Patent Application
20050066817
This application claims the priorities of German patent applications Serial Nos 103 37 584.8 filed Aug. 16, 2003 and 103 46 061.6 flied Oct. 4, 2003.
The invention concerns a mechanically stable porous activated carbon molded or shaped body, referred to hereinafter as a molded body.
The invention also concerns a process for the production of the activated carbon molded body, as well as a filter system including the activated carbon molded body.
DE 101 04 882 A1 discloses an activated carbon molded body having a very high proportion of activated carbon and a correspondingly high adsorption capability. The activated carbon is bound in that case by way of pyrolised phenolic resin. Clay is added to the starting mixture involved in production of the activated carbon molded body, as a filler or also as an extrusion additive. However the clay does not sinter together at the pyrolysis temperatures used. As no separate binding agent is added for the clay, that activated carbon molded body does not have a particularly high level of mechanical stability. The relatively low level of mechanical stability therefore means that the activated carbon molded body produced in that fashion is not suitable for durable reliable use in a motor vehicle.
In order to enhance the mechanical stability of the above-discussed molded body, it would be possible to assume that an increase in the proportion of resin, with a corresponding reduction in the proportion of clay, would necessarily result in an improvement in the level of mechanical stability. In manufacturing activated carbon molded bodies, the usual procedure is for the individual components to be mixed together and then extruded. As however activated carbon does not exhibit a plastic behaviour, the activated carbon as such is not extrudable. The clay added as indicated above means that it is possible to extrude the starting mixture. Accordingly, when the proportion of clay in the starting mixture is reduced, that mixture tends to lose its extrusion capability. In that respect it is not possible to increase the amount of resin to the detriment of the amount of clay in order to produce a molded body which is possibly mechanically more stable as such a starting mixture is then no longer extrudable.
The motor vehicle industry however is increasingly demanding filter systems of smaller dimensions, with a higher capacity for pollutants and enhanced stability. Particularly in the case of tank venting systems for motor vehicles, the available structural space is becoming less and less for example in the small two-seater or four-seater ‘city automobiles’ which are being built nowadays. Having regard to the increased ecological requirements, more specifically in regard to the vaporous emission of fuel from motor vehicles, there is a need for the reduced-size filter systems now involved to also have a corresponding adsorption capacity. In addition it is desirable for the service life of the filter systems to be improved by increasing mechanical stability.
Accordingly there is a need for a filter system which enjoys improved stability and an increased adsorption capability.
An object of the invention is to provide an activated carbon molded body which enjoys good mechanical stability and which is sufficiently porous to provide for appropriate adsorption effects.
Another object of the present invention is to provide an activated carbon molded body which affords good stability and adsorption capability while being simple to manufacture.
A further object of the invention is to provide a process for the production of a mechanically stable porous activated carbon molded body which while affording satisfactory results is simple and straightforward to implement.
Yet a further object of the present invention is to provide a filter system including a mechanically stable porous activated carbon molded body, such as to enjoy a level of adsorption capability for pollutants as to satisfy the requirements imposed thereon nowadays.
In accordance with the present invention the foregoing and other objects are attained in respect of the molded body by a mechanically stable porous activated carbon molded body comprising a support or lattice structure including carbonised resin and pyrolised silicone resin, and activated carbon particles embedded in said structure.
The above-indicated objects are further attained in accordance with the invention by a filter system including an activated carbon molded body in accordance with the invention.
In the process aspect the foregoing and other objects are attained by a process for the production of a mechanically stable porous activated carbon molded body comprising the steps of mixing activated carbon particles, carbonisable resin, pyrolisable resin and optionally further additives with the addition of a liquid phase to provide a workable mass, shaping the mass obtained to give a molded body, drying the molded body and pyrolysing the dried molded body.
Further preferred features of the invention are set forth in the appendant claims hereinafter.
