CN110694471A - But many storehouses off-line denitration reaction system - Google Patents
But many storehouses off-line denitration reaction system Download PDFInfo
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- CN110694471A CN110694471A CN201911118031.6A CN201911118031A CN110694471A CN 110694471 A CN110694471 A CN 110694471A CN 201911118031 A CN201911118031 A CN 201911118031A CN 110694471 A CN110694471 A CN 110694471A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8621—Removing nitrogen compounds
- B01D53/8625—Nitrogen oxides
- B01D53/8631—Processes characterised by a specific device
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8696—Controlling the catalytic process
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
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Abstract
The invention provides a multi-bin offline denitration reaction system, which relates to the technical field of denitration equipment and comprises an inlet main flue, an outlet main flue and a plurality of denitration reactors, wherein the inlet main flue is respectively connected with air inlets of the denitration reactors, the outlet main flue is respectively connected with air outlets of the denitration reactors, each air inlet is provided with an inlet baffle door for opening or closing the air inlet, and each air outlet is provided with an outlet baffle door for opening or closing the air outlet. Compared with the prior art, the denitration method can avoid resource waste caused by simultaneous opening of a plurality of denitration reactors, and ensures the stability of denitration efficiency. Meanwhile, the reactor can be miniaturized under the condition of not influencing the total amount of flue gas treatment, the difficulty of site construction in the aspects of hoisting and manufacturing is greatly reduced, and the assembly is convenient.
Description
Technical Field
The invention relates to the technical field of denitration equipment, in particular to a multi-bin offline denitration reaction system.
Background
Nitrogen oxides NOXIs one of the most main pollutants in the air nowadays, and research and development on pollution prevention and control technologies of the air pollution are started in the seventies of the last century. NOXEmissions problems the earliest studies in the United states and Japan, which had already made the most stringent NO in the world at that timeXEmission standards, and the addition of NO elimination in fuel boilersXTechnical measures of the equipment. NOXUnder the action of sunlight, photochemical reaction can be caused to form photochemical smog, nitric acid rain is easy to form, and ozone reduction is also related to the photochemical smog; NOXNO in (1)2The inhalation has effects on heart, liver and kidney, and also has anesthetic effect on nervous system, and its harmfulness is far greater than that expected by people. Flue gas discharged from industries such as power generation, steel and the like contains a large amount of nitrogen oxides, and if the flue gas is not treated, the exhaust gas discharged into the atmosphere can cause serious pollution, so that the discharged flue gas must be subjected to denitration treatment.
The reaction principle of denitration is that NO is mixedXFormation of N under the action of reducing agent2The reducing agent is NH3And urea mostly. The main denitration techniques today are: the Selective Catalytic Reduction (SCR) method and the selective non-catalytic reduction (SNCR) method, or a combination of both methods may be used. The SNCR technology does not need a catalyst, the reaction temperature is 750-1000 ℃, and a reducing agent is sprayed in the temperature section for reactionThe problem of large escape is mainly used for boiler furnace positions, and the device is suitable for being used independently in regions with low denitration emission requirements. The SCR technology is a catalytic reduction method, a catalyst needs to be added in a reaction interval, the reaction temperature is 250-450 ℃, the denitration efficiency of the method can exceed 85%, but the cost is high and is several times of SNCR, and the occupied area is large. Under the condition of increasingly strict environmental requirements, part of key areas have required NOXEmissions were below 50mg/Nm3This is not achieved by SNCR technology, so SCR technology will be the main direction for future denitration.
The main process route of the SCR is as follows: heating the flue gas to a temperature range required by the reaction through GGH heat exchange and a hot blast stove (if the temperature is proper, the GGH and the hot blast stove do not need to be arranged), arranging an ammonia injection grid at an inlet flue of the reactor, fully mixing the ammonia injection grid with the raw flue gas, then feeding the mixture into the reactor, and reacting NO under the action of a catalystXReduction to N2. The most important of the whole SCR process is the reactor, and whether the design is successful or not determines the final denitration efficiency.
