SCR (Selective Catalytic Reduction) denitration catalyst production device

Abstract

The invention relates to the technical field of SCR (Selective Catalytic Reduction) denitration catalyst production, in particular to an SCR denitration catalyst production device which comprises a continuous calcining space, a substrate runs in the calcining space, a variable tray is designed on the substrate, and the variable tray can bear a honeycomb cuboid calcining object; the assembling frame is assembled on the base plate in a sliding mode, the assembling frame can move towards the honeycomb end of a calcination object, a plurality of flow guide pipes corresponding to honeycomb inner holes of the calcination object are rotationally designed on the assembling frame, a plurality of air holes are designed in the outer walls of the flow guide pipes, and the two ends of each flow guide pipe are open; the device is provided with a switching mechanism with a convection mode and a rotary spraying mode, high-temperature gas can accurately penetrate through honeycomb inner holes of a calcination object, the high-temperature gas can form convection in the honeycomb inner holes, the situation of uneven heating is reduced, high-temperature gas containing calcination atmosphere can be sprayed in a rotary mode, and the calcination quality of the honeycomb inner holes is improved.

Description

Technical Field

[0001] The invention relates to the technical field of denitration catalysts, and in particular to a SCR denitration catalyst production device. Background Art

[0002] SCR (Selective Catalytic Reduction) honeycomb denitrification catalyst is an important environmental protection technology product used for flue gas denitrification in coal-fired power plants. It reduces nitrogen oxides (NOx) in flue gas into nitrogen and water through catalytic action, thereby reducing air pollution. The main production steps of SCR denitrification honeycomb denitrification catalyst are: mixing the main raw materials of titanium dioxide, ammonium metatungstate, and ammonium metavanadate with auxiliary materials such as glass fiber and clay, mixing them evenly, and forming them through extrusion. The equipment makes honeycomb cuboids according to the required pore size, dry and calcine them, and then cut them into honeycomb catalyst monomers of a certain length and assemble them into modules.

[0003] Among them, the quality of the inner pores of the catalyst directly affects the efficiency of the contact between the flue gas and the catalyst. In the prior art, during the calcination heat treatment of the honeycomb deNOx catalyst, it is more important to control the temperature in the calcination chamber. However, since the honeycomb deNOx catalyst has more inner pores, there are differences in the heat treatment of the honeycomb pores of many deNOx catalysts, resulting in reduced molding quality of the inner wall of the honeycomb pores and reduced working performance of the catalyst. Summary of the invention

[0004] The present invention provides an SCR denitration catalyst production device, which can make high-temperature gas accurately pass through the honeycomb inner holes of the calcination object, so that the high-temperature gas can form convection in the honeycomb inner holes, reduce the uneven heating situation, and can also spin-spray the high-temperature gas containing the calcination atmosphere to improve the calcination quality of the honeycomb inner holes.

[0005] In order to achieve the above object, the present invention provides the following technical solutions:

[0006] An SCR denitration catalyst production device, comprising:

[0007] A continuous calcination space, in which a substrate is running, and a variable tray is designed on the substrate, and the variable tray can carry a calcination object of a honeycomb rectangular parallelepiped; an assembly frame slidably assembled on the substrate, and the assembly frame can be displaced toward the honeycomb end of the calcination object, and a plurality of guide tubes corresponding to the honeycomb inner holes of the calcination object are rotatably designed on the assembly frame, and the outer wall of the guide tube is designed with a plurality of air holes, and both ends of the guide tube are open; a switching mechanism with two modes of convection and rotary spraying, in which the air holes are closed in the convection mode, and the guide tube can output convective hot air to the honeycomb inner holes, and in the rotary spraying mode, the insertion end of the guide tube is closed, and the guide tube can be displaced into the honeycomb inner holes, and the guide tube can rotate and open the air holes to output hot air with a calcination atmosphere into the honeycomb inner holes; a pump source for inputting hot air or calcination atmosphere into the guide tube; an integrated driver for controlling the displacement of the assembly frame.