In relation to the present invention it was surprisingly found that it is possible to obtain an activated carbon molded body which enjoys improved mechanical stability and an enhanced adsorption capability if pyrolisable silicone resin is added to a starting mixture besides activated carbon particles and carbonisable resin. Surprisingly the silicone resin increases the plasticity of the starting mixture so that it can be worked and processed using conventional shaping and molding procedures, in particular extrusion. When using silicone resin in the starting mixture for production of the activated carbon molded body according to the invention, there is no necessity to add clay as is required in DE 101 04 882 A1 as discussed hereinbefore in an increased proportion of up to 50% by weight. An addition of silicone resin has the great advantage of permitting working and processing of the starting mixture by extrusion without clay being added to the mixture.
Accordingly with the activated carbon molded body according to the invention it is possible to increase both the proportion of activated carbon and also the proportion of carbonised resin, wherein workability is possible during production of the activated carbon molded body by means of extrusion by virtue of the addition of the silicone resin.
Use of the silicone resin means that it is also possible to markedly reduce the addition of additives which are necessary in the state of the art such as plasticisers, for example oleic acid, or lubricants, for example glycerin and soap. The reduction in the further additives which are usually necessary such as plasticisers and lubricants further makes it possible to increase the proportions of activated carbon and carbonised phenolic resin in the activated carbon molded body according to the invention.
In accordance with a preferred feature of the invention the silicone resin is in the form of a liquid silicone resin, for example a polysiloxane.
In accordance with a further preferred feature the silicone resin is used in powder form.
It has been found that it may be advantageous to use liquid and powder polysiloxane together in the starting mixture. It has further been found that, when using polysiloxane in powder form, the density of the activated carbon molded body produced in that way can be increased. That makes it possible to further improve the sorption properties of the molded body according to the invention.
In accordance with a preferred embodiment of the invention the silicone resin is a polymer containing a plurality of units in accordance with formula I:
in which R1 and R2 may each be the same or different and stand for a substance selected from the group consisting of alkyl, alkenyl and aryl which can each be substituted or unsubstituted or for hydrogen, with the proviso that R1 and R2 are not both hydrogen at the same time.
The silicone resin to be used can accordingly also be referred to as polyorganosiloxane.
The terminal groups which are not shown in formula I can be reproduced for example by following formula II:
In formula II R1, R2 and R3 may each be the same or different and stand for a substance selected from the group consisting of alkyl, alkenyl and aryl which can each be substituted or unsubstituted or for hydrogen, with the proviso that at least one of R1, R2 and R3 does not stand for hydrogen.
In accordance with a preferred feature the silicone resin is selected from the group consisting of methyl silicone rubber, dimethyl silicone rubber, methyl phenyl silicone rubber, methyl vinyl silicone rubber and mixtures thereof.
Another preferred feature of the invention provides that the silicone resin is present in the pyrolised condition substantially as an SiO2 lattice or support structure.
Upon carbonisation of the resin used the added silicone resin also undergoes pyrolysis, forming an SiO2 lattice structure. The SiO2 structure which is formed during the pyrolysis operation can also contribute to the binding of activated carbon particles. In addition the SiO2 structure formed advantageously also enhances the mechanical stability of the activated carbon molded body according to the invention.
In accordance with a further preferred feature the resin has aromatic nuclei. In a further preferred feature the resin is selected from the group consisting of phenolic resin, furan resin, epoxy resin, unsaturated polyester resin and mixtures thereof. In a further preferred feature in this respect the phenolic resin is a novolak.
It has been found that, when using resins with aromatic nuclei, in the pyrolysis operation, the procedure gives rise to a porous carbon structure which is particularly suitable for the purposes involved herein. That carbon structure on the one hand reliably fixes the activated carbon particles and, by virtue of the porous structure afforded, permits access for substances which are to be adsorbed, to the activated carbon particles. In addition the carbon structure produced in that way itself appears to afford a certain sorption capability.