The existing SCR denitration system is generally only provided with one reactor, and when the load changes and the total smoke quantity becomes small, the reactor has the problems of over-small treatment capacity and resource waste; in addition, the monomer reactor is too large, which causes great difficulty in manufacturing and hoisting, and further increases the cost.
In view of this, it is important to design and manufacture a multi-bin offline denitration reaction system capable of reasonably controlling the processing amount according to the load change, avoiding resource waste, and realizing the miniaturization of the reactor.
Disclosure of Invention
The invention aims to provide a multi-bin offline denitration reaction system, which can reasonably control the treatment capacity according to load change, avoid resource waste, realize the miniaturization of a reactor and facilitate the assembly and manufacture of the reactor.
The invention is realized by adopting the following technical scheme.
A multi-bin off-line denitration reaction system comprises an inlet main flue, an outlet main flue and a plurality of denitration reactors, wherein the inlet main flue is respectively connected with air inlets of the denitration reactors, the outlet main flue is respectively connected with air outlets of the denitration reactors, each air inlet is provided with an inlet baffle door for opening or closing the air inlet, and each air outlet is provided with an outlet baffle door for opening or closing the air outlet.
Further, the denitration reactor comprises a shell frame, an inlet end socket, an outlet end socket and a plurality of catalyst blocks, wherein the inlet end socket and the outlet end socket are respectively arranged at two ends of the shell frame and form a reaction inner cavity together with the shell frame, the catalyst blocks are arranged in the reaction inner cavity, the inlet end socket is provided with the air inlet, and the outlet end socket is provided with the air outlet.
Further, the inlet head includes an inlet shell having a first large end and a first small end opposite to each other, and an inlet expansion joint disposed at the first small end, the inlet baffle door being disposed on the inlet expansion joint, the first large end being connected to the shell frame; the outlet end enclosure comprises an outlet shell and an outlet expansion joint, the outlet shell is provided with a second large end and a second small end which are opposite, the outlet expansion joint is arranged at the second small end, the outlet baffle door is arranged on the outlet expansion joint, and the second large end is connected with the shell frame.
Furthermore, a regeneration air inlet is further formed in the inlet shell and communicated with the reaction inner cavity, and regeneration air is introduced into the plurality of catalyst blocks.
Further, the shell frame comprises a beam column frame and surrounding wall plates, the surrounding wall plates are coated on the beam column frame and are respectively connected with the inlet end socket and the outlet end socket, the beam column frame is provided with a plurality of supporting layers which are arranged at intervals in parallel, and the catalyst blocks are respectively arranged on the plurality of supporting layers.
Furthermore, a wall plate reinforcing rib is further arranged on the inner side of the wall enclosing plate.
Furthermore, each support layer is provided with a soot blower for cleaning soot of the corresponding catalyst block.
Furthermore, a plurality of hoisting doors are further arranged on the wall enclosing plate, and the plurality of hoisting doors correspond to the plurality of supporting layers.
Further, a rectifying grid is arranged at the top of the beam-column frame.
Further, denitration reactor still includes sliding support and a plurality of guide bracket, sliding support sets up casing frame's bottom is used for bearing casing frame, guide bracket sets up casing frame's middle part is used for spacing casing frame.