[0008] Optionally, the switching mechanism includes turbofan blades fixedly mounted inside the guide tube. When the pump source inputs hot air into the guide tube, the guide tube is driven to rotate through the turbofan blades. A friction unit for limiting the rotation of multiple guide tubes is installed on the assembly frame. The base plate is also designed with a latch unit for sealing the insertion end of the guide tube. An adaptive switching valve is installed on the inner wall of the air hole. In the convection mode, the air hole is closed, and in the rotary spray mode, the air hole is open.

[0009] Optionally, the latch unit includes a vertical plate slidably mounted on a base plate, a plurality of docking pins corresponding to the guide tubes are rotatably mounted on the outer wall of the vertical plate, and the insertion end of the guide tube can form a rotating seal with the docking pins after passing through the honeycomb inner hole of the calcination object.

[0010] Optionally, the switch valve includes two valve plates rotatably mounted on the inner wall of the air hole, and the flow of the air hole can be blocked when the ends of the two valve plates fit together. The inner wall of the air hole is installed with a baffle bar, and the baffle bar can limit the two valve plates from deflecting toward the inside of the downward guide tube. When the two valve plates collide with the baffle bar, the baffle bar limits the two valve plates to a fit state to close the air hole.

[0011] Optionally, the friction unit includes multiple rotating shafts rotatably mounted on an assembly frame, multiple cams are fixedly mounted on outer walls of the rotating shafts, and the cams can press and limit the outer wall of the guide tube after rotating by a preset angle. The multiple guide tubes are in a rectangular array, and the multiple cams are respectively located between rows and columns. The assembly frame is designed with a transmission component for controlling the synchronous rotation of the multiple rotating shafts.

[0012] Optionally, the transmission component includes an assembly seat fixedly mounted on the assembly frame, a worm is rotatably mounted on the assembly seat, a worm wheel is fixedly mounted on a portion of the outer wall of the rotating shaft that passes through the assembly frame, a plurality of worm wheels are meshed with the worm for transmission, and a high-temperature motor for controlling the rotation of the worm is installed in the assembly seat.

[0013] Optionally, the variable pallet includes a plurality of first bearing rollers and a plurality of second bearing rollers, and the plurality of first bearing rollers and the plurality of second bearing rollers are alternately distributed, and the bottoms of the plurality of first bearing rollers and the second bearing rollers are fixedly mounted on a frame, and a lifter is designed on the base plate, and the lifter can control the downward displacement of any one of the frames.

[0014] Optionally, two ribs are fixedly mounted on the top of each of the first load-bearing roller and the second load-bearing roller, and outer walls of opposite surfaces of the two ribs are provided with a plurality of notches, and the plurality of notches are equidistantly distributed along the axial direction of the ribs.

[0015] Optionally, the SCR deNOx catalyst production device further includes a plurality of calcining furnaces, the calcining space is disposed inside the calcining furnace, the plurality of calcining furnaces are arranged continuously, and the plurality of calcining spaces are sequentially associated, and the temperature inside the plurality of calcining furnaces can be freely set.

[0016] Optionally, the pump source is arranged outside the calcining furnace, and the output end of the pump source is connected to a plurality of collecting pipes, the collecting pipes are fixedly connected to packaging pipes, and the packaging pipes are rotatably connected to the input end of the guide pipe.

[0017] Compared with the prior art, the present invention has the following beneficial effects:

[0018] By designing two usage modes of the guide tube, it can be switched in the calcination space. Among them, the convection mode can be used to make the hot air or high-temperature gas flow so that it can accurately pass through the honeycomb inner holes of the calcination object, so that the high-temperature gas can form convection in the honeycomb inner holes, complete the heat treatment of the inner holes with high quality, and reduce the uneven heating situation.

