A waste gas collection and treatment device for petroleum coke calcination

Abstract

The present invention relates to the technical field of waste gas treatment devices, and specifically to a waste gas collection and treatment device for petroleum coke calcining, comprising: a waste gas treatment mechanism, the waste gas treatment mechanism comprises a box body, a partition plate and a plurality of layered plates for separating the box body are arranged inside the box body, and also comprises: an exhaust mechanism, the exhaust mechanism is arranged at the top of the box body, the exhaust mechanism comprises a discharge box, and a plurality of arc-shaped exhaust blocks for discharging waste gas to corresponding purification tanks are arranged in the discharge box; a monitoring mechanism, two monitoring mechanisms are symmetrically arranged at the inner bottom of the box body located at each purification tank, and the monitoring mechanism comprises a detection component for detecting the impurity content of waste gas, waste gas pressure and stored electricity in the purification tank. Through the arc-shaped exhaust block and the second double-way electric valve in the exhaust mechanism, it is possible to discharge the waste gas to different positions of the box body, avoid the waste gas from passing through the saturated activated carbon bed, and ensure that the waste gas mainly passes through the unsaturated activated carbon bed, thereby improving the overall efficiency of waste gas treatment.

Description

Technical Field

[0001] The invention relates to the technical field of waste gas treatment devices, and in particular to a waste gas collection and treatment device for petroleum coke calcining. Background Art

[0002] Waste gas treatment during petroleum coke calcination is an important environmental protection link in the petrochemical industry. Petroleum coke is a byproduct of petroleum refining, usually containing high carbon and impurities. A large amount of waste gas will be generated during the calcination process, including volatile organic compounds (VOCs), sulfides, nitrogen oxides (NOx) and particulate matter. If these waste gases are discharged directly without treatment, they will cause serious pollution to the environment. Therefore, the prior art, such as the Chinese patent with publication number: CN117942737A, discloses a waste gas collection and treatment device for petroleum coke calcination to treat this waste gas.

[0003] The existing waste gas collection and treatment device for petroleum coke calcining has inconsistent distribution content of pollutants in the waste gas during waste gas collection and treatment. When the existing equipment adsorbs pollutants in the waste gas through activated carbon, it usually adopts a flow-through method to make the waste gas pass through multiple activated carbons in sequence. However, since the content of pollutants in the waste gas is inconsistent, after the front activated carbon has completed the adsorption of pollutants in the waste gas, the waste gas needs to pass through the remaining activated carbon before it can be discharged, resulting in low exhaust efficiency. Summary of the invention

[0004] In view of the above shortcomings of the prior art, the present invention provides a waste gas collection and treatment device for petroleum coke calcination, which can effectively solve the problem in the prior art that due to the uneven distribution of pollutants in the waste gas, the activated carbon in the front quickly reaches a saturated state, while the activated carbon in the back is still in an unsaturated state. This uneven use leads to a decrease in the overall waste gas treatment efficiency and shortens the service life of the activated carbon.

[0005] To achieve the above objectives, the present invention is implemented through the following technical solutions:

[0006] The present invention provides a waste gas collection and treatment device for petroleum coke calcining, comprising:

[0007] An exhaust gas treatment mechanism, the exhaust gas treatment mechanism comprising a box body, a partition plate and a plurality of layered plates for partitioning the box body are arranged inside the box body, and the partition plate divides the box body into two purification areas, and the plurality of layered plates form purification tanks in the purification areas, a plurality of conduction components for transferring exhaust gas in adjacent purification tanks are arranged on both sides of the box body, and a plurality of activated carbon rods for absorbing impurities in the exhaust gas are arranged on both sides of the layered plates;

[0008] An exhaust mechanism, the exhaust mechanism is arranged on the top of the box body, the exhaust mechanism includes a discharge box fixed on the upper end of the box body, a plurality of arc-shaped exhaust blocks for discharging exhaust gas to corresponding purification tanks are arranged in the discharge box, and a second solenoid valve for controlling the arc-shaped exhaust block to discharge exhaust gas is arranged on the top of each arc-shaped exhaust block;

[0009] The monitoring mechanism has multiple monitoring mechanisms and is arranged one-to-one at the inner bottom of the purification tank. The monitoring mechanism includes a pair of detection components for detecting the impurity content of the exhaust gas, the exhaust gas pressure and the stored power in the purification tank. The outer side of the exhaust mechanism is provided with multiple indicator lights for displaying the working status of the purification tank, and the indicator lights correspond to the number of purification tanks. The indicator lights are electrically connected to the detection components.

[0010] Preferably, the partition plate is fixedly connected in the width direction of the inner middle part of the box body, a plurality of linear arrays of the layered plates are fixedly connected to the opposite surfaces of the partition plate and the box body, a plurality of linear arrays of activated carbon rods are fixedly connected to both sides of the partition plate, and a first solenoid valve is symmetrically fixedly connected to both sides of the box body, and two connecting ends of the first solenoid valve are respectively fixedly connected to a first interconnecting pipe and a second interconnecting pipe, the other end of the first interconnecting pipe is connected to one of the purification areas, and the other end of the second interconnecting pipe is connected to the other purification area.

[0011] Preferably, the conduction component includes a first air pump fixedly connected to the outside of the box, and the first air pump corresponds to the position of the purification tank. The output end of the first air pump is fixedly connected to a transmission pipe, and the end of the transmission pipe away from the first air pump is located above the first air pump and extends upward and is connected to the purification tank corresponding to the first air pump. The input end of the first air pump is fixedly connected to an intake pipe, and the end of the intake pipe away from the first air pump is connected to an adjacent purification tank.

[0012] Preferably, an isolation plate is fixedly connected to the inner wall of the discharge box and at a corresponding position of the discharge box, and the discharge box forms a discharge area corresponding to the purification area in the box body through the isolation plate, and a protective plate is fixedly connected to the inner middle part of each of the discharge areas, and a plurality of arc-shaped exhaust blocks are linearly arrayed and embedded in the side of the protective plate facing the box body, and a plurality of exhaust holes are evenly opened on the arc surface of the arc-shaped exhaust block, and a first two-position three-way solenoid valve is fixedly connected to the outer side of the discharge box, and the first two-position three-way solenoid valve has two output ends and one input end, and the two output ends of the first two-position three-way solenoid valve are fixedly connected with a connecting pipe, and the two connecting pipes are respectively located in the two discharge areas in the discharge box, and one end of the connecting pipe away from the first two-position three-way solenoid valve passes through the discharge box and extends to the inside of the discharge box, and a plurality of the second solenoid valves are fixedly connected to the side of the protective plate away from the box body, and one end of the second solenoid valve is connected to the arc-shaped exhaust block at the corresponding position through a pipeline, and the other end is connected to the connecting pipe through a pipeline.

[0013] Preferably, the detection component includes a compression barrel fixedly connected to the casing and located at the bottom of the purification tank, the outer circumferential surface of the compression barrel is alternately provided with a plurality of grooves, and each groove is fixedly provided with a plurality of air holes in a circular array, the top of the compression barrel is fixedly connected with a hemispherical cover, the center position of the inner bottom of the compression barrel is fixedly connected with a battery, the top of the battery is electrically connected with a pressure controller, the inner bottom of the compression barrel is fixedly connected with a plurality of detectors in a circular array with the pressure controller as the center, and each detector is electrically connected to the battery, two of the detection components are fixedly connected with mounting rods at the relatively located convex grooves, the rod body of the mounting rod is fixedly connected with a plurality of power generation components in a linear array, the power generation component includes a generator fixedly connected to the rod body of the mounting rod, the outer circumferential surface of the generator is fixedly connected with a plurality of connecting rods in a circular array, and each of the connecting rods is fixedly connected with a force fan at one end away from the generator.

