtures thereof, b) at least one of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, their oxides and mixtures thereof, and c) at least one of Sc, Y, Ti, Zr, V, Nb, Ta, Cr, Mo, W, Mn, Fe, Co, Ir, Ni, Pd, La, Ce, Pr, Nd, Sm, Eu, their oxides and mixtures thereof.

26. The catalyst according to claim 25, wherein the catalyst comprises at least one of Li, Na, K, their oxides and mixtures thereof.

27. The catalyst according to claim 26, wherein the catalyst comprises Fe, its oxides or mixtures thereof.

28. The catalyst according to claim 26, wherein the catalyst is selected from the group consisting of: Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Zr, its oxides or mixtures thereof, Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and La, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Y, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Mo, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Mn, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, Zr, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof; Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof; and Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof.

29. The catalyst according to claim 25, further comprising a support selected from alumina, zirconia, titania, ceria, magnesia, lanthania, niobia, zeolite, perovskite, silica clay, yttria, iron oxide or mixtures thereof.

30. The catalyst according to claim 29, wherein the catalyst comprises at least one of Li, Na, K, their oxides and mixtures thereof.

31. The catalyst according to claim 29, wherein the catalyst comprises Fe, its oxides, or mixtures thereof.

32. The catalyst according to claim 30, wherein the supported catalyst is selected from: Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, Li, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Zr, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and La, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Y, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Mo, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Mn, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, Zr, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof, on Al2O3; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, Na, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Fe, its oxides or mixtures thereof, on ZrO2; Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Co, its oxides or mixtures thereof, on ZrO2; and Pt, its oxides or mixtures thereof, K, its oxides or mixtures thereof, and Ce, its oxides or mixtures thereof, on ZrO2.

33. The catalyst according to claim 32, wherein the Al2O3 is γ-Al2O3.

34. The catalyst according to claim 25, wherein the catalyst comprises about 0.01 wt. % to about 10 wt. %, with respect to the total weight of all catalyst components plus the support material, of each Group 8, 9 or 10 element present in the catalyst.

35. The catalyst according to claim 34, wherein the catalyst comprises about 0.01 wt. % to about 2 wt. % of each Group 8, 9 or 10 element present in the catalyst.

36. The catalyst according to claim 35, wherein the catalyst comprises about 0.05 wt. % to about 0.5 wt. % of each Group 8, 9 or 10 element present in the catalyst.

37. The catalyst according to claim 25, wherein the catalyst comprises about 0.05 wt. % to about 20 wt. %, with respect to the total weight of all catalyst components plus the support material, of each lanthanide element present in the catalyst.

38. A catalyst for catalyzing the water gas shift reaction comprising: a) Pt, its oxides or mixtures thereof; b) at least one of V, Zr, their oxides and mixtures thereof; and c) at least one of Ti, Mo, Co, their oxides and mixtures thereof.

39. The catalyst according to claim 38, wherein the catalyst further comprises Na, its oxides or mixtures thereof.

40. A method for producing a hydrogen-rich syngas which comprises: contacting a CO-containing gas with a water gas shift catalyst in the presence of water at a temperature of not more than about 450° C., wherein the water gas shift catalyst comprises: a) Pt, its oxides or mixtures thereof; b) at least one of V, Zr, their oxides and mixtures thereof, and c) at least one of Ti, Mo, Co, their oxides and mixtures thereof.

41. The method according to claim 40, wherein the water gas shift catalyst further comprises Na, its oxides or mixtures thereof.

42. A method of preparing a catalyst comprising the steps of applying Li and Fe containing precursors to a surface; calcining the Li and Fe containing surface to a temperature of between about 600° C. and about 900° C. to form a treated surface; applying a Pt containing precursor to the treated surface.

43. A method according to claim 42, wherein Na is impregnated onto the treated surface after the calcination step.

44. A method according to claim 42, wherein the temperature is about 700° C.

45. A fuel processing system for generation of a hydrogen-rich gas from a hydrocarbon or substituted hydrocarbon fuel, the fuel processing system comprising: a fuel reformer for converting a fuel reactant stream comprising a hydrocarbon or a substituted hydrocarbon fuel to a reformed product stream comprising carbon monoxide and water, the fuel reformer having an inlet for receiving the reactant stream, a reaction chamber for converting the reactant stream to the product stream and an outlet for discharging the product stream; a water gas shift reactor for effecting a water gas shift reaction at a temperature of less than about 450° C., the water gas shift reactor comprising an inlet for receiving a water gas shift feed stream comprising carbon monoxide and water from the product stream of the fuel reformer, a reaction chamber comprising the water gas shift catalyst of claim 25, the water gas shift catalyst being effective for generating hydrogen and carbon dioxide from the water gas shift feed stream and an outlet for discharging the resulting hydrogen-rich gas; and a temperature controller adapted for maintaining the temperature of the reaction chamber of the water gas shift reactor at a temperature of less than about 450° C.