The present invention relates to a denitration catalyst unit. More specifically, the present invention relates to a denitration catalyst unit that can achieve a high denitration rate with low pressure loss and contribute to a reduction in initial running costs.
Background technology
[0002]
In the presence of denitrification catalysts, nitrogen oxides in the gas emitted from boiler furnaces and waste incinerator furnaces in thermal power plants and various factories are decomposed to purify the exhaust gas. Various denitration catalyst structures or denitration catalyst units have been proposed to decompose nitrogen oxides in exhaust gas with high efficiency.
[0003]
For example, Patent Document 1 describes a plurality of plate-like catalyst elements that support a catalyst component having catalytic activity on the surface and are configured by alternately repeating ridges and flat portions at intervals. A catalyst structure comprising a stack of catalyst structures, characterized in that the ridges of each catalyst element are arranged in a direction that partially dams the gas flow continuously or stepwise in the direction of gas flow. revealing the body
[0004]
Patent Document 2 discloses a plate-shaped catalyst element having strip-shaped projections and flat portions alternately repeated in parallel, on which a catalyst component is supported, and arranged such that the ridges interrupt gas flow. a catalyst structure in which a plurality of sheets are laminated as above, wherein the ridges are alternately adjacent to the front and back sides of the plate-like catalyst element, and each of the ridges has the same number of two or more belt-like projections, and the ridges are The plate-like catalyst elements arranged so that 0<θ≦90° (where θ is the inclination angle of the ridges with respect to the gas flow direction) with respect to the gas flow direction were alternately turned upside down and laminated in order. Disclosed is a catalyst structure characterized by:
[0005]
Patent Document 3 discloses, as Example 14, six wavy filaments each having a size of 150 mm x 250 mm and a height of 2 mm obliquely (approximately 30°) to the long side at intervals of 30 mm on the short side. 46 catalyst substrates were laminated on a catalyst frame to prepare a catalyst carrier unit of 150 mm × 150 mm × 250 mm, and this unit was immersed in catalyst slurry, dried and calcined to prepare a unit-shaped catalyst. is disclosed.
prior art documents
patent literature
[0006]
Patent Document 1: WO96/014920A1
Patent document 2: JP-A-2000-117120
Patent Document 3: JP-A-2002-361092
SUMMARY OF THE INVENTION
Problems to be Solved by the Invention
[0007]
In the prior art catalyst structure, as shown in FIG. 12, when the plate-shaped catalyst element flattens due to heat during operation, the edge portion of the plate-shaped catalyst element on the gas inflow side bends, The width d of the flow path may be narrowed or uneven, resulting in an increase in pressure loss and a decrease in the denitrification rate.
[0008]
The object of the present invention is to provide a denitrification catalyst unit that can achieve a high denitrification rate with low pressure loss and contribute to the reduction of initial running costs such as fan power.
Means to solve problems
[0009]
As a result of studying to solve the above problems, the present invention including the following forms was completed.
[0010]
[1] A plate-shaped catalyst element having an edge on the gas inflow side, an edge on the gas outflow side, and edges on both sides is separated into an edge on the gas inflow side and edges on both sides. A denitrification catalyst unit formed by stacking a plurality of each with
Each plate-shaped catalyst element has a plurality of flat plate-shaped flat portions and plate-shaped uneven portions having ridges on the upper and lower surfaces, respectively, alternately, and each ridge is plate-shaped. are arranged obliquely and parallel to each other at an angle θ of 50° or more and 85° or less with respect to the extending direction of the edge on the gas inflow side of the catalyst element,
The ridge lines of the ridges on the upper surface of one plate-shaped catalyst element and the ridge lines of the ridges on the lower surface of the adjacent plate-shaped catalyst element are arranged so as to intersect and touch each other,
At least one of the intersecting points is in a range x of more than 0 mm and less than 25 mm toward the inside from the edge on the gas inflow side of the plate-shaped catalyst element,
Denitrification catalyst unit.
[0011]
[2] The denitrification catalyst unit according to [1], wherein each individual plate-like catalyst element comprises a plate-like substrate and a catalyst component carried thereon.
