Patent Application
20230405570
The present invention relates to a catalyst unit and a platy catalyst element for purifying flue gas. Specifically, the present invention relates to a catalyst unit and a platy catalyst element for purifying flue gas, having a high rigidity even with a thin plate thickness, having a low SO2 oxidation activity, and having a high denitration activity.
Flue gas purification has been performed, by, in the presence of a denitration catalyst, decomposing nitrogen oxides in gas exhausted from furnace such as boilers in fire power plants or various factories. Various denitration catalyst structures are proposed in order to decompose nitrogen oxides in flue gas with high efficiency.
For instance, Patent document 1 discloses a flue gas purification catalyst structure comprising a plurality of catalyst elements stacked via a netted substance having many holes penetrating front and back thereof, the catalyst element is composed of a base material and catalyst components supported on the surface of the base material, the catalyst element is a flat plate-like catalyst element, the netted substance is one made by bending a rectangular or square flat plate-like netted substance alternately in an opposite direction at a predetermined interval, in a parallel direction to a pair of edges thereof, to form flat portions and stepped portions alternately, or one made by inflecting a rectangular or square flat plate-like netted substance into wavy plate form at a predetermined interval, in a parallel direction to a pair of edges thereof, to form ridge portions and thalweg portions alternately.
Patent document 2 discloses a plate like catalyst assembled structure comprising many platy catalysts stacked via spacers and placed within a unit frame, wherein the platy catalyst comprises ridge parts and flat parts repeated alternately at intervals, the ridge part has a strip-shaped protrusion and is worked as the spacer, and additional belt like protrusion is provided on a portion from the ridge part to the flat part at approximately right angle with the strip-shaped protrusion.
Patent document 3 discloses a catalyst structure comprising a multitude of platy catalyst elements with catalyst component supported on a surface thereof, wherein the platy catalyst element comprises ridge parts and flat parts repeated alternately in parallel, the ridge part is composed of at least two strip-shaped protrusions on front surface and at least two strip-shaped protrusions on back surface adjacently alternately, the number of the strip-shaped protrusions on the front surface is the same as that of the strip-shaped protrusions on the back surface, the platy catalyst elements are stacked and arranged so that the surfaces are alternately inverted, the ridge parts obstruct gas flow, and a tilt angle θ of the ridge part to a direction of the gas flow is more than 0° and not more than 90°.
Patent document 1: JP 2001-79422 A
Patent document 2: JP 2000-296333 A
Patent document 3: JP 2000-117120 A
An object of the present invention is to provide a catalyst unit and a platy catalyst element for purifying flue gas, having a high rigidity even with a thin plate thickness, having a low SO2 oxidation activity, and having a high denitration activity.
Researches in order to solve the problems have resulted in accomplishment of the present invention including the following embodiments.
The catalyst unit for purifying flue gas of the present invention has a high rigidity even with a thin plate thickness, has a low SO2 oxidation activity, and has a high denitration activity. Since the catalyst unit for purifying flue gas of the present invention has a higher denitration performance even in the same catalyst amount compared to the conventional catalyst unit, it is possible to significantly reduce the amount of catalyst usage to ensure the same denitration performance as the conventional catalyst unit.
The catalyst unit for purifying flue gas of the present invention can be preferably used particularly for treating gas containing a relatively large amount of dust discharged from a coal-fired boiler. The platy catalyst element of the present invention can be manufactured inexpensively and easily by press working or the like.
Embodiments of the present invention are specifically described by reference to the drawings. In addition, the scope of the present invention is not limited by the following embodiments.
The catalyst unit for purity tying flue gas of the present invention comprises a plurality of platy catalyst elements. The platy catalyst element comprises one flat plate portion and one wavy plate portion. The flat plate portion and the wavy plate portion are respectively quadrilateral in view image from normal direction relative to a main face thereof. It is preferable that the quadrangle projected by the flat plate portion and the quadrangle projected by the wavy plate portion have approximately the same shape and approximately the same largeness. A plate thickness t of the flat plate portion and the wavy plate portion is preferably 0.2 to 1 mm, more preferably 0.3 to 0.7 mm. The production cost is lower and the SO2 oxidation activity is lower, when the plate thickness is thinner.
The wavy plate portion is a part that is ridged in a wavelike fashion. As the wave shape, mentioned can be a shape corresponding to the fundamental wave such as a sine wave, a rectangular wave, a sawtooth wave, a trapezoidal wave, a triangular wave, and a water surface wave, or a shape corresponding to a synthetic wave (composite wave) composed of the fundamental waves. A shape corresponding to a sine wave or a synthetic wave composed of a triangular wave and a sine wave having the same wavelength and the same phase is preferred in the present invention. A number of the ridges and a number of the thalwegs are totally not less than 4, preferably not less than 6. Heights of all ridges are preferably the same. The height of the ridge, that is, a value (h) corresponding to twice the amplitude is preferably 2 mm to 20 mm. Distance between ridges, that is, a value (d) corresponding to the wavelength, is preferably 3 mm to 40 mm. Angle (β) of the maximum slope of the hillside is preferably 35° to 70°, more preferably 40° to 65°. Peak angle (α) is preferably 40° to 110°, more preferably 50° to 100°. When the angle α or the angle β is within the above range, the contact efficiency between the platy catalyst element and the gas is higher.
