Organic waste gas treatment device
By separately heating and desorbing the carbon layer inside the activated carbon tank, the problem of activated carbon's inability to desorb in the waste gas purification tower is solved, achieving efficient and environmentally friendly treatment of organic waste gas and reducing energy consumption.
Patent Information
- Application Number
- CN202310420686.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2023-04-19
- Publication Date
- 2026-01-06
- Estimated Expiration
- 2043-04-19
AI Technical Summary
Existing waste gas purification towers cannot desorb activated carbon layers, which makes it easy for activated carbon to generate secondary pollution during transportation. Furthermore, existing activated carbon tanks cannot be regenerated in situ after adsorption saturation.
An organic waste gas treatment device is designed. The carbon layer in the activated carbon tank is heated separately by an electric heater. Combined with a vacuum pump, a hot air circulation fan and a nitrogen source, the carbon layer is desorbed and regenerated. The desorbed gas is then treated by an oxidation device, achieving the goals of environmental protection and energy conservation.
It achieves efficient heating and desorption of carbon layer inside activated carbon canister, improves thermal efficiency, reduces energy consumption, avoids secondary pollution, and has the advantages of being environmentally friendly and energy-saving.
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Figure CN116328490B_ABST
Abstract
Description
Technical Field
[0001] This invention relates to the fields of chemical and environmental protection technology, and in particular to an organic waste gas treatment device. Background Technology
[0002] VOCs (volatile organic compounds) refer to organic compounds with a saturated vapor pressure greater than 133.32 Pa at room temperature and a boiling point between 50 and 260°C at normal pressure, or any volatile organic solid or liquid at normal temperature and pressure. Due to the high volatility of organic solvents, the vast majority will be converted into VOCs and emitted into the air.
[0003] Existing methods use exhaust gas purification towers to purify organic waste gas. These towers include packed towers, which are suitable for rapid and instantaneous absorption processes and are often used for gas purification. However, existing exhaust gas purification towers cannot desorb activated carbon layers.
[0004] The existing method of treating organic waste gas using activated carbon tanks consists of tanks filled with activated carbon. After the waste gas is adsorbed by the activated carbon tank, it is sent into the exhaust stack for discharge. It is impossible to regenerate in situ after the adsorption is saturated, and the activated carbon is prone to secondary pollution during the transfer process. Summary of the Invention
[0005] Therefore, the present invention provides an organic waste gas treatment device that can heat the carbon layer in the activated carbon tank separately, with high thermal efficiency and the advantages of energy saving, consumption reduction and environmental protection.
[0006] According to the technical solution provided by the present invention, the present invention provides an organic waste gas treatment device, including: a pretreatment device, activated carbon tank A, activated carbon tank B, nitrogen source, electric heater, main fan, hot circulation fan, vacuum pump, first condenser, oxidation device, pressure relief valve and second condenser.
[0007] The pretreatment device is connected to the air inlet A of activated carbon canister A and the air inlet B of activated carbon canister B, respectively.
[0008] The first end of the parallel connection of the hot circulating fan and the vacuum pump is connected in sequence to the first condenser and the filter device. The second end of the parallel connection of the hot circulating fan and the vacuum pump is connected in sequence to the pressure relief valve, the second condenser and the oxidation device. The third end of the parallel connection of the hot circulating fan and the vacuum pump is connected in sequence to the nitrogen source and the electric heater. The electric heater is connected to the air inlet A of the activated carbon canister A and the air inlet B of the activated carbon canister B, respectively.
[0009] The outlet A of the activated carbon canister A is connected to the outlet B of the activated carbon canister B.
[0010] The main fan is connected to the air outlet A of activated carbon tank A and the air outlet B of activated carbon tank B, respectively.
[0011] In one embodiment of the present invention, the activated carbon canister A includes at least a first carbon layer A and a second carbon layer A, the first carbon layer A and the second carbon layer A respectively form a first air outlet channel A and a second air outlet channel A with the side wall of the activated carbon canister A, and a first air inlet channel A is formed between the first carbon layer A and the second carbon layer A.