It has been found that the molded body according to the invention enjoys excellent embedding or fixing of activated carbon particles in the three-dimensional lattice structure produced by carbonisation of preferably synthetic resin.
In a further preferred feature the activated carbon particles are substantially completely bound by the carbonised resin.
In a further preferred feature the activated carbon molded body according to the invention contains less than about 20% by weight of calcined and/or refractory material, preferably less than about 15% of calcined ceramic and/or refractory material, in each case with respect to the total weight of the activated carbon molded body. In a further preferred feature the activated carbon molded body contains less than about 10% of calcined ceramic and/or refractory material with respect to the total weight of the molded body.
The small proportion of calcined ceramic and/or refractory material in the starting mixture for production of the molded body means that it is: possible to increase the proportion of resin to be carbonised and activated carbon particles in order to provide an activated carbon molded body which enjoys enhanced mechanical stability and improved adsorption capability.
In a further preferred embodiment of the invention the activated carbon molded body contains between about 15% by weight and about 60% by weight, preferably between about 20% by weight and 50% by weight of carbonised resin, with respect to the total weight of the molded body. It is further preferred for the activated carbon molded body to contain between about 0.50/c by weight and about 25% by weight and preferably between about 2% by weight and about 20% by weight of pyrolised silicone resin.
It will be noted at this juncture that the proportions specified in percent by weight hereinbefore and hereinafter relate in each case to the total weight of the activated carbon molded body unless otherwise stated.
In accordance with a further embodiment of the invention the activated carbon molded body contains between about 15% by weight and about 60% by weight, preferably between about 30% by weight and about 50% by weight of activated carbon.
The lattice structure which is produced from carbonisation of resin, preferably synthetic resin, preferably binds the activated carbon or activated carbon particles. The activated carbon or the particles thereof are partially embedded in or fixed to the porous carbon structure produced upon carbonisation of the resin so that the result is an abrasion-resistant, mechanically stable structure enjoying a very good level of sorption capability. A porous carbon which is produced by the carbonisation of resin is referred to as glass-like carbon.
The SiO2 lattice structure produced by the pyrolysis of silicone resin can also lead to binding, fixing or embedding of the activated carbon particles. In addition, the SiO2 lattice structure produced also provides for stabilisation of the activated carbon molded body produced.
Preferably no clay is added in production of the molded body according to the invention. It has been found that, when using calcined ceramic and/or refractory material, instead of the clay which is usually employed in prior procedures, production of the activated carbon molded body according to the invention affords a reduction in the water content in the entire batch and thus a reduction in the degree of drying shrinkage. Preferably fire clay is used as the ceramic material and/or calcined refractory material.
A further preferred embodiment of the invention provides that the activated carbon molded body contains stabilisation fibers. For example glass fibers and/or carbon fibers can be used for that purpose. It is noted that the addition of stabilisation fibers advantageously improves mechanical stability of the porous molded body of the invention.
It has been found that a passage structure affords a sufficiently large area for substances to be adsorbed, usually pollutants. That structure at the same time affords satisfactory mechanical stability.
In accordance with a preferred feature of the activated carbon molded body it has a passage structure. That structure may have passages which extend through the body and/or passages which do not extend entirely therethrough. The passages may extend in a straight line and/or in a configuration differing from a straight line, for example in a wavy or corrugated configuration. The activated carbon molded body is accordingly preferably in the form of a molded body with passages extending therethrough, the passages preferably being straight.
The passages may be of any desired geometrically regular and/or irregular, that is to say general shape. A geometrically regular shape has proven to be an advantageous shape for a passage cross-section, in particular a tetragonal, preferably square, hexagonal, octagonal and/or circular shape.
The term shape of a passage cross-section is used to denote the shape of the cross-section of an individual passage, the cross-section being perpendicular to the axis of the passage. In the case of passages which are not straight the axis of the passage is similarly not straight. The shape of the passage cross-section of the individual passages is simply referred to hereinafter as the passage shape.