[0012]
[3] A plate-like catalyst element having an edge on the gas inflow side, an edge on the gas outflow side, and edges on both sides,
The plate-shaped catalyst element has a plurality of flat plate-shaped flat portions and plate-shaped uneven portions having parallel ridges on the upper and lower surfaces, respectively, alternately, and each ridge has a plate-like shape. are arranged obliquely and parallel to each other at an angle θ of 50° or more and 85° or less with respect to the extending direction of the edge on the gas inflow side of the catalyst element,
A plurality of plate-like catalyst elements are arranged so that the edges on the gas inflow side and the edges on both sides are aligned, and the ridgeline of the ridges on the upper surface of one plate-like catalyst element is adjacent to the other one. ridges on the lower surface of the plate-like catalyst element of the plate-like catalyst element, and when stacked, at least one of the points of intersection is on the gas inflow side of the plate-like catalyst element. lies in a range x of more than 0 mm and less than 25 mm inward from the existing edge,
Plate-shaped catalyst element.
[0013]
[4] The plate-like catalyst element according to [3], which comprises a plate-like substrate and a catalyst component carried thereon.
The invention's effect
[0014]
According to the present invention, a high denitrification rate can be achieved with low pressure loss, contributing to a reduction in initial running costs. INDUSTRIAL APPLICABILITY The present invention is suitable for removing nitrogen oxides (NOx) contained in the exhaust gas of gas-fired plants.
Brief description of the drawing
[0015]
1 is a three-view (front, top, right side) view showing a plate-like catalyst element A used in the present invention; FIG.
2 is a three-view (front, top, right side) view showing a plate-like catalyst element B used in the present invention. FIG.
3 is a front view showing an example of a denitration catalyst unit of the present invention; FIG.
4 is a perspective view showing an example of a denitration catalyst unit of the present invention; FIG.
FIG. 5 is a view (top see-through) showing the arrangement of points at which ridge lines of ridges on the upper surface of plate-like catalyst element A and ridge lines of ridges on the lower surface of plate-like catalyst element B intersect;
6 is a view (top see-through) showing the arrangement of points at which ridgelines of ridges on the lower surface of plate-like catalyst element A and ridgelines of ridges on the upper surface of plate-like catalyst element B intersect. FIG.
7 is a three-view (front, top, right side) view showing a plate-like catalyst element C used in the present invention. FIG.
8 is a front view showing an example of the denitration catalyst unit of the present invention; FIG.
9 is a view (top see-through) showing the arrangement of points at which the ridge lines of the ridges on the upper surface of the plate-like catalyst element A and the ridge lines of the ridges on the lower surface of the plate-like catalyst element C intersect. FIG.
10 is a view (top see-through) showing the arrangement of points at which the ridge lines of the ridges on the lower surface of the plate-like catalyst element A and the ridge lines of the ridges on the upper surface of the plate-like catalyst element C intersect. FIG.
11 is a diagram showing an example of the state of the edges on the gas inflow side in the denitration catalyst unit of the present invention. FIG.
12 is a diagram showing an example of the state of an edge on the gas inflow side of a conventional denitration catalyst unit. FIG.
MODE FOR CARRYING OUT THE INVENTION
[0016]
An embodiment of the present invention will be specifically described based on the drawings. In addition, the scope of the present invention is not limited by the following embodiments.
[0017]
The denitration catalyst unit of the present invention consists of a plurality of plate-shaped catalyst elements.
[0018]
Each plate-like catalyst element preferably contains a plate-like substrate and a catalyst component supported on its surface. A plate-like catalyst element can be obtained by impregnating or coating a plate-like base material such as metal lath, inorganic fiber woven fabric, or non-woven fabric with a catalyst component, followed by press working or the like.
[0019]
The catalyst component is not particularly limited as long as it has a denitration catalytic effect. For example, those containing oxides of titanium, oxides of molybdenum and/or tungsten, and oxides of vanadium (titanium-based catalysts); Mainly containing (zeolite-based catalyst; a mixture of a titanium-based catalyst and a zeolite-based catalyst can be mentioned. Of these, the titanium-based catalyst is preferred.
[0020]
Examples of titanium-based catalysts include Ti--V--W catalysts, Ti--V--Mo catalysts, and Ti--V---Mo catalysts.
The ratio of the V element to the Ti element is preferably 2% by weight or less, more preferably 1% by weight or less as a weight percentage of V2O5/TiO2. The ratio of Mo element and/or W element to Ti element is preferably 10% by weight or less, more preferably 10% by weight or less, as a weight percentage of (MoO3+WO3)/TiO2 when molybdenum oxide and tungsten oxide are used in combination. is 5% by weight or less.