[0012] The air intake end A includes a first air intake end A disposed on the upper end of the first carbon layer A and a second air intake end A disposed on the upper end of the second carbon layer A;
[0013] The air outlet A includes a first air outlet A located at the lower end of the first air inlet channel A and a second air outlet A located at the lower end of the second air outlet channel A;
[0014] The air outlet A includes a first air outlet A located at the lower end of the first air outlet channel A and a second air outlet A located at the lower end of the second air outlet channel A;
[0015] The activated carbon canister B includes at least a first carbon layer B and a second carbon layer B. The first carbon layer B and the second carbon layer B form a first air outlet channel B and a second air outlet channel B with the side wall of the activated carbon canister B, respectively. A first air inlet channel B is formed between the first carbon layer B and the second carbon layer B.
[0016] The air intake end B includes a first air intake end B located on the upper end of the first carbon layer B and a second air intake end B located on the upper end of the second carbon layer B.
[0017] The air outlet B includes a first air outlet B located at the lower end of the first air inlet channel B and a second air outlet B located at the lower end of the second air outlet channel B;
[0018] The air outlet B includes a first air outlet B located at the lower end of the first air outlet channel B and a second air outlet B located at the lower end of the second air outlet channel B.
[0019] In one embodiment of the present invention, a first air inlet valve A is connected between the first air inlet end A and one end of the electric heater, a second air inlet valve A is connected between the second air inlet end A and one end of the electric heater, and the first air outlet end A and the second air outlet end A are connected to the main fan.
[0020] A first air inlet valve B is connected between the first air inlet end B and one end of the electric heater, and a second air inlet valve B is connected between the second air inlet end B and one end of the electric heater. The first air outlet end B and the second air outlet end B are connected to the main fan.
[0021] In one embodiment of the present invention, the first intake channel A is connected to a first pressure transmitter A and a first safety valve A, the second intake channel A is connected to a second pressure transmitter A and a second safety valve A, the second intake channel B is connected to a first pressure transmitter B and a first safety valve B, and the second intake channel B is connected to a second pressure transmitter B and a second safety valve B.
[0022] In one embodiment of the present invention, the first carbon layer A is connected to a first temperature transmitter A, the second carbon layer A is connected to a second temperature transmitter A, the first carbon layer B is connected to a first temperature transmitter B, and the second carbon layer B is connected to a second temperature transmitter B.
[0023] In one embodiment of the present invention, the first air outlet A is connected to a first emergency pressure relief valve A and a first air outlet valve A, the second air outlet A is connected to a second emergency pressure relief valve A and a second air outlet valve A, the first air outlet B is connected to a first emergency pressure relief valve B and a first air outlet valve B, and the second air outlet B is connected to a second emergency pressure relief valve B and a second air outlet valve B.
[0024] In one embodiment of the present invention, the first carbon layer A, the second carbon layer A, the first carbon layer B, and the second carbon layer B are all provided with nozzles.
[0025] In one embodiment of the present invention, an air inlet valve A is connected between the pretreatment device and the air inlet A, and an air inlet valve B is connected between the pretreatment device and the air inlet B.
[0026] In one embodiment of the present invention, the two ends of the heat circulation fan are respectively connected to a first valve and a second valve, the two ends of the vacuum pump are respectively connected to a third valve and a fourth valve, a fifth valve is provided between the third end of the heat circulation fan and the vacuum pump connected in parallel and the electric heater, the nitrogen source is connected to a nitrogen pipeline, and a nitrogen on / off valve is connected to the nitrogen pipeline.
[0027] In one embodiment of the present invention, the oxidation device is connected in parallel with a sixth valve, one end of the oxidation device is connected to the second condenser in sequence through a first flame arrester and a seventh valve, and the sixth valve and the other end of the oxidation device are connected to an exhaust gas treatment device through a second flame arrester.