[0019] When in the rotary spray mode, during the heat treatment of the calcination object, the calcination atmosphere can be added to the high-temperature gas, and then the calcination atmosphere can be released into the inner hole of the calcination object by utilizing the rotation of the guide tube, so that the calcination atmosphere quickly enters the inner hole of the honeycomb and flows in parallel, thereby better controlling the calcination process and improving the calcination quality of the calcination object. BRIEF DESCRIPTION OF THE DRAWINGS

[0020] Figure 1 It is a three-dimensional structural schematic diagram of the variable tray, the calcining object and the switching mechanism in the present invention;

[0021] Figure 2It is a schematic diagram of the structure of the flow guide pipe and the switching mechanism in the present invention;

[0022] Figure 3 For the present invention Figure 2 Enlarged view of point C in the middle;

[0023] Figure 4 It is a schematic diagram of the structure of the variable tray in the present invention;

[0024] Figure 5 is a cross-sectional view of the switching mechanism in the present invention;

[0025] Figure 6 It is a schematic diagram of the three-dimensional structure of the guide tube and the turbofan blade in the present invention;

[0026] Figure 7 It is a structural schematic diagram of the calcining furnace in the present invention.

[0027] In the figure: 1, base plate; 2, assembly seat; 3, assembly frame; 4, guide tube; 5, air hole; 6, turbofan blade; 7, packaging pipe; 8, collecting pipe; 9, cam; 11, first bearing roller; 12, second bearing roller; 13, rib; 14, frame; 15, calcining furnace; 17, worm gear; 18, worm; 20, vertical plate; 21, docking pin; 23, valve plate; 24, baffle. DETAILED DESCRIPTION

[0028] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0029] Example 1

[0030] See also Figures 1 to 7 , the embodiment of the present invention provides a technical solution:

[0031] An SCR denitration catalyst production device, comprising:

[0032] A continuous calcination space, in which a substrate 1 is operated, on which a variable tray is designed, which can carry a calcination object of a honeycomb-shaped rectangular parallelepiped; an assembly frame 3 slidably assembled on the substrate 1, the assembly frame 3 can be displaced toward the honeycomb end of the calcination object, and a plurality of guide tubes 4 corresponding to the honeycomb inner holes of the calcination object are rotatably designed on the assembly frame 3, and the outer wall of the guide tube 4 is designed with a plurality of air holes 5, and both ends of the guide tube 4 are open; a switching mechanism for convection and rotary spraying modes is provided, in which the air holes 5 are closed, and the guide tube 4 can output convective hot air to the honeycomb inner holes, and in the rotary spraying mode, the insertion end of the guide tube 4 is closed, and the guide tube 4 can be displaced into the honeycomb inner holes, and the guide tube 4 can rotate and open the air holes 5 to output hot air with a calcination atmosphere into the honeycomb inner holes; a pump source for inputting hot air or calcination atmosphere into the guide tube 4; an integrated driver for controlling the displacement of the assembly frame 3.

[0033] In the accompanying drawings, Figures 1 to 7 The total number of arrays of flow guide tubes is not fully shown.

[0034] In the prior art, when the honeycomb SCR denitration catalyst is subjected to calcination heat treatment, if the extrusion molding quality of the inner hole is defective, it will cause uneven heating of the inner hole, and excessive calcination will reduce the quality of the calcined object. In the present invention, by designing two usage modes of the guide tube 4, it can be switched in the calcination space, wherein the convection mode can be used to flow hot air or high-temperature gas so that it can accurately pass through the honeycomb inner hole of the calcination object, so that the high-temperature gas can form convection in the honeycomb inner hole, and the heat treatment of the inner hole is completed with high quality, reducing the uneven heating. Secondly, it can also be switched to the rotary spray mode. In the process of heat treatment of the calcination object, it is also necessary to add a calcination atmosphere to the high-temperature gas. For example, studies have shown that the iron oxide / LA catalyst calcined in an air atmosphere Compared with the catalyst calcined under argon atmosphere, it has better denitrification activity at low temperature, especially at 120-200°C, the denitrification efficiency can reach 80%-100%. Therefore, when the preset temperature is reached, it is necessary to add calcination atmosphere. The flowing atmosphere helps to avoid overheating in local areas and reduce catalyst structural damage or performance degradation caused by uneven temperature. The flow of calcination atmosphere can help achieve more uniform heating and ensure that all parts of the catalyst can reach consistent temperature conditions during the calcination process. The present invention, by designing a rotary spray mode, can add calcination atmosphere to the high-temperature gas, and at the same time utilize the rotation of the guide tube 4 to release the calcination atmosphere into the inner hole of the calcination object, so that the calcination atmosphere quickly enters the inner hole of the honeycomb and flows in parallel, thereby better controlling the calcination process and improving the calcination quality of the calcination object.