It was found that the passage shape has an influence on the flow resistance of the activated carbon molded body. It was found in this respect that, in the case of a gas which is passed through the activated carbon molded body, in dependence on the passage shape, regions are formed involving differing flow speeds.
This signifies that a flow resistance is set in dependence on the passage shape. That flow resistance can be measured by recording the pressure of the gas before it flows into the activated carbon molded body and after it flows out of the body. The pressure drop in the flow is then a measurement in respect of the flow resistance in the activated carbon molded body.
The internal wall surfaces of the individual passages act as frictional surfaces and are responsible to a considerable extent for the pressure drop. It has been found that, with the same sum of the surface areas of the passage cross-sections, the pressure drop is dependent on the passage shape.
The area of the cross-section of an passage is referred to hereinafter as the passage cross-sectional area. The sum of the passage cross-sectional areas is referred to hereinafter as the open area.
In addition the term frictional surface is used to denote the internal wall surface of the passage. When a passage is of a circular passage shape, the frictional surface is of smaller area than for all other passage shapes of the same passage cross-sectional area.
When a gas flows through an activated carbon molded body of a square passage shape, lower flow speeds occur in the corner regions, in comparison with flow speeds in the proximity of the passage axis. The greater the passage shape approaches a circular passage shape, the correspondingly smaller become the regions which involve low flow speeds. A regularly hexagonal passage shape comes close to a circular passage shape, in which respect, with the regularly hexagonal passage shape, it is also possible to optimise the open area and accordingly it is possible to achieve a large open area.
In comparative measurement procedures, it was found that an activated carbon molded body which involves a regularly hexagonal passage shape exhibits a lower flow resistance compared to an activated carbon molded body involving a square or tetragonal passage shape of the same passage cross-sectional area.
Accordingly the pressure drop in an activated carbon molded body which has passages of a hexagonal passage shape is less than in an activated carbon molded body having passages of a tetragonal passage shape.
In a preferred embodiment therefore the activated carbon molded body has a regularly hexagonal passage shape, that is to say a honeycomb structure.
In accordance with another preferred feature of the invention the activated carbon molded body has passages of a tetragonal passage cross-section as such an activated carbon molded body can be produced on conventional extruders.
It has been found that the activated carbon molded body of the invention can enjoy an extremely high level of mechanical stability, as indicated by the fact that in a preferred configuration wherein the activated carbon molded body is of a cylindrical shape with a diameter of substantially 30 mm, a length of substantially 100 mm and a cell provision of 200 cells per square inch (cpsi), that is to say 200 passages of approximately square or regular hexagonal cross-section, with the passages extending through the body, the molded body has a bursting force in parallel relationship with the direction in which the passages extend of at least 2000 N, preferably at least 2500 N. It is further preferred for the bursting force to be at least 3000 N, further preferably at least 3500 N or more preferably at least 4000 N.
An activated carbon molded body according to the invention of the above-specified dimensions also has an improved bursting force in perpendicular relationship to the direction in which the passages extend, the bursting force advantageously being at least 200 N and further preferably at least 400 N.
In the process for producing the mechanically stable porous activated carbon molded body according to the invention, which involves mixing the components as specified above, shaping them to provide a molded body, drying the molded body and pyrolysing the dried molded body, the liquid phase added in the mixing step is preferably an aqueous phase or water. The viscosity of the mixture can be adjusted by way of the amount of water added. The plasticity of the mixture or starting composition can further be adjusted by way of the added silicone resin, preferably polysiloxane.
Although the added silicone resin, preferably polyorganosiloxane imparts adequate plasticity or extrusion capability to the starting mixture, it will be appreciated that it is also possible to add further additives. For example it is possible to add wax to the mixture in order to provide for good slidability of the individual particles relative to each other, that is to say thereby to improve the factor of what is known as internal slidability. Improved internal slidability promotes homogeneous distribution of the individual constituents during extrusion of the material at the aperture of the extruder. In addition increasing internal slidability can have the extremely advantageous effect of at least substantially avoiding local accumulation or blockage effects in individual passages of the extruder aperture in the extrusion operation.