[0014] Preferably, it also includes a heat conduction mechanism, the heat conduction mechanism includes a cooling shell fixedly connected to the center position of the bottom of the box body, one side of the cooling shell has an open end, the open end of the cooling shell is fixedly connected to a mounting block, a plurality of fans are embedded in a linear array on the side of the mounting block, two electrically controlled heat exchangers are embedded in the upper end of the cooling shell, the two electrically controlled heat exchangers correspond to the positions of the purification zones respectively, and a plurality of holes are formed on the side of the electrically controlled heat exchanger facing the box body, an S-shaped curved pipe is fixedly installed inside the cooling shell, the S-shaped curved pipe has an output end and an input end, the input end of the S-shaped curved pipe is fixedly connected to an input pipe, and the input pipe is connected to the product of the calcined petroleum coke. The exhaust gas generating process is connected, the output end of the S-shaped curved pipe is fixedly connected with an output pipe, one end of the output pipe away from the S-shaped curved pipe is fixedly connected with the input end of a first two-position three-way solenoid valve, the output pipe is connected with a heat exchanger, and the heat exchanger is installed on the outside of the box body, the bottom rectangular array of the box body is fixedly connected with a plurality of one-way valve assemblies, the one-way valve assembly includes a valve body fixedly connected to the bottom of the box body, the bottom of the valve body is slidably connected with a valve seat, the inner circumferential surface of the valve body is fixedly connected with a plurality of support rods in an annular array, the end of each support rod away from the valve body is commonly fixedly connected with a connecting block, and the connecting block and the opposite surface of the valve seat are fixedly connected with a plurality of elastic rods.

[0015] Preferably, it also includes an air cooling mechanism, which includes a transmission seat arranged on the side of the box body, the top of the transmission seat is fixedly connected with an air bag, and the side of the transmission seat is provided with a second air pump, the output end of the second air pump is fixedly connected to the transmission seat through a pipeline, and the input end of the second air pump is fixedly connected to a three-way pipe, the three-way pipe has two output ends and one input end, and the input end of the three-way pipe is connected to the input end of the second air pump, the two output ends of the three-way pipe are respectively fixedly connected to the shunt pipes located on both sides of the box body, and a plurality of second two-position three-way solenoid valves are fixedly connected to the two sides of the bottom of the box body, the second two-position three-way solenoid valves correspond to the positions and numbers of the purification areas of the box body, and the second two-position three-way solenoid valves have one output end and two input ends, the input end of one of the second two-position three-way solenoid valves on the same side is connected to the shunt pipe on the same side through a pipeline, the other input end of the second two-position three-way solenoid valve passes through the box body through a pipeline and is connected to the purification area at the same position, and the output end of the second two-position three-way solenoid valve is connected to the atmosphere.

[0016] Compared with the known prior art, the technical solution provided by the present invention has the following beneficial effects:

[0017] 1. The waste gas collection and treatment device for petroleum coke calcining can discharge the waste gas to different positions of the box through the arc-shaped exhaust block and the second double-way electric valve in the exhaust mechanism, thereby maximizing the utilization rate of activated carbon. Among them, through the second double-way electric valve in the arc-shaped exhaust block, the waste gas can be discharged into different positions of the box through the arc-shaped exhaust blocks at different positions. At the same time, it can be achieved that the activated carbon in the box that is already in a saturated state does not emit waste gas, and the waste gas after purification no longer passes through the remaining activated carbon, avoiding the waste gas from passing through the saturated activated carbon bed, ensuring that the waste gas mainly passes through the unsaturated activated carbon bed, thereby improving the overall efficiency of waste gas treatment.

[0018] 2. The waste gas collection and treatment device for petroleum coke calcination can detect the waste gas pressure and pollutants in the waste gas at different positions of the box through the detection component and the power generation component in the monitoring mechanism. At the same time, the power generation component can use the airflow generated when the waste gas flows to generate electricity, thereby serving as the energy for the operation of the monitoring mechanism. In addition, the detection component can also store the excess power of the power generation component, thereby serving as a backup energy source. Among them, the monitoring component can monitor the pollutant concentration and pressure in the waste gas in the activated carbon area at different positions in the box in real time, and judge the adsorption capacity of the activated carbon here for the pollutants in the waste gas, and then judge whether the activated carbon here is saturated and whether the pollutants in the waste gas meet the emission standards, so as to help adjust and optimize the flow and discharge path of the waste gas in the box, which helps to ensure the efficient operation of the waste gas treatment system and improve the equipment's waste gas treatment rate. The power generation component uses the airflow generated by the waste gas flow to generate electricity, which can convert the energy generated in the waste gas treatment process into electricity, provide energy for the monitoring mechanism, realize self-sufficient energy supply, reduce dependence on external power supply, and thus reduce operating costs. In addition, the excess electricity can be stored for backup, further improving the stability of the operation of the monitoring mechanism. BRIEF DESCRIPTION OF THE DRAWINGS

[0019] In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required for use in the embodiments or the prior art descriptions are briefly introduced below. Obviously, the drawings described below are only some embodiments of the present invention, and for ordinary technicians in this field, other drawings can be obtained based on these drawings without creative work.

[0020] Figure 1 It is a schematic diagram of the overall structure of the present invention;

[0021] Figure 2 It is a schematic structural diagram of the overall side of the present invention;

[0022] Figure 3 It is a schematic diagram of the structure of the present invention as a whole when viewed from above;

[0023] Figure 4 It is a schematic diagram of the structure inside the waste gas treatment mechanism of the present invention;

[0024] Figure 5 This is a schematic diagram of the structure of the bottom of the exhaust gas treatment mechanism of the present invention;

[0025] Figure 6 It is a structural schematic diagram of the exhaust mechanism of the present invention;

[0026] Figure 7 It is a schematic diagram of the structure of the exhaust mechanism conduction of the present invention;

[0027] Figure 8It is a structural schematic diagram of the monitoring mechanism of the present invention;

[0028] Fig. 9 It is a structural schematic diagram of the cross section of the monitoring mechanism of the present invention;

[0029] Fig.10 It is a structural schematic diagram of the heat conduction mechanism of the present invention;

[0030] Fig.11 It is a schematic structural diagram of the cross section of the one-way valve assembly of the present invention.