[0035] The substrate 1 can be moved in the calcining space, and the moving speed or the residence time can be adjusted to ensure the calcining time and the transfer of the calcined object.

[0036] Among the more preferred embodiments, the switching mechanism includes a turbofan blade 6 fixedly installed inside the guide tube 4. When the pump source inputs hot air into the guide tube 4, the turbofan blade 6 drives the guide tube 4 to rotate. A friction unit for limiting the rotation of multiple guide tubes 4 is installed on the assembly frame 3. The base plate 1 is also designed with a latch unit for sealing the insertion end of the guide tube 4. An adaptive switching valve is installed on the inner wall of the air hole 5. In the convection mode, the air hole 5 is closed, and in the rotary spray mode, the air hole 5 is open.

[0037] See also Figure 5 and Figure 6 In this embodiment, the pump source will input high-temperature gas into the guide tube 4, or the pump source can extract the high-temperature gas in the calcination space and output it to the inside of the guide tube 4. After the high-temperature gas enters the inside of the guide tube 4, due to the rotational assembly relationship between the guide tube 4 and the assembly frame 3, when the high-temperature airflow passes through the turbofan blades 6, the guide tube 4 can rotate, so that the high-temperature gas mixed with the calcination atmosphere can quickly fill the inner hole, thereby improving the calcination quality of the inner hole. In the convection mode, the insertion end of the guide tube 4 is open, and the pores 5 will be closed, so that the high-temperature gas input from one end of the guide tube 4 can be output from the insertion end, guiding and aligning the high-temperature gas, so that the high-temperature gas can enter the honeycomb inner hole of the calcination object.

[0038] Example 2

[0039] Based on Example 1, this Example 2 provides a specific preferred embodiment, specifically:

[0040] The latch unit comprises a vertical plate 20 slidably mounted on the base plate 1, and a plurality of docking pins 21 corresponding to the guide tube 4 are rotatably mounted on the outer wall of the vertical plate 20. The insertion end of the guide tube 4 can form a rotation seal with the docking pins 21 after passing through the honeycomb inner hole of the calcined object. Figure 1 In this embodiment, by designing the cooperation between the docking pin 21 and the insertion end of the guide tube 4, the end of the guide tube 4 can be closed. At this time, the pressure of the high-temperature gas input into the guide tube 4 will increase, and the high-temperature gas will be ejected outward through the pores 5, so that the calcination atmosphere can directly enter the honeycomb inner hole of the calcination object, thereby improving the calcination quality of the honeycomb inner hole of the calcination object.