In the platy catalyst element, an edge of the flat plate portion and an edge of the wavy plate portion are connected. In the platy catalyst element 101 as shown in
As shown in
The platy catalyst element can be obtained, for example, by impregnating or coating a plate-shaped base material such as metal lath, inorganic fiber woven fabric, or inorganic fiber non-woven fabric with a catalyst component to carry the catalyst component on the plate-shaped base material, and then subjecting the product to press working or the like.
The catalyst component is not particularly limited as long as it has a denitration catalytic effect. For example, mentioned can be a titanium-based catalyst comprising oxide of titanium, oxide of molybdenum and/or tungsten, and oxide of vanadium; a zeolite-based catalyst comprising mainly an aluminosilicate such as zeolite on which metals such as Cu and Fe are supported; or a mixed catalyst of the titanium-based catalyst and the zeolite-based catalyst. Among these, the titanium-based catalyst is preferred.
As the titanium-based catalyst, mentioned can be Ti-V-W catalyst, Ti-V-Mo catalyst, Ti-V-W-Mo catalyst and the others. A ratio of V element to Ti element is preferably not more than 10% by weight, more preferably not more than 8% by weight in terms of a weight percentage of V2O5TiO2. A ratio of Mo element and/or W element to Ti element is preferably not more than 20% by weight in terms of a weight percentage of (MoO3+WO3)/TiO2, when molybdenum oxide and/or tungsten oxide are used.
In the preparation of the titanium-based catalyst, a titanium oxide powder or a titanium oxide precursor can be used as a raw material for the oxide of titanium. As the titanium oxide precursor, mentioned can be a titanium oxide slurry, a titanium oxide sol; titanium sulfate, titanium tetrachloride, titanate, titanium alkoxide, or the like. In the present invention, as a raw material for the oxide of titanium, one that forms anatase-type titanium oxide is preferably used.
As a raw material for the oxide of vanadium, used can be a vanadium compound such as vanadium pentoxide, ammonium metavanadate, vanadyl sulfate and the like.
Ammonium paratungstate, ammonium metatungstate, tungsten trioxide, tungsten chloride, or the like can be used as a raw material for the oxide of tungsten.
Ammonium molybdate, molybdenum trioxide or the like can be used as a raw material for the oxide of molybdenum.
The catalyst components used in the present invention can comprise cocatalyst or additive. As the cocatalyst or additive, mentioned can be oxide of P, oxide of S, oxide of Al (e.g., alumina), oxide of Si (e.g., glass fibers), oxide of Zr (e.g., zirconia), gypsum (eg, gypsum dihydrate, etc.), zeolite, and the like. These can be used in the form of powders, sols, slurries, fibers, or the like during catalyst preparation.
In a kneader, 10 kg of titanium dioxide, 1 kg of ammonium molybdate ((NH4)6Mo7O244H2O), 0.3 kg of ammonium metavanadate and 0.5 kg of oxalic acid were mixed and kneaded for 1 hour while adding water. Next, 2 kg of silica-alumina inorganic fibers were added to the kneaded product and kneaded for an additional 30 minutes to obtain a catalyst paste. Using a pair of mill rolls, the obtained catalyst paste was applied on surfaces and in meshes of a previously prepared strip-shaped metal lath made of stainless steel with a width of 500 mm to obtain a strip-shaped catalyst.
A wavy plate portion and a flat plate portion were formed in the strip-shaped catalyst using forming rolls. It was cut to a specified size with a cutting machine to obtain a platy catalyst element 101 having a plate thickness of 0.3 mm, an angle α of 60 and a height h of 6 mm wherein an edge of the flat plate portion and an edge of the wavy plate portion were connected and the edge of the wavy plate portion connected to the edge of the flat plate portion was a portion on a center line between a ridge line and a thalweg line of the wavy plate portion as shown in
The catalyst unit for purifying flue gas was set in a denitration reactor, and a simulant flue gas containing 350 ppm of NOx, 4% of O2, 12% of H2O and 350 ppm of NH3 was passed at a temperature of 350° C. and 6 m/sec to measure denitration ratio. Then, a simulant flue gas containing 2000 ppm of SOx, 4% of O2, and 12% of H2O was passed at a temperature of 380° C. and 6 m/sec to measure SO2 oxidation ratio. Table 1 shows relative values of denitration ratio and SO2 oxidation ratio in Example 1 with respect to denitration ratio and SO2 oxidation ratio in Comparative Example 1.
By the bending and cutting process, made from the strip-shaped catalyst obtained in Example 1 was a platy catalyst element comprising a flat plate portion and a wavy plate portion and having a plate thickness of 0.3 mm, an angle α of 60° and a height h of 6 mm wherein an edge of the flat late portion and an edge of the wavy plate portion were connected and the edge of the wavy plate portion connected to the edge of the flat plate portion was a portion on a ridge line or a thalweg line of the wavy plate portion. A plurality of platy catalyst elements 102 were alternately turned inside out and stacked as shown in
By the bending and cutting process, made from the strip-shaped catalyst obtained in Example 1 was a platy catalyst element comprising four flat plate portions and three protrusion line portions and having a plate thickness of 0.3 mm, an angle α of 60° and a height h of 6 mm. A plurality of platy catalyst elements 111 were alternately turned 180° and stacked as shown in
A platy catalyst element 111 as shown in
Table 1 shows relative values of denitration ratio and SO2 oxidation ratio in Comparative Example 2 with respect to the denitration ratio and SO2 oxidation ratio in Comparative Example 1.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2020-183972 | Nov 2020 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2021/040257 | 11/1/2021 | WO |