The invention has the following beneficial effects:
according to the multi-bin offline denitration reaction system provided by the invention, the inlet main flue and the outlet main flue are respectively connected with the denitration reactors, the flue gas volume processed by one conventional reactor is uniformly divided into the denitration reactors for processing, the inlet baffle door and the outlet baffle door are respectively arranged at the air inlet and the air outlet, the offline or online state of the denitration reactors can be controlled through the inlet baffle door and the outlet baffle door, and the online or offline state of the denitration reactors can be flexibly adjusted through the change of the total flue gas volume, so that part of the denitration reactors can be properly closed according to the actual flue gas volume, the waste of resources caused by the simultaneous opening of the denitration reactors is further avoided, and the stability of the denitration efficiency is ensured. Meanwhile, the reactor can be miniaturized under the condition of not influencing the total amount of flue gas treatment because of treatment by a plurality of reactors, so that the difficulty of site construction in the aspects of hoisting and manufacturing is greatly reduced, and the assembly is convenient. In addition, handle through a plurality of denitration reactors, can realize not shutting down the maintenance or change the catalyst, reach and reduce down time, guarantee the stable effect of denitration efficiency.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings needed to be used in the embodiments will be briefly described below, it should be understood that the following drawings only illustrate some embodiments of the present invention and therefore should not be considered as limiting the scope, and for those skilled in the art, other related drawings can be obtained according to the drawings without inventive efforts.
Fig. 1 is a schematic structural view of a multi-bin offline denitration reaction system provided by the invention at a first view angle;
FIG. 2 is a schematic structural diagram of a multi-bin offline denitration reaction system provided by the present invention at a second view angle;
FIG. 3 is a schematic structural diagram of the denitration reactor in FIG. 1 from a first perspective;
FIG. 4 is a schematic structural view of the denitration reactor in FIG. 1 from a second perspective;
fig. 5 is a schematic structural view of the denitration reactor in fig. 1 from a third perspective.
Icon: 100-a multi-bin off-line denitration reaction system; 110-inlet main flue; 130-outlet main flue; 150-a denitration reactor; 151-housing frame; 1511-beam column frame; 1513-surrounding wall plate; 1515-wall plate reinforcing ribs; 1517-support layer; 1519-soot blower; 153-inlet head; 1531-an inlet housing; 1533-inlet expansion joint; 1535 — inlet for regeneration air; 154-a rectifying grid; 155-outlet end enclosure; 1551-outlet housing; 1553-outlet expansion joint; 156-hoisting a door; 157-catalyst block; 158-sliding support; 159-a guide bracket; 170-inlet flapper door; 190-outlet flapper door.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. The components of embodiments of the present invention generally described and illustrated in the figures herein may be arranged and designed in a wide variety of different configurations.
Thus, the following detailed description of the embodiments of the present invention, presented in the figures, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
It should be noted that: like reference numbers and letters refer to like items in the following figures, and thus, once an item is defined in one figure, it need not be further defined and explained in subsequent figures.
In the description of the present invention, it should be noted that the terms "center", "upper", "vertical", "horizontal", "inner", "outer", etc. indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings or the orientations or positional relationships conventionally put on the products of the present invention when used, and are only used for convenience of describing the present invention and simplifying the description, but do not indicate or imply that the devices or elements referred to must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and the like are used merely to distinguish one description from another, and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it should also be noted that, unless otherwise explicitly specified or limited, the terms "disposed," "connected," "mounted," and "connected" are to be construed broadly and may, for example, be fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
As disclosed in the background art, in the existing denitration system, only one denitration reactor is usually adopted for denitration operation, when the amount of flue gas to be processed is small, the reactor cannot reach the optimal processing amount, so that the problems of excessively small processing amount and resource waste exist.
How to realize the miniaturization of the denitration reactor and adjust the total treatment capacity of the denitration reactor according to the amount of flue gas, so as to avoid resource waste is the problem to be solved by the invention.
Some embodiments of the invention are described in detail below with reference to the accompanying drawings. Features in the embodiments described below may be combined with each other without conflict.
First embodiment
With reference to fig. 1 to 5, the present embodiment provides a multi-bin offline denitration reaction system 100, which can avoid the waste of resources, can realize miniaturization, is convenient to assemble and manufacture, can realize maintenance without shutdown or catalyst replacement, and achieves the effects of reducing shutdown time and ensuring stable denitration efficiency.