[0041] In a preferred embodiment, the switch valve includes two valve plates 23 rotatably mounted on the inner wall of the air hole 5. When the ends of the two valve plates 23 are fitted together, the flow of the air hole 5 can be blocked. A baffle 24 is installed on the inner wall of the air hole 5. The baffle 24 can limit the two valve plates 23 from deflecting downward into the guide tube 4. When the two valve plates 23 collide with the baffle 24, the baffle 24 limits the two valve plates 23 to fit together to close the air hole 5. Please refer to Figure 3 In this embodiment, when both ends of the flow guide tube 4 are open, high-temperature gas is input into one end and the gas is output from the other end. The opening of the flow guide tube 4 is much larger than the opening of the pore 5, so that the high-temperature gas can be output more smoothly to the insertion end of the flow guide tube 4. According to the Bernoulli principle, the pressure in the area where the fluid flows quickly will decrease, so that the air pressure in the calcination space will cause the two valve plates 23 to deflect toward the inside of the flow guide tube 4, and then keep in contact under the restriction of the baffle 24 to close the pore 5, so as to achieve the output of high-temperature gas. When switching to the rotary spray mode, the insertion end of the flow guide tube 4 is blocked. At this time, the gas pressure inside the flow guide tube 4 will increase, and the gas pressure in the calcination space is lower than the gas pressure inside the flow guide tube 4, so that the two valve plates 23 will deflect outward, release the closure of the pore 5, and allow the airflow inside the flow guide tube 4 to be output outward.

[0042] Example 3

[0043] Based on Example 1 and Example 2, this Example 3 provides a specific preferred embodiment, specifically:

[0044] The friction unit includes a plurality of rotating shafts rotatably mounted on an assembly frame 3, and a plurality of cams 9 are fixedly mounted on the outer walls of the rotating shafts. After the cams 9 rotate by a preset angle, they can press and limit the outer wall of the guide tube 4. The plurality of guide tubes 4 are in a rectangular array, and the plurality of cams 9 are respectively located between the rows and columns. A transmission component for controlling the synchronous rotation of the plurality of rotating shafts is designed on the assembly frame 3. In a convection state, the cams 9 press the outer wall of the guide tube 4, thereby locking the guide tube 4 by friction. When the rotary spray mode is switched, the cams 9 release the lock on the guide tube 4, so that the guide tube 4 can rotate with the cooperation of the turbofan blades 6, thereby effectively inputting the calcining atmosphere into the honeycomb inner hole. The continuous input of the calcining atmosphere can increase the pressure of the honeycomb inner hole and cause the calcining atmosphere to flow. Alternatively, after the calcining atmosphere is input into the honeycomb inner hole, the guide tube 4 can be withdrawn, and the calcining atmosphere can flow by using the convection mode to improve the calcining quality of the honeycomb inner hole.

[0045] Furthermore, the transmission component includes an assembly seat 2 fixedly mounted on the assembly frame 3, a worm 18 is rotatably mounted on the assembly seat 2, a worm wheel 17 is fixedly mounted on the outer wall of the rotating shaft passing through the assembly frame 3, a plurality of worm wheels 17 are meshed with the worm 18 for transmission, and a high-temperature motor for controlling the rotation of the worm 18 is installed in the assembly seat 2, see Figure 2 By utilizing the cooperation of the worm 18 and the multiple worm wheels 17, the multiple cams 9 can be controlled synchronously to be unlocked or locked synchronously.

[0046] Example 4

[0047] On the basis of Embodiments 1 to 3, this Embodiment 4 provides a specific preferred embodiment, specifically:

[0048] The variable tray includes a plurality of first bearing rollers 11 and a plurality of second bearing rollers 12, which are alternately distributed. A frame 14 is fixedly installed at the bottom of the plurality of first bearing rollers 11 and the second bearing rollers 12. A lifter is designed on the base plate 1, and the lifter can control any frame 14 to move downward. Please refer to Figure 1 and Figure 4 In this embodiment, the first load-bearing roller 11 and the second load-bearing roller 12 constitute the load-bearing chassis of the variable tray. When one of the frames 14 is displaced downward, the downward displacement of the first load-bearing roller 11 or the second load-bearing roller 12 can be controlled, so as to release part of the bonding part of the calcining object, so that the part can also contact with the high-temperature gas or calcining atmosphere, and does not affect the stability of the variable tray. The lifter can operate at high temperature, and only needs to control the downward movement and resetting of the frame 14. The calcination quality of the outer surface will affect the thermal stability and durability of the calcination object. Therefore, it is necessary to improve whether the outer surface has different calcination heat treatment to avoid poor calcination quality of the bearing bonding part and reduce bad points.