A tenside or soap can also be added to the starting material in the mixing step in order to improve sliding of the material in the extruder or at the extrusion tool. A comparable effect can be achieved if between about 10 and 50% by weight of the tenside or soap proportion is replaced by graphite powder.
The good plasticising effect of the silicone resin added means that the proportion of further additives can surprisingly be reduced. In that respect the mixture can contain on a percentage basis more activated carbon and carbonisable resin than was previously possible.
For the purposes of improving the strength of the article obtained after the extrusion operation, generally referred to as the green body, a preferred feature provides that a binding agent is added, for example liquid starch, cellulose ether or a cellulose derivative, for example methyl hydroxypropyl cellulose.
The cellulose ether referred to above binds the water added in the mixing step of the production process, outside the activated carbon, and thus contributes to stabillsatlon of the green body produced. In addition the green body binding agent also promotes homogenisation of the starting mixture comprising activated carbon, the optionally added ceramic or refractory material, silicone resin and the preferably synthetic carbonisable resin. In the starting mixture, the cellulose ether opposes separation thereof which is to be attributed to the differing densities of the various constituents.
By way of example the cellulose ether used may include methyl cellulose, ethylhydroxyethyl cellulose, hydroxybutyl cellulose, hydroxybutylmethyl cellulose, hydroxyethyl cellulose, hydroxymethyl cellulose, hydroxypropyl cellulose, methylhydroxypropyl cellulose, hydroxyethylmethyl cellulose, sodium carboxymethyl cellulose and mixtures thereof.
Preferably the amount of added green body binding agent, for example cellulose ether, is not more than about 5% by weight with respect to the total weight of the starting mixture. Otherwise there is the risk that, upon pyrolysis of the extruded activated carbon molded body, excessively large defects occur in the form of macroporosity, due to the green body binding agent being burnt out.
Preferably, when adding water for adjusting the viscosity of the material prepared in the mixing step, up to 20% by weight of the water can be added mixed with a portion of the cellulose ether. That can advantageously avoid excessive adsorption of the water in or on the activated carbon.
After the shaping or molding operation, preferably by extrusion, of the material obtained in the mixing step to provide a shaped or molded body, the body is preferably cut to the desired length and preferably subsequently dried. Drying is preferably subsequently effected using microwave heating or by a combination of microwave irradiation with conventional circulatory air drying at temperatures of between about 50° C. and about 80° C. It will be appreciated that it is also possible to use other drying procedures.
It has been found that it is advantageous if the moisture is removed permanently and quickly in order to avoid splitting of the extruded molded body during the drying operation. Preferably the molded body is dried until the water content is about 2.5/% by weight or less.
In the pyrollsing step of the production process the molded body produced in the drying step is firstly heated preferably to a temperature which is above the melting temperature of the preferably synthetic resin, to provide a pre-hardened green body. In that heating step the preferably synthetic resin which added in the mixing step melts and embeds the activated carbon particles into the resulting molten material.
In a preferred embodiment the pyrolysis operation is carried out in an inert gas atmosphere, the inert gas used preferably being nitrogen.
The resins used are preferably the above-mentioned resins with aromatic nuclei as well as synthetic resins. Phenolic resins, furan resins, epoxy resins, unsaturated polyester resins and mixtures thereof have proven to be highly suitable. Preferably novolak resins are employed.
A preferred embodiment of the production process provides that the resin is added in the mixing step in powder form. That has the extremely advantageous effect that the pores of the activated carbon particles are not closed or blocked by the resin as long as the resin has not melted. In order to implement adequate embedding of the activated carbon particles and thus fixing thereof in the carbon lattice structure produced in carbonisation of the preferably synthetic resin, the amount of resin should be selected to be sufficiently large, in relation to the amount of activated carbon used.