The off-line denitration reaction system 100 with multiple bins provided by the embodiment comprises an inlet main flue 110, an outlet main flue 130 and multiple denitration reactors 150, wherein the inlet main flue 110 is respectively connected with air inlets of the multiple denitration reactors 150, the outlet main flue 130 is respectively connected with air outlets of the multiple denitration reactors 150, each air inlet is provided with an inlet baffle door 170 for opening or closing the air inlet, and each air outlet is provided with an outlet baffle door 190 for opening or closing the air outlet.
In actual operation, the plurality of inlet baffle doors 170 and the plurality of outlet baffle doors 190 are all electrically controlled doors, and the denitration reactor 150 is controlled to be in an online or offline state under the control of an external control machine, wherein the specifications of the baffle doors are selected according to the design temperature and the design pressure of the reactor. Of course, here inlet and outlet flapper doors 170, 190 may also be manually opened, with a worker closing portions of inlet and outlet flapper doors 170, 190 depending on the actual amount of smoke.
It should be noted that the on-line state mentioned in this embodiment refers to that both the gas inlet and the gas outlet of the denitration reactor 150 are opened, so that the denitration reactor 150 can normally perform the denitration operation, and the off-line state mentioned in this embodiment refers to that both the gas inlet and the gas outlet of the denitration reactor 150 are closed, so that the denitration reactor 150 is in a stop state and does not participate in the denitration operation.
In this embodiment, the number of the denitration reactors 150 is 6, 6 denitration reactors 150 are arranged in an array, the inlet main flue 110 is connected with 6 air inlets respectively, the outlet main flue 130 is connected with 6 air outlets respectively, the air inlet and the air outlet of each denitration reactor 150 are provided with a baffle door, the on-off of the baffle door on the air inlet and the air outlet is adjusted according to the change of the total flue gas volume, and the on-line off state of the denitration reactor 150 is controlled. Of course, the number of 6 is merely illustrative, and not limited thereto, and other numbers of denitration reactors 150 are also possible.
The denitration reactor 150 comprises a shell frame 151, an inlet end socket 153, an outlet end socket 155, a plurality of catalyst blocks 157, a sliding support 158 and a plurality of guide supports 159, wherein the inlet end socket 153 and the outlet end socket 155 are respectively arranged at two ends of the shell frame 151 and enclose a reaction cavity together with the shell frame 151, the plurality of catalyst blocks 157 are arranged in the reaction cavity, the inlet end socket 153 is provided with an air inlet, and the outlet end socket 155 is provided with an air outlet. A sliding bracket 158 is provided at the bottom of the housing frame 151 for carrying the housing frame 151, and a guide bracket 159 is provided at the middle of the housing frame 151 for limiting the housing frame 151.
In this embodiment, there are 4 catalyst blocks 157, which are arranged in the reaction chamber in 4 layers at intervals along the vertical direction, and 4 layers of catalyst are used. The catalyst block 157 is a rectangular block with a length and width dimension of 2m × 1m, and can be a plate or honeycomb catalyst. Of course, the number of layers, shape, size, etc. of the catalyst are all exemplified herein and are not limited to only the values listed in the present example.
The catalyst mentioned in the present example is a composite material having TiO2 as a base material, V2O5 as a main active component, and WO3 and MoO3 as antioxidant and antitoxic auxiliary components, and the structure and components thereof are the same as those of the conventional denitration catalyst, and reference may be made to the conventional denitration catalyst.
In the present embodiment, a rectification grill 154 is provided on the top of the housing frame 151. A square steel pipe with the thickness of 80mm multiplied by 2mm is adopted, a plurality of small modules which are convenient to install are assembled according to a flow field simulation result and are respectively installed on the uppermost layer of the reactor, and the small modules play a role in guiding and uniformly distributing inlet flue gas.
In this embodiment, the inlet expansion joint 1533 and the outlet expansion joint 1553 both function to absorb expansion and contraction displacements in the vertical and horizontal directions within the reaction chamber, and the specifications of the expansion joints are selected according to the expansion amount, temperature and pressure. In this embodiment, the inlet housing 1531 and the outlet housing 1551 are both big and small heads, and the big end and the small end are both rectangles, which play a role in communicating the external flue with the reaction chamber.