[0049] Example 5

[0050] On the basis of Embodiments 1 to 4, this Embodiment 5 provides a specific preferred embodiment, specifically:

[0051] Two ribs 13 are fixedly installed on the top of the first bearing roller 11 and the second bearing roller 12. The outer walls of the opposite sides of the two ribs 13 are provided with a plurality of notches, and the plurality of notches are equidistantly distributed along the axial direction of the ribs 13. The design of the ribs 13 can improve the bearing stability of the calcination object, and when the first bearing roller 11 or the second bearing roller 12 moves downward, the position of the notch will also change, thereby improving the calcination quality of the side of the calcination object.

[0052] Furthermore, the SCR denitration catalyst production device also includes a plurality of calcining furnaces 15, a calcining space is arranged inside the calcining furnace 15, the plurality of calcining furnaces 15 are arranged continuously, and the plurality of calcining spaces are sequentially associated, and the temperature inside the plurality of calcining furnaces 15 can be freely set.

[0053] Furthermore, the pump source is arranged outside the calcining furnace 15, and the output end of the pump source is connected to a plurality of collecting pipes 8, and the collecting pipes 8 are fixedly connected to the packaging pipes 7, and the packaging pipes 7 are rotatably connected to the input end of the guide pipe 4, see Figure 2 The pump source can synchronously input high-temperature gas to multiple collecting pipes 8, and the multiple collecting pipes 8 transfer the high-temperature gas to the guide pipe 4 by using the intermediary relationship of the packaging pipe 7.

[0054] By utilizing the above-mentioned structures, the high-temperature gas can accurately pass through the honeycomb inner holes of the calcination object, so that the high-temperature gas can form convection in the honeycomb inner holes, reducing the uneven heating situation. The high-temperature gas containing the calcination atmosphere can also be rotary sprayed to improve the calcination quality of the honeycomb inner holes.

[0055] The standard parts used in this embodiment can be purchased directly from the market, and the non-standard structural components recorded in the specification and the drawings can also be directly processed according to the existing technical common sense without any doubt. At the same time, the connection method of each component adopts the mature conventional means in the prior art, and the machinery, parts and equipment all adopt the conventional models in the prior art, so no specific description will be given here.

[0056] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A SCR denitration catalyst production device, characterized in that: include: A continuous calcining space, in which a substrate (1) is running, and a variable tray is designed on the substrate (1), and the variable tray can carry a calcining object in the shape of a honeycomb cuboid; An assembly frame (3) slidably assembled on a substrate (1), the assembly frame (3) being displaceable toward a honeycomb end of a calcining object, the assembly frame (3) being rotatably provided with a plurality of flow guide tubes (4) corresponding to inner holes of the honeycomb of the calcining object, the outer wall of the flow guide tube (4) being provided with a plurality of air holes (5), and both ends of the flow guide tube (4) being open; The invention has a switching mechanism for two modes: convection mode and rotary spray mode. In the convection mode, the air hole (5) is closed, and the guide tube (4) can output convection hot air to the inner hole of the honeycomb. In the rotary spray mode, the insertion end of the guide tube (4) is closed, and the guide tube (4) can be displaced into the inner hole of the honeycomb. The guide tube (4) can rotate and open the air hole (5) to output hot air with a calcining atmosphere to the inner hole of the honeycomb. A pump source for inputting hot air or calcining atmosphere into the flow guide tube (4); An integrated drive controls the displacement of the assembly frame (3).

2. The SCR denitration catalyst production device according to claim 1, characterized in that: The switching mechanism comprises a turbofan blade (6) fixedly mounted inside the guide tube (4); when the pump source inputs hot air into the guide tube (4), the turbofan blade (6) drives the guide tube (4) to rotate; a friction unit for limiting the rotation of the plurality of guide tubes (4) is mounted on the assembly frame (3); a latch unit for blocking the insertion end of the guide tube (4) is also designed on the base plate (1); an adaptive switch valve is mounted on the inner wall of the air hole (5); in the convection mode, the air hole (5) is closed; in the rotary spray mode, the air hole (5) is open.