[0031] Reference numerals: 1, exhaust gas treatment mechanism; 11, box; 12, partition plate; 13, layered plate; 14, activated carbon rod; 15, conduction component; 151, first air pump; 152, transmission pipe; 153, suction pipe; 16, first solenoid valve; 161, first intercommunication pipe; 162, second intercommunication pipe;

[0032] 2. Exhaust mechanism; 21. Discharge box; 22. Isolation plate; 23. Protective plate; 24. Arc exhaust block; 25. First and second position three-way solenoid valve; 26. Connecting pipe; 27. Second solenoid valve;

[0033] 3. Monitoring mechanism; 31. Detection assembly; 311. Compression barrel; 312. Hemispherical cover; 313. Pressure controller; 314. Detector; 315. Air vent; 316. Storage battery; 32. Mounting rod; 33. Power generation assembly; 331. Generator; 332. Connecting rod; 333. Forced fan; 34. Indicator light;

[0034] 4. Heat transfer mechanism; 41. Cooling shell; 42. Electric heat transfer device; 43. S-shaped curved pipe; 44. Input pipe; 45. Output pipe; 46. One-way valve assembly; 461. Valve body; 462. Connecting block; 463. Support rod; 464. Elastic rod; 465. Valve seat; 47. Mounting block; 48. Fan; 49. Heat exchanger;

[0035] 5. Air cooling mechanism; 51. Transmission seat; 52. Air bag; 53. Second air pump; 54. Three-way pipe; 55. Second two-position three-way solenoid valve; 56. Diverter pipe. DETAILED DESCRIPTION

[0036] In order to make the purpose, technical solution and advantages of the embodiments of the present invention clearer, the technical solution in the embodiments of the present invention will be clearly and completely described below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments are 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.

[0037] The present invention will be further described below in conjunction with the embodiments.

[0038] Example: Refer to Figures 1 to 11 , the waste gas treatment mechanism 1 comprises a box body 11, a partition plate 12 and a plurality of layered plates 13 for partitioning the box body 11 are arranged inside the box body 11, and the partition plate 12 divides the box body 11 into two purification zones, and the plurality of layered plates 13 form purification tanks in the purification zones, a plurality of conduction components 15 for transferring waste gas in adjacent purification tanks are arranged on both sides of the box body 11, and a plurality of activated carbon rods 14 for absorbing impurities in the waste gas are arranged on both sides of the layered plates 13;

[0039] The exhaust mechanism 2 is arranged at the top of the box body 11. The exhaust mechanism 2 includes a discharge box 21 fixed at the upper end of the box body 11. A plurality of arc-shaped exhaust blocks 24 for discharging exhaust gas to corresponding purification tanks are arranged in the discharge box 21. The top of each arc-shaped exhaust block 24 is provided with a second solenoid valve 27 for controlling the arc-shaped exhaust block 24 to discharge exhaust gas;

[0040] The monitoring mechanism 3 has multiple monitoring mechanisms 3 and is arranged one by one at the inner bottom of the purification tank. The monitoring mechanism 3 includes a pair of detection components 31 for detecting the impurity content of the exhaust gas, the exhaust gas pressure and the stored power in the purification tank. The outer side of the exhaust mechanism 2 is provided with multiple indicator lights 34 for displaying the working status of the purification tank, and the indicator lights 34 correspond to the number of purification tanks. The indicator lights 34 are electrically connected to the detection components 31.

[0041] A partition plate 12 can be used to evenly divide the box body 11 into two parts to form two purification areas. By setting multiple layered plates 13 in each purification area, the purification area can be further divided into multiple purification tanks. The exhaust mechanism 2 can discharge the exhaust gas from purification tanks at different positions separately based on the content of exhaust gas pollutants in the current purification tank according to the monitoring mechanism 3 set in each purification tank, thereby improving the adsorption effect of the activated carbon rod 14 on exhaust gas pollutants.

[0042] Reference Figures 4 to 5 The partition plate 12 is fixedly connected in the width direction of the inner middle part of the box body 11, a plurality of layered plates 13 are fixedly connected in a linear array to the opposite surfaces of the partition plate 12 and the box body 11, a plurality of activated carbon rods 14 are fixedly connected in a linear array to both sides of the partition plate 12, and a first solenoid valve 16 is symmetrically fixedly connected to both sides of the box body 11. The two connecting ends of the first solenoid valve 16 are respectively fixedly connected to a first interconnecting pipe 161 and a second interconnecting pipe 162. The other end of the first interconnecting pipe 161 is connected to one of the purification zones, and the other end of the second interconnecting pipe 162 is connected to the other purification zone.

[0043] The partition plate 12 can be used to evenly divide the box body 11 into two purification areas, and the layered plate 13 can further divide the purification area to form a plurality of purification tanks, so that the exhaust gas can pass through the activated carbon rods 14 arranged in the purification tanks to adsorb the pollutants in the exhaust gas entering the purification tanks, thereby achieving the purpose of purifying the exhaust gas, and the first solenoid valve 16, the first interconnecting pipe 161 and the second interconnecting pipe 162 are used to realize the mutual transmission of the exhaust gas in the two purification areas, thereby realizing the interchange of the exhaust gas flow in the two purification areas.

[0044] Reference Figures 1 to 7 The conduction component 15 includes a first air pump 151 fixedly connected to the outside of the box body 11, and the first air pump 151 corresponds to the position of the purification tank. The output end of the first air pump 151 is fixedly connected to a transmission pipe 152, and one end of the transmission pipe 152 away from the first air pump 151 is located above the first air pump 151 and extends upward and is connected to the purification tank corresponding to the first air pump 151. The input end of the first air pump 151 is fixedly connected to an air intake pipe 153, and one end of the air intake pipe 153 away from the first air pump 151 is connected to an adjacent purification tank.

[0045] The first air pump 151 in the conduction component 15 can be used to transport the exhaust gas entering the purification tank to another adjacent purification tank, so that the exhaust gas can pass through the activated carbon rods 14 in multiple purification tanks until the pollutants in the exhaust gas meet the emission standards, thereby achieving the purpose of purifying the exhaust gas layer by layer.

[0046] Reference Figures 6 to 11 The inner wall of the discharge box 21 is fixedly connected with an isolation plate 22 at a corresponding position of the discharge box 21. The discharge box 21 forms a discharge area corresponding to the purification area in the box body 11 through the isolation plate 22. A protective plate 23 is fixedly connected to the inner middle of each discharge area. A plurality of arc-shaped exhaust blocks 24 are linearly arrayed and embedded on the side of the protective plate 23 facing the box body 11. A plurality of exhaust holes are evenly opened on the arc surface of the arc-shaped exhaust block 24. A first two-position three-way solenoid valve 25 is fixedly connected to the outer side of the discharge box 21. The first two-position three-way solenoid valve 25 has two output ports. and an input end, and two output ends of the first two-position three-way solenoid valve 25 are fixedly connected with a connecting pipe 26, the two connecting pipes 26 are respectively located in two discharge areas in the discharge box 21, and one end of the connecting pipe 26 away from the first two-position three-way solenoid valve 25 passes through the discharge box 21 and extends to the inside of the discharge box 21, and a plurality of second solenoid valves 27 are fixedly connected to a side of the protective plate 23 away from the box body 11, one end of the second solenoid valve 27 is connected to the arc-shaped exhaust block 24 at the corresponding position through a pipeline, and the other end is connected to the connecting pipe 26 through a pipeline.

[0047] By using multiple arc-shaped exhaust blocks 24 arranged in the discharge box 21, the transported waste gas can be transmitted in a direction, and the second solenoid valve 27 can control the delivery of waste gas to the arc-shaped exhaust block 24 at each position, thereby outputting the waste gas to the purification tanks at different positions.