In this embodiment, the inlet housing 1531 is further provided with a regeneration air inlet 1535, the regeneration air inlet 1535 is communicated with the reaction cavity, and is configured to introduce regeneration air into the plurality of catalyst blocks 157, and the regeneration air can play a role in regeneration after the catalyst activity is reduced, so as to improve the catalytic activity of the catalyst blocks 157 again. It should be noted that in this embodiment, the regeneration air inlet 1535 is opened when the denitration reactor 150 is in the off-line state, so as to regenerate the catalyst, and the regeneration air inlet 1535 is closed when the denitration reactor 150 is in the on-line state, so as to avoid affecting the internal air pressure and the denitration efficiency.
In this embodiment, the inlet housing 1531 is further provided with a manhole door for easy installation of the grille shutter 154. The manhole door is used for checking a reaction inner cavity for daily maintenance, is 600mm multiplied by 500mm, and is arranged at the lower part of the inlet shell 1531.
The shell frame 151 comprises a beam column frame 1511, wall boards 1513 and wall board reinforcing ribs 1515, the wall boards 1513 are coated on the beam column frame 1511 and are respectively connected with the inlet end socket 153 and the outlet end socket 155, the beam column frame 1511 is provided with a plurality of supporting layers 1517 which are arranged at intervals and in parallel, and the catalyst blocks 157 are respectively arranged on the supporting layers 1517. The beam column frame 1511 is the support main body of the whole reactor, and plays a role in supporting the whole load. The wall board 1513 is also provided with wall board reinforcing ribs 1515 on the inner side, and the wall board reinforcing ribs 1515 play a role in coating and resisting negative pressure. The fairing grating 154 is disposed on top of the spar frame 1511.
In this embodiment, the supporting layer 1517 is formed by a supporting beam, the supporting beam is arranged in a groined shape, frame columns are arranged on the stomach wall plates on both sides of the main beam direction for transferring each layer of load to the sliding support 158 of the bottom layer, and since the sliding support 158 of the bottom layer is slidably arranged, in order to limit the degree of freedom of the housing frame 151 in the horizontal direction, guide supports 159 are arranged on the outer wall plates 1513 of the first, third and fourth catalyst layers from bottom to top, thereby playing a role of stabilizing the structure. The combination of the sliding support 158 for one layer of bearing weight and the three layers of guide supports 159 is beneficial to reducing the integral bottom bending moment of the denitration reactor 150 and reducing the material consumption of the denitration reactor 150.
In this embodiment, each supporting layer 1517 is provided with a soot blower 1519 for cleaning soot from the catalyst block 157, removing the soot deposited on the surface of the catalyst, and improving the utilization rate of the catalyst. The wall panel 1513 is further provided with a plurality of lifting doors 156, and the plurality of lifting doors 156 correspond to the plurality of support layers 1517. Thereby facilitating maintenance and replacement of the catalyst layer, as well as maintenance of the sootblower 1519. Specifically, the lifting door 156 is a special door for installing the catalytic caking agent, the door width is larger than the size of the catalytic caking agent 157, the lifting door 156 is provided with a heat preservation and protection plate, and the lifting door 156 can be opened under the condition that the surrounding heat preservation is not removed.
In summary, in the off-line denitration reaction system 100 with multiple bins provided in this embodiment, the flue gas volume processed by one conventional reactor is equally divided into multiple identical small denitration reactors 150 for processing, and the off-line on-line state of each denitration reactor 150 can be flexibly adjusted along with the change of the total flue gas volume, so that the stability of denitration efficiency is ensured. Meanwhile, the denitration reactors 150 are miniaturized and arranged in a matrix mode, so that the difficulty of site construction in the aspects of hoisting, manufacturing and purchasing is greatly reduced, the components of each denitration reactor 150 can be produced in batch, the components are assembled and molded on the ground, single wall plates do not need to be hoisted like large reactors, high-altitude assembly is achieved, and the assembly difficulty is low. In addition, the structure provided by the invention can flexibly adjust the off-line online state of the reactor, and can overhaul or replace the catalyst or regenerate the failed catalyst without shutdown, thereby achieving the effects of reducing the shutdown time and ensuring the stable denitration efficiency, reducing the equipment loss due to off-line, and saving the energy consumption of the matched equipment of the off-line reactor.