3. The SCR denitration catalyst production device according to claim 2, characterized in that: The latch unit comprises a vertical plate (20) slidably mounted on a base plate (1); a plurality of docking pins (21) corresponding to the flow guide tube (4) are rotatably mounted on the outer wall of the vertical plate (20); and the insertion end of the flow guide tube (4) can form a rotational seal with the docking pins (21) after passing through the honeycomb inner hole of the calcining object.

4. The SCR denitration catalyst production device according to claim 3, characterized in that: The switch valve comprises two valve plates (23) rotatably mounted on the inner wall of the air hole (5); when the ends of the two valve plates (23) are in contact with each other, the flow of the air hole (5) can be blocked; a baffle (24) is mounted on the inner wall of the air hole (5); the baffle (24) can limit the two valve plates (23) from deflecting toward the inside of the downward flow guide tube (4); when the two valve plates (23) collide with the baffle (24), the baffle (24) limits the two valve plates (23) to a contacting state to close the air hole (5).

5. The SCR denitration catalyst production device according to claim 3, characterized in that: The friction unit comprises a plurality of rotating shafts rotatably mounted on an assembly frame (3); a plurality of cams (9) are fixedly mounted on the outer walls of the rotating shafts; the cams (9) are capable of pressing and limiting the outer walls of the guide tubes (4) after rotating at a preset angle; the plurality of guide tubes (4) are arranged in a rectangular array; the plurality of cams (9) are respectively located between rows and columns; and a transmission component for controlling the synchronous rotation of the plurality of rotating shafts is designed on the assembly frame (3).

6. The SCR denitration catalyst production device according to claim 5, characterized in that: The transmission component comprises an assembly seat (2) fixedly mounted on an assembly frame (3), a worm (18) being rotatably mounted on the assembly seat (2), a worm wheel (17) being fixedly mounted on a portion of the outer wall of the rotating shaft that passes through the assembly frame (3), a plurality of worm wheels (17) meshingly transmitting with the worm (18), and a high-temperature motor for controlling the rotation of the worm (18) being mounted in the assembly seat (2).

7. The SCR denitration catalyst production device according to claim 1, characterized in that: The variable pallet comprises a plurality of first bearing rollers (11) and a plurality of second bearing rollers (12), wherein the plurality of first bearing rollers (11) and the second bearing rollers (12) are alternately distributed, and the bottoms of the plurality of first bearing rollers (11) and the second bearing rollers (12) are fixedly mounted on a frame (14), and a lifter is designed on the base plate (1), and the lifter can control any frame (14) to move downward.

8. The SCR denitration catalyst production device according to claim 7, characterized in that: Two ribs (13) are fixedly mounted on the top of the first load-bearing roller (11) and the second load-bearing roller (12), and the outer walls of the opposite surfaces of the two ribs (13) are provided with a plurality of notches, which are equidistantly distributed along the axial direction of the ribs (13).

9. The SCR denitration catalyst production device according to any one of claims 1 to 8, characterized in that: The SCR denitration catalyst production device also includes a plurality of calcining furnaces (15), wherein the calcining space is arranged inside the calcining furnace (15), the plurality of calcining furnaces (15) are arranged in series, and the plurality of calcining spaces are sequentially associated, and the temperature inside the plurality of calcining furnaces (15) can be freely set.

10. The SCR denitration catalyst production device according to claim 9, characterized in that: The pump source is arranged outside the calcining furnace (15); the output end of the pump source is connected to a plurality of collecting pipes (8); the collecting pipes (8) are fixedly connected to a packaging pipe (7); and the packaging pipe (7) is rotatably connected to the input end of the guide pipe (4).

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