[0048] Reference Figures 8 to 9 The detection component 31 includes a compression barrel 311 fixedly connected to the box body 11 and located at the bottom of the purification tank. The outer circumferential surface of the compression barrel 311 is alternately provided with a plurality of grooves, and each groove is provided with a plurality of air holes 315 in a circular array. The top of the compression barrel 311 is fixedly connected to a hemispherical cover 312. The center of the bottom of the compression barrel 311 is fixedly connected to a battery 316. The top of the battery 316 is electrically connected to a pressure controller 313. The bottom of the compression barrel 311 is provided with a circular array with the pressure controller 313 as the center. A plurality of detectors 314 are fixedly connected in a row, and each detector 314 is electrically connected to a battery 316; a mounting rod 32 is fixedly connected at a convex groove relatively to two detection components 31; a plurality of power generation components 33 are fixedly connected to a linear array of the rod body of the mounting rod 32; the power generation component 33 includes a generator 331 fixedly connected to the rod body of the mounting rod 32; a plurality of connecting rods 332 are fixedly connected to an annular array on the outer peripheral surface of the generator 331; a force fan 333 is fixedly connected to one end of each connecting rod 332 away from the generator 331.

[0049] By using the pressure controller 313 and multiple detectors 314 in the detection component 31, it is possible to detect the exhaust gas content stored in the current purification tank, the content of pollutants in the exhaust gas, and the exhaust gas emission rate, so as to judge the exhaust gas in the current purification tank and the adsorption of pollutants in the exhaust gas by the activated carbon rod 14. The power generation component 33 can use the airflow generated by the flow of exhaust gas as power to provide power supply for the detection component 31.

[0050] Reference Figure 3 , Figure 10 to Figure 11, and also includes a heat conduction mechanism 4, which includes a cooling shell 41 fixedly connected to the center position of the bottom of the box body 11, one side of the cooling shell 41 has an open end, the open end of the cooling shell 41 is fixedly connected to a mounting block 47, and a plurality of fans 48 are embedded in a linear array on the side of the mounting block 47, and two electrically controlled heat exchangers 42 are embedded in the upper end of the cooling shell 41, and the two electrically controlled heat exchangers 42 correspond to the positions of the purification zones respectively, and a plurality of holes and grooves are opened on the side of the electrically controlled heat exchanger 42 facing the box body 11, and an S-shaped curved pipe 43 is fixedly installed inside the cooling shell 41, and the S-shaped curved pipe 43 has an output end and an input end, and the input end of the S-shaped curved pipe 43 is fixedly connected to an input pipe 44, and the input pipe 44 is connected to a process of waste gas generated by calcining petroleum coke, and the S-shaped The output end of the curved pipe 43 is fixedly connected to an output pipe 45, and one end of the output pipe 45 away from the S-shaped curved pipe 43 is fixedly connected to the input end of the first two-position three-way solenoid valve 25. The output pipe 45 is connected to a heat exchanger 49, and the heat exchanger 49 is installed on the outside of the box body 11. The bottom rectangular array of the box body 11 is fixedly connected to a plurality of one-way valve assemblies 46. The one-way valve assembly 46 includes a valve body 461 fixedly connected to the bottom of the box body 11, and the bottom of the valve body 461 is slidably connected to a valve seat 465. The inner circumferential surface of the valve body 461 is fixedly connected to a plurality of support rods 463 in an annular array, and one end of each support rod 463 away from the valve body 461 is commonly fixedly connected to a connecting block 462, and the connecting block 462 is fixedly connected to a plurality of elastic rods 464 on the opposite surface of the valve seat 465.

[0051] By utilizing the S-shaped curved pipe 43 and the fan 48 in the heat conduction mechanism 4, it is possible to absorb the airflow generated by the external wind and perform heat-cold exchange on the exhaust gas generated in the S-shaped curved pipe 43, thereby achieving a cooling effect on the exhaust gas flowing in the S-shaped curved pipe 43, and the airflow used for heat-cold exchange acts on the thermal regeneration of the activated carbon rod 14.

[0052] Reference Figures 1 to 3, and also includes an air cooling mechanism 5, the air cooling mechanism 5 includes a transmission seat 51 arranged on the side of the box body 11, the top of the transmission seat 51 is fixedly connected with an air bag 52, and the side of the transmission seat 51 is provided with a second air pump 53, the output end of the second air pump 53 is fixedly connected with the transmission seat 51 through a pipeline, and the input end of the second air pump 53 is fixedly connected with a three-way pipe 54, the three-way pipe 54 has two output ends and one input end, and the input end of the three-way pipe 54 is connected with the input end of the second air pump 53, and the two output ends of the three-way pipe 54 are respectively fixedly connected with the air bags located on both sides of the box body 11. The shunt pipe 56 and the bottom sides of the box body 11 are fixedly connected with a plurality of second two-position three-way solenoid valves 55, the second two-position three-way solenoid valves 55 correspond to the positions and numbers of the purification zones of the box body 11, and the second two-position three-way solenoid valves 55 have an output end and two input ends, the input end of one of the second two-position three-way solenoid valves 55 on the same side is connected to the shunt pipe 56 on the same side through a pipeline, the other input end of the second two-position three-way solenoid valve 55 is connected to the purification zone at the same position through a pipeline penetrating the box body 11, and the output end of the second two-position three-way solenoid valve 55 is connected to the atmosphere.

[0053] By utilizing the second air pump 53 in the air cooling mechanism 5 , the purified exhaust gas can be recovered to the air bag 52 for storage, thereby being used to cool the activated carbon rods 14 after thermal regeneration, thereby restoring the activated carbon rods 14 to room temperature.

[0054] The operating principle of this embodiment is as follows:

[0055] Step 1: First, the waste gas generated during the previous process is connected to the input pipe 44 through a pipeline, so that the high-temperature waste gas is guided to the S-shaped curved pipe 43 through the input pipe 44 (the waste gas generated by the calcination of petroleum coke is of high temperature because: the calcination process of petroleum coke is often carried out in a high-temperature furnace, such as a rotary kiln, a roasting furnace, etc. These furnaces work under high temperature conditions, and the waste gas will also absorb a large amount of heat when passing through the furnace body, thereby maintaining a high temperature, resulting in the temperature of the waste gas reaching the range of 800-1200°C). At the same time, the equipment is started. At this time, the controller controls the fan 48 located in the mounting block 47 to start (the controller is a prior art and is not drawn in the figure), and as the fan 48 is started (Note: when the fan 48 is started, the outside air is sucked into the cooling shell 41), the outside air will continuously enter the cooling shell 41, and at this time the high-temperature waste gas flowing in the S-shaped curved pipe 43 The S-shaped curved pipe 43 will exchange heat with the outside air entering the cooling shell 41 (the main constituent materials of the S-shaped curved pipe 43 are: copper, aluminum, etc., which are materials with good thermal conductivity), so that the outside air entering the cooling shell 41 and the high-temperature exhaust gas flowing in the S-shaped curved pipe 43 exchange heat, thereby heating the outside air (the outside air heated in the cooling shell 41 is hereinafter referred to as hot air), and at the same time, the high-temperature exhaust gas flowing in the S-shaped curved pipe 43 is cooled. Since the waste gas collection and treatment device for petroleum coke calcination generates a large amount of heat during operation, it is generally installed in a special area in the factory, and a good ventilation and cooling system is configured in this area to ensure that the air temperature in this area is maintained at a stable value (and the outside air in this scheme refers to the outside air in the equipment installation area), and this temperature range is generally between 20°C and 30°C;

[0056] At the same time, in order to enhance the heating effect (heat exchange efficiency) of the high-temperature exhaust gas flowing in the S-shaped curved pipe 43 on the air entering the cooling shell 41, the S-shaped curved pipe 43 is set to have multiple sections of S-shaped bends, which can effectively increase the flow time of the high-temperature exhaust gas in the S-shaped curved pipe 43, thereby extending the contact time between the high-temperature exhaust gas in the S-shaped curved pipe 43 and the air in the cooling shell 41, thereby improving the heat exchange efficiency between the high-temperature exhaust gas and the outside air, because each bend section of the high-temperature exhaust gas in the pipe will increase the flow path, so that it will pass through a longer time before reaching the output end. This extended flow time allows the high-temperature exhaust gas to have a longer contact time with the cooling medium (such as outside air), thereby improving the efficiency of heat transfer and dissipation. At the same time, the structure of the multiple sections of the S-shaped curved pipe 43 can guide the high-temperature exhaust gas to continuously turn along the inner wall of the pipe, thereby increasing the contact area between the high-temperature exhaust gas and the inner wall of the pipe. This design helps to enhance the heat exchange between the high-temperature exhaust gas and the inner wall of the pipe and improve the effect of heat exchange.