The optimal flue gas flow velocity in the SCR denitration process reactor is about 4-6 m/s, and the ideal denitration efficiency can be achieved in the velocity range, because the system is provided with only one reactor under the condition that the total flue gas amount is greatly changed, the flue gas flow velocity possibly deviates from the range. The reactor with the multi-bin structure is adopted, so that the flow rate can be always in the designed flow rate range by opening or closing part of the reactor, the stability of the denitration efficiency is ensured, and the equipment loss is reduced.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (10)
1. The multi-bin off-line denitration reaction system is characterized by comprising an inlet main flue, an outlet main flue and a plurality of denitration reactors, wherein the inlet main flue is respectively connected with air inlets of the denitration reactors, the outlet main flue is respectively connected with air outlets of the denitration reactors, an inlet baffle door for opening or closing the air inlet is arranged at each air inlet, and an outlet baffle door for opening or closing the air outlet is arranged at each air outlet.
2. The off-line denitration reaction system according to claim 1, wherein the denitration reactor comprises a housing frame, an inlet end enclosure, an outlet end enclosure and a plurality of catalyst blocks, the inlet end enclosure and the outlet end enclosure are respectively arranged at two ends of the housing frame and enclose a reaction cavity together with the housing frame, the plurality of catalyst blocks are arranged in the reaction cavity, the inlet end enclosure is provided with the air inlet, and the outlet end enclosure is provided with the air outlet.
3. The multi-bin offline denitration reactor system according to claim 2, wherein said inlet head comprises an inlet housing and an inlet expansion joint, said inlet housing having a first large end and a first small end opposite, said inlet expansion joint being disposed at said first small end, said inlet flapper door being disposed on said inlet expansion joint, said first large end being connected to said housing frame; the outlet end enclosure comprises an outlet shell and an outlet expansion joint, the outlet shell is provided with a second large end and a second small end which are opposite, the outlet expansion joint is arranged at the second small end, the outlet baffle door is arranged on the outlet expansion joint, and the second large end is connected with the shell frame.
4. The multi-bin offline denitration reaction system according to claim 3, wherein a regeneration air inlet is further formed in the inlet shell, and the regeneration air inlet is communicated with the reaction inner cavity and used for introducing regeneration air into the plurality of catalyst blocks.
5. The off-line denitration reaction system according to claim 2, wherein the housing frame comprises a beam column frame and surrounding wall plates, the surrounding wall plates are coated on the beam column frame and are respectively connected with the inlet end socket and the outlet end socket, the beam column frame is provided with a plurality of supporting layers which are arranged at intervals and in parallel, and the catalyst blocks are respectively arranged on the supporting layers.
6. The multi-bin offline denitration reaction system according to claim 5, wherein a wall plate reinforcing rib is further arranged on the inner side of the surrounding wall plate.
7. The multi-bin offline denitration reaction system according to claim 5, wherein each supporting layer is provided with a soot blower for cleaning the corresponding catalyst block.
8. The multi-bin offline denitration reaction system according to claim 5, wherein a plurality of hoisting doors are further arranged on the wall enclosing plate, and correspond to the plurality of supporting layers.
9. The multi-bin offline denitration reaction system according to claim 5, wherein a rectification grid is arranged at the top of the beam column framework.
10. The off-line denitration reaction system according to claim 2, wherein the denitration reactor further comprises a sliding support and a plurality of guide supports, the sliding support is arranged at the bottom of the shell frame and used for bearing the shell frame, and the guide supports are arranged in the middle of the shell frame and used for limiting the shell frame.
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