[0028] The technical solution of the present invention has the following advantages compared with the prior art:
[0029] The organic waste gas treatment device of the present invention can heat the carbon layer in the activated carbon tank separately, with high thermal efficiency and the advantages of energy saving, consumption reduction and environmental protection. Attached Figure Description
[0030] To make the content of this invention easier to understand, the invention will be further described in detail below with reference to specific embodiments and accompanying drawings.
[0031] Figure 1 This is a schematic diagram of the organic waste gas treatment device of the present invention.
[0032] Figure 2 This is a schematic diagram of a carbon canister structure with one layer of carbon.
[0033] Figure 3 This is a schematic diagram of a carbon canister with three carbon layers.
[0034] Figure 4 This is a schematic diagram of four carbon canisters connected together; the carbon layer is not limited to one, two, or three layers, and theoretically can have 1+N layers; the carbon canisters are not limited to one, two, or three layers, and theoretically can have 1+N canisters.
[0035] Explanation of reference numerals on the accompanying drawings:
[0036] 1. Pretreatment device; 101. Spray tower; 102. Filter; 103. Demister; 100. Spray pipe; 110. Nozzle;
[0037] 2. Activated carbon canister A; 21. Air inlet A; 22a. First carbon layer A; 22b. Second carbon layer A; 23a. First air outlet channel A; 23b. Second air outlet channel A; 23c. First air inlet channel A; 24a. First air inlet A; 24b. Second air inlet A; 26a. First air outlet A; 26b. Second air outlet A; 27a. First air outlet A; 27b. Second air outlet A; 28a. First air inlet valve A; 8b. Second inlet valve A; 201a. First pressure transmitter A; 201b. Second pressure transmitter A; 202a. First safety valve A; 202b. Second safety valve A; 203a. First temperature transmitter A; 203b. Second temperature transmitter A; 204a. First emergency pressure relief valve A; 204b. Second emergency pressure relief valve A; 205a. First outlet valve A; 205b. Second outlet valve A; 206. Inlet valve A;
[0038] 3. Activated carbon canister B; 31. Air inlet B; 32a. First carbon layer B; 32b. Second carbon layer B; 33a. First air outlet channel B; 33b. Second air outlet channel B; 33c. Third air outlet channel B; 34a. First air inlet B; 34b. Second air inlet B; 36a. First air outlet B; 36b. Second air outlet B; 37a. First air outlet B; 37b. Second air outlet B; 38a. First air inlet valve B; 8b. Second inlet valve B; 301a. First pressure transmitter B; 301b. Second pressure transmitter B; 302a. First safety valve B; 302b. Second safety valve B; 303a. First temperature transmitter B; 303b. Second temperature transmitter B; 304a. First emergency pressure relief valve B; 304b. Second emergency pressure relief valve B; 305a. First outlet valve B; 305b. Second outlet valve B; 306. Inlet valve B;
[0039] 4. Nitrogen source; 5. Electric heater; 6. Main fan; 7. Hot air circulation fan; 8. Vacuum pump; 9. First condenser; 10. Oxidation unit; 11. Pressure relief valve; 12. Second condenser; 13. Exhaust gas treatment unit; 14. Filtration unit
[0040] 411. First valve; 412. Second valve; 413. Third valve; 414. Fourth valve; 415. Fifth valve; 416. Sixth valve; 417. Seventh valve; 418. Nitrogen on / off valve; 419. First flame arrester; 420. Second flame arrester. Detailed Implementation
[0041] The present invention will be further described below with reference to the accompanying drawings and specific embodiments, so that those skilled in the art can better understand and implement the present invention. However, the embodiments described are not intended to limit the present invention.
[0042] In this invention, when directions (up, down, left, right, front, and back) are described, it is only for the convenience of describing the technical solution of this invention, and does not indicate or imply that the technical features referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, it should not be construed as a limitation of this invention.
[0043] In this invention, "several" means one or more, "multiple" means two or more, "greater than," "less than," "exceeding," etc., are understood to exclude the stated number; "above," "below," "within," etc., are understood to include the stated number. In the description of this invention, the terms "first" and "second" are used only to distinguish technical features and should not be construed as indicating or implying relative importance, or implicitly indicating the number of indicated technical features, or implicitly indicating the order of the indicated technical features.