During the pyrolysis step the temperature is increased until carbonisation of the resin material employed takes place. During carbonisation of the resin material a porous solid carbon structure is formed, referred to as glass-like carbon. The activated carbon particles are then preferably fixed in that porous carbon structure. The pores of the activated carbon, which are possibly occupied with resin material, are accessible again for adsorption purposes due to the carbonisation procedure and the formation of a porous carbon structure.
Pyrolysis or carbonisation of the carbonisable resin is preferably implemented at a final temperature which is in a range of between about 350° C. and about 550° C., preferably at about 450° C. That temperature is preferably maintained for a period of between about 60 minutes and about 80 minutes.
The end of pyrolysis of the resin material can be controlled by monitoring the pyrolysis products which fume off. As soon as substantially no new decomposition products are produced, pyrolysis or carbonisation is terminated.
During the pyrolysis operation the additives which are optionally added such as for example wax, tenside or soap, cellulose ether or starch are also carbonised or decomposed.
A final temperature of 750° C. has proven to be particularly advantageous for forming the SiO2 structure from the silicone resin during the pyrolysis operation as that temperature makes it possible to achieve the highest levels of mechanical strength in the finished molded body.
It has been found that the sorption characteristics of the activated carbon molded body which can be produced by the process according to the invention can also be influenced by way of the properties of the activated carbon. Essential parameters in that respect include pore size, pore size distribution and the active surface area of the activated carbon used, as well as the particle size and particle size distribution of the activated carbon. All types of activated carbon can be used with this invention. Thus, both a microporous coconut carbon with more than 95% micropore proportion and a BET surface area of 1200 m2/g was used, and also a mesoporous charcoal with a mesopore proportion of more than 50% and a BET surface area of 2000 m2/g.
The former is preferably employed in cabin air filtration for odor elimination and the latter is preferably used in tank venting and solvent recovery. What is essential is that in both cases the pore structure is also retained in the finished molded body.
Preferably the synthetic resin material used is a novolak material in powder form, which is a partially cross-linked phenolformaidehyde resin and has a melting point of between 80° C. and 160° C., in particular between about 100° C. and 140° C.
The proportion of stabilisation fibers which are optionally added can be selected in dependence on the other components. In that respect the melting point of the added fibers should be above the maximum set pyrolysis temperature so that they do not melt during the pyrolysis procedure. If glass powder or glass frit material is additionally added to the mixture in the mixing step of the production process, additional cross-linking takes place between the glass fibers in the final product. Preferably, for mechanical stabilisation of the final product, about 10% by weight with respect to the weight of the activated carbon, glass fibers and glass frit material is added to the mixture produced in the mixing step of the process.
The present invention will be described in greater detail hereinafter by means of Examples and with reference to the accompanying Figures of drawings. It will be appreciated that the Examples and the drawings are provided exclusively for further explanation of the invention and are not deemed to constitute a limitation in respect thereof.
Reference is made to
Attention is now drawn to
The bursting force was measured on activated carbon molded bodies of a diameter of 30 mm, a length of 100 mm and a cell configuration of 200 cpsi (cells per square inch). In that respect the bursting force is denoted by the applied force at which the activated carbon molded body ruptured. The force is specified in Newtons. The bursting force was determined by means of a material tensile testing machine from Zwick, 89079 Ulm, Federal Republic of Germany, with a maximum advance movement of 25 mm/minute, with a foam rubber member of a thickness of 5 mm being disposed between the pressure plates of the machine and the test body in order to homogenise the pressure forces applied.
By virtue of the markedly higher proportion of resin the comparative filter enjoys a higher level of mechanical stability than the filter from the state of the art disclosed in DE 101 04 882 A1. It will be noted however that this is to the detriment of the adsorption efficiency at high levels of hydrocarbon concentration. Likewise a filter which was produced in accordance with that comparative composition has a very high residual loading.