[0057] Among them, as the fan 48 continuously blows outside air into the cooling shell 41 (the outside air at this time also refers to the outside air in the equipment installation area, that is, the outside air temperature is maintained between 20°C and 30°C), the air pressure in the cooling shell 41 continues to rise, and the air pressure in the cooling shell 41 can only be reduced by the electric control heat exchanger 42 and the one-way valve assembly 46 in the cooling shell 41, and the electric control heat exchanger 42 is responsible for discharging the outside air in the cooling shell 41 into the corresponding purification area in the exhaust gas treatment mechanism 1 (the electric control heat exchanger 42 is controlled to be turned on or off by the controller, and when the electric control heat exchanger 42 is turned off, the outside air The one-way valve assembly 46 discharges the hot air heated by the high-temperature exhaust gas flowing through the S-shaped curved pipe 43 back into the outside environment. At this time, since the electric-controlled heat exchanger 42 is in a closed state, as the air pressure in the cooling shell 41 continues to increase, a downward air pressure is generated on the valve seat 465 in the one-way valve assembly 46, thereby separating the valve seat 465 from the valve body 461. In addition, in order to ensure that when the electric-controlled heat exchanger 42 is opened later, the outside air can smoothly pass through the electric-controlled heat exchanger 42 and enter the exhaust gas treatment mechanism 1, an elastic rod 464 is provided in the valve seat 465. The elastic rod 464 has a strong traction on the valve seat 465, so that the valve seat 465 and the valve body 461 can be separated only when the air pressure in the cooling shell 41 is higher than a certain value (the specific value is determined by the constituent material of the elastic rod 464 and the number of the elastic rods 464, and the staff can customize the value according to the use needs). As the valve seat 465 and the valve body 461 separate, the hot air in the cooling shell 41 also begins to be continuously discharged to the external environment, thereby maintaining the air pressure in the cooling shell 41 in a relatively stable range, thereby ensuring the stability of the air pressure in the cooling shell 41. , and also enhances the fluidity of the outside air, thereby enhancing the cooling effect of the outside air on the high-temperature exhaust gas flowing in the S-shaped curved pipe 43 (enhanced outside air fluidity can increase the intensity of convective heat exchange, and strong convection can make the heat exchange process between the high-temperature exhaust gas and the outside air more efficient, resulting in a faster drop in the exhaust gas temperature, especially in the S-shaped curved pipe 43, the enhanced air fluidity can more effectively take away the heat on the pipe surface, thereby improving the cooling effect on the high-temperature exhaust gas), and when one of the electrically controlled heat exchangers 42 is opened, the air pressure inside the cooling shell 41 is insufficient to support the opening of the one-way valve assembly 46.

[0058] Step 2: After the first step of processing, the temperature of the waste gas after cooling is lower than that when it is just input due to heat exchange with the outside air, and it is kept consistent with the temperature of the hot air in the cooling shell 41. Because in the cooling shell 41, the high-temperature waste gas in the S-shaped curved pipe 43 contacts the outside air in the cooling shell for heat exchange. Through this process, the heat of the high-temperature waste gas is transferred to the outside air of the cooling shell. This heat exchange gradually reduces the temperature of the high-temperature waste gas, while the air in the cooling shell absorbs heat and heats up. Finally, after sufficient heat exchange, the temperature of the high-temperature waste gas and the air in the cooling shell will tend to be consistent, and the temperature of the high-temperature waste gas and the outside air in the cooling shell will be introduced later. Note that at this time, the temperature of the high-temperature waste gas and the air in the cooling shell is higher than the outside air temperature;

[0059] The high-temperature exhaust gas is transported to the output pipe 45 through the S-shaped curved pipe 43, and the heat exchanger 49 provided in the output pipe 45 can further cool the high-temperature exhaust gas, so that the high-temperature exhaust gas is consistent with the environment (the heat exchanger 49 is a prior art, which mainly transfers the heat in the high-temperature exhaust gas to the cooling medium (such as air or water) through efficient heat conduction, so that the temperature of the exhaust gas is gradually reduced to a temperature close to that of the cooling medium. Under the action of the heat exchanger, a temperature difference is formed between the exhaust gas and the cooling medium, so that heat is continuously transferred from the exhaust gas to the cooling medium. Finally, the temperature of the exhaust gas will tend to the temperature of the cooling medium, and the temperature close to the ambient temperature is between 20°C and 30°C);

[0060] The output pipe 45 further transports the exhaust gas (the exhaust gas temperature at this time is close to the ambient temperature, both between 20°C and 30°C) to the first two-position three-way solenoid valve 25 (the first two-position three-way solenoid valve 25 is also controlled by the controller). At this time, the first two-position three-way solenoid valve 25 will open one of the two output ends, thereby transmitting the exhaust gas to the discharge box 21 on the same side of the connecting pipe 26 through the connecting pipe 26 fixedly connected to the output end, and the discharge box 21 is evenly divided into two parts by the isolation plate 22. When the connecting pipe 26 located on the same side transmits the exhaust gas to the same part of the discharge box 21, the connecting pipe 26 will be connected to each arc exhaust block 24 through the second solenoid valve 27 (the second solenoid valve 27 in each arc exhaust block 24 is connected to the controller, and only one second solenoid valve 27 can be opened at a time).

[0061] Among them, the distribution position of the arc-shaped exhaust block 24 in the discharge box 21 corresponds to the structure of the box body 11 in the exhaust gas treatment mechanism 1, and the box body 11 is also evenly divided into two parts through the partition plate 12, thereby forming two purification areas (these two purification areas correspond to the two parts of the discharge box 21 divided by the isolation plate 22), and multiple layered plates 13 further divide the two purification areas into multiple purification tanks (the number and position of the purification tanks correspond to the arc-shaped exhaust blocks 24), and activated carbon rods 14 are arranged in the layered plates 13 to absorb pollutants in the exhaust gas entering the purification tank.