[0044] In this invention, unless otherwise explicitly defined, the terms "setting," "installing," and "connecting" should be interpreted broadly. For example, they can refer to a direct connection or an indirect connection through an intermediate medium; a fixed connection, a detachable connection, or an integrally formed connection; a mechanical connection, an electrical connection, or a connection capable of mutual communication; or the internal connection of two components or the interaction between two components. Those skilled in the art can reasonably determine the specific meaning of the above terms in this invention based on the specific content of the technical solution.
[0045] Reference Figure 1 As shown, an organic waste gas treatment device of the present invention includes: a pretreatment device 1, an activated carbon tank A2, an activated carbon tank B3, a nitrogen source 4, an electric heater 5, a main fan 6, a hot circulation fan 7, a vacuum pump 8, a first condenser 9, an oxidation device 10, a pressure relief valve 11, and a second condenser 12.
[0046] The pretreatment device 1 is connected to the air inlet A21 of the activated carbon canister A2 and the air inlet B31 of the activated carbon canister B3, respectively.
[0047] The first end of the parallel connection of the hot circulating fan 7 and the vacuum pump 8 is connected in sequence to the first condenser 9 and the filter device. The second end of the parallel connection of the hot circulating fan 7 and the vacuum pump 8 is connected in sequence to the pressure relief valve 11, the second condenser 12 and the oxidation device 10. The third end of the parallel connection of the hot circulating fan 7 and the vacuum pump 8 is connected in sequence to the nitrogen source 4 and the electric heater 5. The electric heater 5 is connected to the air inlet A of the activated carbon canister A2 and the air inlet B of the activated carbon canister B3, respectively.
[0048] The outlet A of the activated carbon canister A2 is connected to the outlet B of the activated carbon canister B3.
[0049] The main fan 6 is connected to the air outlet A of activated carbon tank A2 and the air outlet B of activated carbon tank B3, respectively.
[0050] Specifically, the pretreatment device 1 includes a spray tower 101, a filter 102, and a demister 103 connected in sequence; the activated carbon tank A2 includes at least a first carbon layer A22a and a second carbon layer A22b, the first carbon layer A22a and the second carbon layer A22b forming a first air outlet channel A23a and a second air outlet channel A23b with the side wall of the activated carbon tank A2, respectively, and a first air inlet channel A23c is formed between the first carbon layer A22a and the second carbon layer A22b; the air inlet end A includes a first air inlet end A24a located above the first carbon layer A22a and a second air inlet end A24b located above the second carbon layer A22b; the air outlet end A includes a first air outlet end A26a located below the first air inlet channel A23c and a second air outlet end A26b located below the second air outlet channel A23b; the air outlet end A includes a first air outlet end A27a located below the first air outlet channel A23a and a second air outlet end A26b located below the second air outlet channel A23b. The second air outlet A27b is located at the lower end of the air duct A23b; the activated carbon canister B3 includes at least a first carbon layer B32a and a second carbon layer B32b, the first carbon layer B32a and the second carbon layer B32b respectively form a first air outlet duct B33a and a second air outlet duct B33b with the side wall of the activated carbon canister B3, and a first air inlet duct B33c is formed between the first carbon layer B32a and the second carbon layer B32b; the air inlet B includes a portion disposed on the first carbon layer B32a. The first air inlet B34a is located at the upper end of 2a, and the second air inlet B34b is located at the upper end of the second carbon layer B32b; the air outlet B includes a first air outlet B36a located at the lower end of the first air inlet channel B33c and a second air outlet B36b located at the lower end of the second air outlet channel B33b; the air outlet B includes a first air outlet B37a located at the lower end of the first air outlet channel B33a and a second air outlet B37b located at the lower end of the second air outlet channel B33b. In this embodiment, the number of activated carbon canisters and their internal carbon layers can be set as needed. Each carbon layer is provided with a nozzle 100, and the nozzle 100 is distributed with nozzles 110. For example... Figures 2 to 4 As shown.