The
Reference is now made to
It can be clearly seen that the passage structure of the 400 cell system has the same adsorption dynamics as the foam system with microporous activated carbon which is used as the comparison. As the structure however has only a third of the air resistance (this aspect is not shown) in comparison with the foam system, the molded body system according to the invention affords a considerable technical advantage over a foam impregnated with microporous activated carbon.
The foam system comprises four layers of a 10 mm thick cross-linked PU foam which was impregnated with activated carbon granules. That material can be obtained from helsa-automotive GmbH, 95479 Gefrees, Federal Republic of Germany, under the material designation 8126.
The activated carbon filters compared in
Embodiment 1
150 g of a fire clay was added to a mixture of 1500 g of a phenolic resin in powder form with 10009 of activated carbon powder. 200 g of a cellulose ether was added to the mixture as a green binder. Finally 1875 g of water was added to the material and the substances were mixed and kneaded in a kneader to form a homogeneous mass. 50 g of a polyglycol, 50 g of soap and 90 g of oleic acid were added as extrusion additives. 85 g of liquid methylphenylvinyl hydrogen polysiloxane was added to the mass as the silicone resin component.
That mass was extruded in a 200 cell system, dried by means of microwaves and pyrolysed in a pyrolysis furnace in a nitrogen atmosphere at 750° C.
An operation of determining working capacity was carried out on that filter, based on ASTM D 5228-92. The set n-butane concentration was 50% in air, and the volume through-put for loading was 0.1 l/min and for desorption 22 I/min. The system was loaded up to a break-through of 5000 ppm and then desorbed with the 22 l/min of air for 15 minutes. The result was a working capacity of 1.85 g. The residual loading on the filter was 0.7 g.
Embodiment 2
The mode of operation involved in production of the body is the same as in embodiment 1. The individual components are made up as follows: activated carbon 10509; phenolic resin 1115 g; fire clay 150 g; cellulose ether 200 g; water 18759; polyglycol 50 g; soap 50 g; oleic acid 90 g; and liquid silicone resin 125 g. Here 295 g of a phenylmethyl, polysiloxane was added as a new and additional component. The other component correspond to those specified in embodiment 1.
The same operation of determining working capacity was carried out on this filter as in embodiment 1. The result obtained was a working capacity of 29 and a residual loading of 0.55 g. The difference in terms of composition in relation to the state of the art is clearly indicated by Table 1. It will be seen that the amount of extrusion additives could be markedly reduced. The differing composition in the finished filter is illustrated by
The third embodiment described hereinafter now shows that a molded body which was produced in accordance with the novel composition of the invention can also be very satisfactorily used for gas cleaning purposes at low levels of concentration.
Embodiment 3
The composition involved is the same as in embodiment 1. In this case however a molded body with a cell configuration of 400 cpsi, a diameter of 25 mm and a length of 40 mm was produced. That filter was measured with the same afflux speed of 0.6 m/s as is usual in testing foam matrix systems for odor filters for cabin air filtration in a motor vehicle Measurement was implement with n-butane at a concentration of 80 ppm. The temperature was 23° C. and the relative humidity was 20%.
Embodiment 4
Embodiments 1 through 3 show activated carbon molded bodies involving a regularly tetragonal passage shape. The present Example demonstrates the advantages of an activated carbon molded body with a regularly hexagonal passage shape in comparison with an activated carbon molded body with a square passage shape.
For illustrative purposes, the passage shapes shown in
It will be clear from a comparison of
The theoretical results were checked on the basis of experimental measurement procedures. Three activated carbon molded bodies were measured, which each had an open area of 78% of the cross-sectional area of the overall activated carbon molded body:
Reference is now made to
The invention as described hereinbefore has been set forth solely by way of example and Illustration thereof and it will be appreciated that other modifications and alterations may be made therein without thereby departing from the spirit and scope of the invention.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10337584.8 | Aug 2003 | DE | national |
| 10346061.6 | Oct 2003 | DE | national |