[0062] At this time, the second solenoid valve 27 close to the first two-position three-way solenoid valve 25 is opened under the control of the controller, causing the exhaust gas to enter the corresponding position in the arc-shaped exhaust block 24, and the arc-shaped exhaust block 24 discharges the exhaust gas into the corresponding purification tank through the exhaust hole (each purification tank is a separate sealed space), so as to use the activated carbon rods 14 alternating with each other in the purification tank to complete the adsorption of pollutants in the exhaust gas entering the purification tank. At this time, the exhaust gas and the activated carbon rods 14 have the same temperature. The activated carbon rods 14 are cooled by the flow of the purified exhaust gas, so the temperature of the activated carbon rods 14 is also consistent with the exhaust gas and the ambient temperature (the cooling process of the activated carbon rods 14 by the purified exhaust gas will be introduced later), both of which are normal ambient temperatures. Keeping the exhaust gas and the activated carbon rods 14 at the same ambient temperature helps to improve the adsorption efficiency of the activated carbon, because at normal ambient temperature, the pore structure and surface activity of the activated carbon can remain stable, maximizing the adsorption of pollutants in the exhaust gas. The temperature consistency also avoids the fluctuation of the activated carbon performance caused by the temperature difference, and ensures its stable thermal regeneration ability. When the exhaust gas is continuously discharged into the corresponding purification tank through the arc exhaust block 24, the monitoring mechanism 3 located in the purification tank can detect the amount of exhaust gas discharged into the purification tank at this time and the content of pollutants in the exhaust gas (the specific function and working method of the monitoring mechanism 3 are explained in the third step). Of course, when the monitoring mechanism 3 detects that the exhaust gas pressure in the purification tank reaches a certain value, and the pollutants in the exhaust gas have not been completely adsorbed, the monitoring mechanism 3 will send a signal to the controller, and the controller will start the corresponding first air pump 151, so as to transfer the exhaust gas in the purification tank from one purification tank to another purification tank, thereby treating the exhaust gas that has not been purified in the previous purification tank. The waste gas is further purified and passes through multiple purification tanks in this order until the monitoring mechanism 3 in a certain purification tank detects that the waste gas meets the emission standards. Then, the waste gas will be discharged into the shunt pipe 56 from the second two-position three-way solenoid valve 55 in the purification tank. Under the action of the suction force of the second air pump 53, the shunt pipe 56 stores the purified waste gas in the air bag 52 (the temperature of the purified waste gas stored in the air bag 52 will not change, and the specific role of the gas stored in the air bag 52 will be described later), thereby avoiding the need for the waste gas after purification to be purified through the subsequent purification tank (each purification tank is provided with an activated carbon rod 14), thereby reducing the flow path during waste gas purification and improving the waste gas purification efficiency of the equipment;

[0063] At the same time, when the exhaust gas reaches the last purification tank in the purification zone, the first solenoid valve 16 will be activated, so that the two purification zones in the discharge box 21 are temporarily connected to each other, and then the exhaust gas is transferred to the purification tank of another purification zone, so that the exhaust gas continues to be purified in the purification tank of another purification zone. When the exhaust gas starts to transfer from one purification zone to another, it indicates that the activated carbon rods 14 in all the purification tanks in the previous purification zone are in a saturated state and have lost the function of purifying the exhaust gas. When the exhaust gas is completely transferred to another purification zone, the purification zone is completely closed. With the closure of the purification zone, the electric-controlled heat exchanger 42 at the corresponding position of the closed purification zone is opened (the two electric-controlled heat exchangers 42 cannot be opened at the same time, and only one of them can be opened in the same time period);

[0064] Among them, since the temperature of the high-temperature exhaust gas flowing in the S-shaped curved pipe 43 can reach the range of 800-1200°C, and the temperature for thermal regeneration of the activated carbon rod 14 requires a temperature between 600°C and 900°C, the high-temperature exhaust gas flows in the S-shaped curved pipe 43 and exchanges heat with the air in the cooling shell 41, thereby reducing the original high-temperature exhaust gas temperature of 800-1200°C to between 600°C and 900°C, and increasing the original 20-30°C air temperature in the cooling shell 41 to between 600°C and 900°C (when the high-temperature exhaust gas flows in the S-shaped curved pipe 43, the heat of the high-temperature exhaust gas is transferred through the S-shaped curved pipe The heat of the high-temperature exhaust gas in the S-shaped curved duct 43 is transferred to the air in the cooling shell 41, and the amount of high-temperature exhaust gas in the S-shaped curved duct 43 is less than the amount of air in the cooling shell 41, resulting in that in the S-shaped curved duct 43, when the heat of the high-temperature exhaust gas is transferred to the air in the cooling shell 41, the total heat of the exhaust gas is higher than the total heat of the air in the cooling shell. This is because the heat density of the exhaust gas is higher, while the heat density of the air in the cooling shell is lower. Due to the heat difference between the exhaust gas and the air during the heat transfer process, the heat will be transferred from the high-temperature exhaust gas to the cooling air until the heat is balanced. Finally, the temperatures of the exhaust gas and the air tend to an intermediate value of 600°C to 900°C to achieve heat exchange. It should be noted that there is a volume difference (equal to the gas volume difference) between the volume size of the cooling shell 41 and the total volume of the S-shaped curved pipe 43 in the cooling shell 41. This volume difference is based on the premise that the air in the cooling shell 41 and the exhaust gas in the S-shaped curved pipe 43 reach the pyrolysis temperature after dynamic heat equilibrium. According to the first law of thermodynamics, heat is always transferred from a high-temperature object to a low-temperature object. The heat of the high-temperature exhaust gas is gradually absorbed by the air in the cooling shell, causing the exhaust gas temperature to drop. At the same time, the air temperature in the cooling shell increases, thereby achieving a temperature balance. This heat exchange causes the exhaust gas temperature to drop from 800-1200°C to 600-900°C. , and the air temperature in the cooling shell rises to 600-900°C), so that the high-temperature exhaust gas is kept consistent with the air temperature in the cooling shell 41, so the air in the cooling shell 41 heated by the high-temperature exhaust gas can reach the temperature required for the thermal regeneration of the activated carbon rod 14, thereby realizing the thermal regeneration of the activated carbon rod 14 (the thermal regeneration principle of activated carbon is to heat the activated carbon to a high temperature, and the pollutants adsorbed on the surface of the high-temperature activated carbon are volatilized or decomposed. During the heating process, the organic matter adsorbed on the activated carbon is gasified or burned, the pores of the activated carbon are cleared, and its adsorption capacity is restored. After regeneration, the activated carbon can be reused to remove pollutants in gas or liquid);

[0065] When the electric-controlled heat transfer device 42 is opened to introduce high-temperature air into the purification zone, the second two-position three-way solenoid valve 55 located at the same position in the purification zone will be fully opened (the output end of the second two-position three-way solenoid valve 55 is opened to discharge the high-temperature air into the atmosphere. At this time, the output end of the second two-position three-way solenoid valve 55 is connected to the input end of the second two-position three-way solenoid valve 55 connected to the purification zone, and the input end connected to the shunt pipe 56 is closed);

[0066] Thereby, the thermal regeneration of the activated carbon rods 14 in the saturated state in the purification zone is completed, and based on this, the thermal regeneration of the activated carbon rods 14 in the two purification zones is completed in sequence (when the activated carbon rods 14 in one purification zone are thermally regenerated, the exhaust gas is purified in the other purification zone, and the two purification zones cannot perform thermal regeneration of the activated carbon rods 14 at the same time. At the same time, only the activated carbon rods 14 in one purification zone can be thermally regenerated, and the activated carbon rods 14 after thermal regeneration have a relatively high temperature, so the activated carbon rods 14 will be cooled by flowing through the purified exhaust gas later on), avoiding the operation of manually replacing the activated carbon and improving the utilization rate of the activated carbon.