[0051] Specifically, a first intake valve A28a is connected between the first intake end A24a and one end of the electric heater 5, and a second intake valve A28b is connected between the second intake end A24b and one end of the electric heater 5. The first air outlet end A27a and the second air outlet end A27b are connected to the main fan 6. A first intake valve B38a is connected between the first intake end B34a and one end of the electric heater 5, and a second intake valve B38b is connected between the second intake end B34b and one end of the electric heater 5. The first air outlet end B37a and the second air outlet end B37b are connected to the main fan 6.
[0052] Specifically, the first air outlet channel A23a is connected to the first pressure transmitter A201a and the first safety valve A202a, the second air outlet channel A23b is connected to the second pressure transmitter A201b and the second safety valve A202b, the second air outlet channel B33b is connected to the first pressure transmitter B301a and the first safety valve B302a, and the second air outlet channel B33b is connected to the second pressure transmitter B301b and the second safety valve B302b.
[0053] Specifically, the first carbon layer A22a is connected to a first temperature transmitter A203a, the second carbon layer A22b is connected to a second temperature transmitter A203b, the first carbon layer B32a is connected to a first temperature transmitter B303a, and the second carbon layer B32b is connected to a second temperature transmitter B303b.
[0054] Specifically, the first air outlet A26a is connected to a first emergency pressure relief valve A204a and a first air outlet valve A205a, the second air outlet A26b is connected to a second emergency pressure relief valve A204b and a second air outlet valve A205b, the first air outlet B36a is connected to a first emergency pressure relief valve B304a and a first air outlet valve B305a, and the second air outlet B36b is connected to a second emergency pressure relief valve B304b and a second air outlet valve B305b.
[0055] Specifically, the first carbon layer A22a, the second carbon layer A22b, the first carbon layer B32a, and the second carbon layer B32b are all provided with nozzles 100.
[0056] Specifically, an air inlet valve A206 is connected between the pretreatment device 1 and the air inlet end A21, and an air inlet valve B306 is connected between the pretreatment device 1 and the air inlet end B31.
[0057] Specifically, the two ends of the heat circulation fan 7 are respectively connected to a first valve and a second valve 412, the two ends of the vacuum pump 8 are respectively connected to a third valve 413 and a fourth valve 414, a fifth valve 415 is provided between the third end of the heat circulation fan 7 and the vacuum pump 8 connected in parallel and the electric heater 5, the nitrogen source 4 is connected to a nitrogen pipeline, and a nitrogen on / off valve 418 is connected to the nitrogen pipeline.
[0058] Specifically, the oxidation device 10 is connected in parallel with a sixth valve 416. One end of the oxidation device 10 is connected to the second condenser 12 in sequence through a first flame arrester 419 and a seventh valve 417. The other end of the oxidation device 10 and the sixth valve 416 are connected to a tail gas treatment device 13 through a second flame arrester 420.
[0059] Working process: After activated carbon tank A2 reaches adsorption saturation, the process switches to activated carbon tank B3 for adsorption; the corresponding valve is opened and vacuum pump 8 is started to deoxygenate activated carbon tank A2. Once the oxygen content reaches the required level, vacuum pump 8 is turned off and all open valves are closed.
[0060] Open the nitrogen on / off valve 418 to purge the activated carbon tank A2 with nitrogen. After completion, close the nitrogen on / off valve 418, start the hot air circulation fan 7 and the electric heater 5, and perform heat desorption treatment on the first carbon layer A22a.
[0061] When the oxidation device 10 is started, the gas desorbed from the activated carbon tank A2 is depressurized by the pressure relief valve 11. The depressurized gas is oxidized by the oxidation device 10. The oxidized gas is then reabsorbed by the activated carbon tank B3 through the pretreatment device 1 and discharged in compliance with the standards.
[0062] Once the first carbon layer A22a reaches the specified temperature, the second carbon layer A22b undergoes a heating and desorption process. The desorbed gas is released through the pressure relief valve 11, and then oxidized by the oxidation device 10. The oxidized gas is then reabsorbed by the activated carbon tank B3 through the pretreatment device 1 and discharged in compliance with standards. This process, by heating the carbon layers within the carbon tank separately, features a small installed capacity and relatively high thermal efficiency, offering advantages in energy saving and consumption reduction.