[0021]
In the preparation of a titanium-based catalyst, titanium oxide powder or a titanium oxide precursor can be used as a raw material for titanium oxide. Titanium oxide precursors include titanium oxide slurry, titanium oxide sol; titanium sulfate, titanium tetrachloride, titanate, titanium alkoxide, and the like. In the present invention, as a raw material for titanium oxide, one that forms anatase-type titanium oxide is preferably used.
As raw materials for vanadium oxides, vanadium compounds such as vanadium pentoxide, ammonium metavanadate, and vanadyl sulfate can be used.
Ammonium paratungstate, ammonium metatungstate, tungsten trioxide, tungsten chloride, etc. can be used as raw materials for tungsten oxide.
Ammonium molybdate, molybdenum trioxide, etc. can be used as raw materials for molybdenum oxide.
[0022]
The catalyst components used in the present invention include P oxides, S oxides, Al oxides (e.g., alumina), Si oxides (e.g., glass fibers), Zr Oxides (eg, zirconia), gypsum (eg, gypsum dihydrate, etc.), zeolites, and the like may be included. These can be used in the form of powders, sols, slurries, fibers, etc. during catalyst preparation.
[0023]
The denitration catalyst unit of the present invention preferably has a plurality of plate-like catalyst elements housed in a frame 5 as shown in FIG.
[0024]
Each plate-shaped catalyst element has a plate-like shape with an edge on the gas inflow side, an edge on the gas outflow side, and edges on both sides. The individual plate-shaped catalytic elements are preferably square or rectangular in overall shape. In the denitrification catalyst unit of the present invention, the plate-like catalyst elements are stacked with the edges on the gas inflow side and the edges on both sides aligned.
[0025]
Each plate-shaped catalyst element has a plurality of flat portions 1 and uneven portions 2 alternately. The flat portion 1 has a flat plate shape. The concave-convex portion 2 has a plate-like shape having parallel ridges 3 and 3' on its upper and lower surfaces, respectively. The ridges 3, 3' may be curved, but are preferably substantially straight as shown in Fig. 1 and the like. The height h of the ridges 3, 3' and the width w of the ridges 3, 3' can be set appropriately. The width of the uneven portion 2 is 2w. The width w 2 of the ridge section at the edge on the gas inflow side or the gas outflow side is w/(sin(90°−θ)). It is preferable that the right back of each of the ridges 3', 3 has grooves 4, 4' corresponding to the shape of the ridges. It is preferable that each uneven portion has a Z-shaped or S-shaped cross section formed by the ridges on the upper surface and the ridges on the lower surface. In the figure, thin lines indicate the ridge lines of the ridges, and thick lines indicate the trough lines of the grooves. Furthermore, the larger the ratio h/w of the height h to the width w, the higher the denitrification rate, and the smaller the ratio, the lower the pressure loss. Also, the plate thickness t of the flat portion and the uneven portion is not particularly limited, but is preferably 0.1 to 0.5 mm.
[0026]
　Each ridge is located on the gas inflow side of the plate-shaped catalyst element.
More about this source textSource text required for additional translation information
Send feedback
Side panels
History
Saved
Contributeare arranged obliquely and parallel to each other at an angle .theta. The angle θ has a lower limit of 50°, preferably 55°, more preferably 65°, still more preferably 70°, and an upper limit of 85°, preferably 83°, more preferably 80°. When the angle θ is small, the effect of increasing the denitrification rate tends to be high. When the angle θ is large, the effect of reducing pressure loss tends to be high. The parallel ridges on the same plane are preferably arranged at equal intervals. The distance p between the ridge lines of the parallel ridges on the same plane can be set as appropriate. The width p 0 is p-2w or w 1sin (90°-θ). The plate-like catalyst element of the present invention tends to have a lower pressure loss as the angle θ increases, and a higher denitration rate as the width p 0 decreases.
[0027]
In the denitrification catalyst unit of the present invention, the ridge line of the ridge 3 on the upper surface of one plate-like catalyst element and the ridge line of the ridge 3' on the lower surface of the other adjacent plate-like catalyst element intersect. placed in contact with each other. The minor angle θ 1 formed by the two ridges at the crossing point is preferably 10° or more and 80° or less, more preferably 20° or more and 70° or less, still more preferably 20° or more and 65° or less. By arranging the ridge lines of the ridges so as to intersect and contact each other, the average distance between the upper surface of the flat portion of the plate-shaped catalyst element and the lower surface of the flat portion of the adjacent plate-shaped catalyst element can be reduced to , 3′ constrains the lower limit.