[0067] Among them, after the activated carbon rod 14 completes thermal regeneration, the purified exhaust gas stored in the airbag 52 will be transported to the purification area by the second air pump 53 (the temperature of the purified exhaust gas will not change and will also be maintained between 20°C and 30°C). That is, the second air pump 53 transmits the purified exhaust gas stored in the airbag 52 to the diversion pipe 56, and then opens the two input ends of the second two-position three-way solenoid valve 55 (the two input ends of the second two-position three-way solenoid valve 55 are opened and the input end is closed), thereby completing the thermal regeneration of the activated carbon rod. 14 has a cooling effect (the electrically controlled heat transfer device 42 is in a closed state when the airbag 52 starts to transport gas), and when the gas transported in the purification area reaches a certain pressure value, the gas transported to the purification area will be discharged from the output end of the second two-position three-way solenoid valve 55 (that is, at this time, the input end of the second two-position three-way solenoid valve 55 connected to the shunt pipe 56 is closed, and the input end of the second two-position three-way solenoid valve 55 connected to the purification area is in an open state), and when the thermal regeneration and cooling of the activated carbon rods 14 in the purification area are completed, the second two-position three-way solenoid valve 55 will be completely closed.

[0068] Step 3: When the exhaust gas enters the purification tank, the detection component 31 of the monitoring mechanism 3 located in the purification tank is responsible for detecting the content of the exhaust gas in the purification tank, the content of pollutants in the exhaust gas and the proportion of different pollutants in the exhaust gas.

[0069] Among them, as the exhaust gas continues to enter the purification tank, the air pressure in the purification tank becomes stronger and stronger, and the stronger and stronger air pressure acts on the hemispherical cover 312 of the detection component 31, and the hemispherical cover 312 will further apply the air pressure to the compression barrel 311, thereby causing the compression barrel 311 to be compressed. As the compression barrel 311 is compressed, the hemispherical cover 312 will contact the pressure controller 313. When the pressure on the pressure controller 313 reaches a specified value (the specified value can be customized by the user according to actual needs), the first air pump 151 will start, thereby transferring the exhaust gas in the purification tank to the adjacent purification tank. When the pressure on the pressure controller 313 does not reach the specified value (just reaches the specified value), the detector 314 in the detection component 31 detects that the exhaust gas at this time meets the emission standards. , the first air pump 151 will not start, and the second two-position three-way solenoid valve 55 will be started, thereby transmitting the exhaust gas (purified exhaust gas) in the purification tank here to the air bag 52. When the detector 314 in the pressure controller 313 detects that the content of pollutants in the exhaust gas has not changed when the exhaust gas is transmitted from one purification tank to another purification tank, it indicates that the activated carbon rod 14 in the previous purification tank is already in a saturated state and cannot absorb the pollutants in the exhaust gas. Therefore, the monitoring mechanism 3 will control the second solenoid valve 27 corresponding to this purification tank to close, so that the exhaust gas no longer passes through this purification tank, thereby achieving the abandonment of this purification tank and preventing the exhaust gas from passing through this purification tank again (this purification tank indicates that the activated carbon rod 14 is already in a saturated state), thereby reducing the purification path of the exhaust gas and improving the purification efficiency of the exhaust gas.

[0070] Among them, the detection component 31 can control the indicator light 34 at the corresponding position to display different colors according to different detection results. For example, when the purification tank is abandoned, the indicator light 34 located here is displayed in red; when the pressure in the purification tank reaches a specified value and the purification of the exhaust gas has not been completed, the indicator light 34 here is displayed in yellow; when the pressure in the purification tank reaches a specified value and the purification of the exhaust gas is completed, the indicator light 34 here is displayed in green (this example is for illustration, and the specific prompt method of the indicator light 34 is customized according to actual needs).

[0071] Among them, all other electric drive devices in the equipment except the monitoring mechanism 3 are powered by an external power supply, and the power of the monitoring mechanism 3 comes from the power generation component 33 (the independent power supply can ensure that the monitoring mechanism 3 obtains a stable power supply, reducing equipment failures or data errors caused by power supply fluctuations or interference). Whether the exhaust gas is converted from one purification tank to another purification tank, or the exhaust gas is directly discharged from the current purification tank, the exhaust gas will generate airflow during transmission, and the airflow generated by the exhaust gas during transmission will be blocked by the force fan 333, thereby causing the force fan 333 to rotate, and with the rotation of the force fan 333, the generator 331 starts to work, and the generator 331 is provided with a permanent magnet stator and a coil rotor. When the generator 331 is subjected to the force fan 333 and rotates in a circle, the generator 331 will rotate at a high speed, thereby obtaining the rotation of the coil rotor, so that the generator 331 generates electricity, and half of the electricity generated by the generator 331 acts on the detection component 31 to cause operation, and the other half is stored in the battery 316 in the detection component 31 as a backup energy source.

[0072] The above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit it. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the aforementioned embodiments, or make equivalent replacements for some of the technical features therein. However, these modifications or replacements will not cause the essence of the corresponding technical solutions to deviate from the protection scope of the technical solutions of the embodiments of the present invention.

Claims

1. A waste gas collection and treatment device for petroleum coke calcination, characterized in that: include: An exhaust gas treatment mechanism (1), the exhaust gas treatment mechanism (1) comprising a box (11), a partition plate (12) and a plurality of layered plates (13) for partitioning the box (11) being arranged inside the box (11), the partition plate (12) dividing the box (11) into two purification zones, the plurality of layered plates (13) forming purification tanks in the purification zones, a plurality of conduction components (15) for transferring exhaust gas in adjacent purification tanks being arranged on both sides of the box (11), and a plurality of activated carbon rods (14) for absorbing impurities in the exhaust gas being arranged on both sides of the layered plates (13); An exhaust mechanism (2), the exhaust mechanism (2) being arranged at the top of the box body (11), the exhaust mechanism (2) comprising a discharge box (21) fixed at the upper end of the box body (11), a plurality of arc-shaped exhaust blocks (24) for discharging exhaust gas to corresponding purification tanks being arranged in the discharge box (21), and a second solenoid valve (27) for controlling the arc-shaped exhaust block (24) to discharge exhaust gas is arranged at the top of each of the arc-shaped exhaust blocks (24); A monitoring mechanism (3), the monitoring mechanism (3) having a plurality of monitoring mechanisms (3) arranged one-to-one at the inner bottom of the purification tank, the monitoring mechanism (3) comprising a pair of detection components (31) for detecting the impurity content of the exhaust gas, the exhaust gas pressure and the stored power in the purification tank, the outer side of the exhaust mechanism (2) is provided with a plurality of indicator lights (34) for displaying the working status of the purification tank, and the indicator lights (34) correspond to the number of the purification tanks, and the indicator lights (34) are electrically connected to the detection components (31).

2. The waste gas collection and treatment device for petroleum coke calcination according to claim 1, characterized in that: The partition plate (12) is fixedly connected in the width direction of the inner middle part of the box body (11); a plurality of the layered plates (13) are fixedly connected in a linear array to the opposite surfaces of the partition plate (12) and the box body (11); a plurality of the activated carbon rods (14) are fixedly connected in a linear array to both sides of the partition plate (12); a first solenoid valve (16) is symmetrically fixedly connected to both sides of the box body (11); two connecting ends of the first solenoid valve (16) are respectively fixedly connected to a first interconnecting pipe (161) and a second interconnecting pipe (162); the other end of the first interconnecting pipe (161) is connected to one of the purification zones, and the other end of the second interconnecting pipe (162) is connected to the other purification zone.

3. The waste gas collection and treatment device for petroleum coke calcining according to claim 1, characterized in that: The conduction component (15) comprises a first air pump (151) fixedly connected to the outside of the box (11), and the first air pump (151) corresponds to the position of the purification tank. The output end of the first air pump (151) is fixedly connected to a transmission pipe (152), and the end of the transmission pipe (152) away from the first air pump (151) is located above the first air pump (151) and extends upward and is connected to the purification tank corresponding to the first air pump (151). The input end of the first air pump (151) is fixedly connected to an air intake pipe (153), and the end of the air intake pipe (153) away from the first air pump (151) is connected to an adjacent purification tank.

4. The waste gas collection and treatment device for petroleum coke calcination according to claim 1, characterized in that: An isolation plate (22) is fixedly connected to the inner wall of the discharge box (21) and at a corresponding position of the discharge box (21); the discharge box (21) forms a discharge area corresponding to the purification area in the box body (11) through the isolation plate (22); a protective plate (23) is fixedly connected to the inner middle of each discharge area; a plurality of arc-shaped exhaust blocks (24) are linearly arrayed and embedded on a side of the protective plate (23) facing the box body (11); a plurality of exhaust holes are evenly formed on the arc surface of the arc-shaped exhaust block (24); a first two-position three-way solenoid valve (25) is fixedly connected to the outer side of the discharge box (21); the first two-position three-way solenoid valve (25) has two An output end and an input end, the two output ends of the first two-position three-way solenoid valve (25) are both fixedly connected to a connecting pipe (26), the two connecting pipes (26) are respectively located in two discharge areas in the discharge box (21), and one end of the connecting pipe (26) away from the first two-position three-way solenoid valve (25) passes through the discharge box (21) and extends into the inside of the discharge box (21), a plurality of the second solenoid valves (27) are fixedly connected to a side of the protective plate (23) away from the box body (11), one end of the second solenoid valve (27) is connected to the arc-shaped exhaust block (24) at a corresponding position through a pipeline, and the other end is connected to the connecting pipe (26) through a pipeline.

5. The waste gas collection and treatment device for petroleum coke calcination according to claim 1, characterized in that: The detection assembly (31) comprises a compression barrel (311) fixedly connected to a box body (11) and located at the bottom of the purification tank; the outer peripheral surface of the compression barrel (311) is alternately provided with a plurality of grooves, and each groove is provided with a plurality of air holes (315) fixedly arranged in a circular array; the top of the compression barrel (311) is fixedly connected to a hemispherical cover (312); a storage battery (316) is fixedly connected to the center of the bottom of the compression barrel (311); the top of the storage battery (316) is electrically connected to a pressure controller (313); the bottom of the compression barrel (311) is provided with a circular array with the pressure controller (313) as the center. A plurality of detectors (314) are fixedly connected, and each detector (314) is electrically connected to a storage battery (316); two detection components (31) are fixedly connected to mounting rods (32) at the convex grooves opposite to each other; a plurality of power generation components (33) are fixedly connected to the rod bodies of the mounting rods (32) in a linear array; the power generation components (33) include a generator (331) fixedly connected to the rod bodies of the mounting rods (32); a plurality of connecting rods (332) are fixedly connected to the outer peripheral surfaces of the generators (331) in an annular array; and a force-bearing fan (333) is fixedly connected to one end of each connecting rod (332) away from the generator (331).

6. The waste gas collection and treatment device for petroleum coke calcining according to claim 1, characterized in that: The heat conduction mechanism (4) further comprises a cooling shell (41) fixedly connected to the center position of the bottom of the box body (11), one side of the cooling shell (41) having an open end, the open end of the cooling shell (41) being fixedly connected to a mounting block (47), a plurality of fans (48) being embedded in a linear array on the side of the mounting block (47), two electrically controlled heat exchangers (42) being embedded in the upper end of the cooling shell (41), the two electrically controlled heat exchangers (42) respectively corresponding to the positions of the purification zones, and a plurality of holes and grooves being formed on a side of the electrically controlled heat exchangers (42) facing the box body (11), an S-shaped curved pipe (43) being fixedly installed inside the cooling shell (41), the S-shaped curved pipe (43) having an output end and an input end, the input end of the S-shaped curved pipe (43) being fixedly connected to an input pipe (44), the input pipe (44) being connected to a process of waste gas generated by calcining petroleum coke, the S-shaped curved pipe (43) being fixedly connected to the input end of the S-shaped curved pipe (43), the input pipe (44) being connected to a process of waste gas generated by calcining petroleum coke, and the S-shaped curved pipe (43) being fixedly connected to the input end of the S-shaped curved pipe (43), the input pipe (44) being connected to a process of waste gas generated by calcining petroleum coke, and the S-shaped curved pipe (43) being fixedly connected to the input end of the S-shaped curved pipe (43). The output end of the pipeline (43) is fixedly connected to an output pipe (45), one end of the output pipe (45) away from the S-shaped curved pipeline (43) is fixedly connected to the input end of the first two-position three-way solenoid valve (25), the output pipe (45) is connected to a heat exchanger (49), and the heat exchanger (49) is installed on the outside of the box (11), and a plurality of one-way valve assemblies (46) are fixedly connected to the bottom of the box (11) in a rectangular array, the one-way valve assembly (46) comprises a valve body (461) fixedly connected to the bottom of the box (11), the bottom of the valve body (461) is slidably connected to a valve seat (465), the inner circumferential surface of the valve body (461) is fixedly connected to a plurality of support rods (463) in an annular array, one end of each of the support rods (463) away from the valve body (461) is commonly fixedly connected to a connection block (462), and the surface of the connection block (462) opposite to the valve seat (465) is fixedly connected to a plurality of elastic rods (464).

7. The waste gas collection and treatment device for petroleum coke calcination according to claim 1, characterized in that: The air cooling mechanism (5) further comprises an air cooling mechanism (5), the air cooling mechanism (5) comprising a transmission seat (51) arranged on the side of the box body (11), the top of the transmission seat (51) being fixedly connected to an air bag (52), the side of the transmission seat (51) being provided with a second air pump (53), the output end of the second air pump (53) being fixedly connected to the transmission seat (51) via a pipeline, the input end of the second air pump (53) being fixedly connected to a three-way pipe (54), the three-way pipe (54) having two output ends and one input end, the input end of the three-way pipe (54) being connected to the input end of the second air pump (53), the two output ends of the three-way pipe (54) being respectively fixedly connected to a plurality of air bags located on the box body (11). (11) on both sides of the shunt pipe (56), a plurality of second two-position three-way solenoid valves (55) are fixedly connected to both sides of the bottom of the box (11), the second two-position three-way solenoid valves (55) correspond to the positions and numbers of the purification zones of the box (11), and the second two-position three-way solenoid valves (55) have an output end and two input ends, one of the input ends of the second two-position three-way solenoid valves (55) on the same side is connected to the shunt pipe (56) on the same side through a pipeline, the other input end of the second two-position three-way solenoid valve (55) is connected to the purification zone at the same position through a pipeline penetrating the box (11), and the output end of the second two-position three-way solenoid valve (55) is connected to the atmosphere.

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