[0028]
In the denitrification catalyst unit of the present invention, at least one of the intersection points 6, 6' is more than 0 mm and 25 mm from the edge of the plate-shaped catalyst element on the gas inflow side toward the inner side (gas outflow side). less than, preferably 4 mm or more and 20 mm or less, more preferably 7 mm or more and 16 mm or less.
[0029]
An example of a mode in which the intersecting points 6, 6' are located within this range x is shown below.
The plate-like catalyst element B shown in FIG. 2 is the plate-like catalyst element A shown in FIG. When turned over in this way, the cross section of the uneven portion at the edge on the front (gas inflow) side of the plate-shaped catalyst element A forms a Z-shaped waveform, The cross-section of the undulations at the existing edge forms an inverted Z-shaped corrugation. As shown in FIGS. 3, 5 and 6, a point 6 (FIG. 5) where the ridgeline of the ridges on the upper surface of the plate-like catalyst element A and the ridgeline of the ridges on the lower surface of the plate-like catalyst element B intersect and contact each other. A point 6' (FIG. 6) where the ridgeline of the ridges on the lower surface of the plate-like catalyst element A and the ridgeline of the ridges on the upper surface of the plate-like catalyst element B intersect and touch is almost from the edge on the gas inflow side. They are alternately shifted left and right at the same distance. When one plate-like element is used by reversing front and back like plate-like catalyst element A and plate-like catalyst element B, in order to have at least one crossing point in range x, W3 and W4 Preferably the difference is 2x/(tan θ).
[0030]
A plate-like catalyst element C shown in FIG. 6 is obtained by turning over the plate-like catalyst element A shown in FIG. When turned over in this way, the cross section of the uneven portion on the edge on the front (gas inflow) side of the plate-shaped catalyst element A and the cross section of the uneven portion on the edge on the front (gas inflow) side of the plate-shaped catalyst element B are Together, it forms a Z-shaped waveform. As shown in FIGS. 8, 9 and 10, a point 6 where the ridgeline of the ridge on the upper surface of the plate-like catalyst element A and the ridgeline of the ridge on the lower surface of the plate-like catalyst element C intersect and contact with each other; A point 6' where the ridgeline of the ridge on the lower surface of the catalyst element A and the ridgeline of the ridge on the upper surface of the plate-shaped catalyst element C intersect and touch each other alternately shifts forward and backward at positions approximately the same distance from the edges on both sides. are placed. When one plate-like element is reversed left-to-right, such as the plate-like catalyst element A and the plate-like catalyst element C, the ridges of the ridges are formed into ridges so that at least one intersecting point exists in the range x. along the midpoint of the width of , the difference between W 3 and W 4 is preferably 2x/(tan θ)−1.5W 2 .
[0031]
The intersection points 6, 6' are located in the range x, so that even when the plate-shaped catalyst element is flattened and bent, the upper surface of the flat portion of the plate-shaped catalyst element at the edge on the gas inflow side. It is possible to prevent the distance d between the lower surfaces of the flat portions of the adjacent plate-shaped catalyst elements from becoming uneven (FIG. 11). As a result, the denitration catalyst unit of the present invention can achieve a high denitration rate with low pressure loss, which can contribute to a reduction in initial running costs such as fan power.
[0032]
Examples are shown below to specifically demonstrate the effects of the denitration catalyst unit of the present invention.
[0033]
Comparative example
The denitration catalyst unit was assembled so that the points 6 and 6' where the plate-like catalyst elements with an angle θ of 75° and p 0 of 30 mm were overlapped and intersected were 30 mm from the edge on the gas inflow side. Simulated combustion exhaust gas was flowed through this, and pressure loss and denitrification rate were measured.
[0034]
Example
The points 6 and 6' where the plate-shaped catalyst elements A with an angle θ of 75° and p 0 of 30 mm are overlapped and intersected as shown in FIGS. A denitrification catalyst unit was assembled as follows. Simulated combustion exhaust gas was flowed through this, and pressure loss and denitrification rate were measured.
[0035]
The pressure loss of the denitration catalyst unit of the example was about 30% lower than the pressure loss of the denitration catalyst unit of the comparative example. The denitration rate of the denitration catalyst unit of the example was higher than that of the denitration catalyst unit of the comparative example.