[0063] Finally, it should be noted that the above specific embodiments are only used to illustrate the technical solutions of the present invention and not to limit it. Although the present invention has been described in detail with reference to examples, those skilled in the art should understand that modifications or equivalent substitutions can be made to the technical solutions of the present invention without departing from the spirit and scope of the technical solutions of the present invention, and all such modifications or substitutions should be covered within the scope of the claims of the present invention.
Claims
1. An organic waste gas treatment device, characterized in that, The application relates to a device for treating waste gas, which comprises: a pretreatment device (1), an activated carbon tank A (2), an activated carbon tank B (3), a nitrogen source (4), an electric heater (5), a main fan (6), a heat circulation fan (7), a vacuum pump (8), a first condenser (9), an oxidation device (10), a pressure relief valve (11) and a second condenser (12); the pretreatment device (1) is connected with an air inlet end A (21) of the activated carbon tank A (2) and an air inlet end B (31) of the activated carbon tank B (3) respectively; a first end of the heat circulation fan (7) and the vacuum pump (8) connected in parallel is connected with the first condenser (9), a filtering device, a second end of the heat circulation fan (7) and the vacuum pump (8) connected in parallel is connected with the pressure relief valve (11), the second condenser (12) and the oxidation device (10) in sequence, a third end of the heat circulation fan (7) and the vacuum pump (8) connected in parallel is connected with the nitrogen source (4) and the electric heater (5) in sequence, and the electric heater (5) is connected with an air inlet end A (24a, 24b) of the activated carbon tank A (2) and an air inlet end B (34a, 34b) of the activated carbon tank B (3) respectively; an air outlet end A (26a, 26b) of the activated carbon tank A (2) is connected with an air outlet end B (36a, 33b) of the activated carbon tank B (3); the main fan (6) is connected with an air outlet end A (27a, 27b) of the activated carbon tank A (2) and an air outlet end B (37a, 37b) of the activated carbon tank B (3) respectively; the activated carbon tank A (2) comprises at least a first carbon layer A (22a) and a second carbon layer A (22b), the first carbon layer A (22a) and the second carbon layer A (22b) form a first air outlet channel A (23a) and a second air outlet channel A (23b) with the side wall of the activated carbon tank A (2) respectively, and a first air inlet channel A (23c) is formed between the first carbon layer A (22a) and the second carbon layer A (22b); the air inlet end A comprises a first air inlet end A (24a) arranged at the upper end of the first carbon layer A (22a) and a second air inlet end A (24b) arranged at the upper end of the second carbon layer A (22b); the air outlet end A (26a, 26b) comprises a first air outlet end A (26a) arranged at the lower end of the first air inlet channel A (23c) and a second air outlet end A (26b) arranged at the lower end of the second air outlet channel A (23b); the air outlet end A (27a, 27b) comprises a first air outlet end A (27a) arranged at the lower end of the first air outlet channel A (23a) and a second air outlet end A (27b) arranged at the lower end of the second air outlet channel A (23b); the activated carbon tank B (3) comprises at least a first carbon layer B (32a) and a second carbon layer B (32b), the first carbon layer B (32a) and the second carbon layer B (32b) form a first air outlet channel B (33a) and a second air outlet channel B (33b) with the side wall of the activated carbon tank B (3) respectively, and a first air inlet channel B (33c) is formed between the first carbon layer B (32a) and the second carbon layer B (32b). The air inlet end B includes a first air inlet end B (34a) arranged on the upper end of the first carbon layer B (32a) and a second air inlet end B (34b) arranged on the upper end of the second carbon layer B (32b); The air outlet end B includes a first air outlet end B (36a) arranged on the lower end of the first air inlet channel B (33c) and a second air outlet end B (36b) arranged on the lower end of the second air outlet channel B (33b); The air outlet end B includes a first air outlet end B (36a) arranged on the lower end of the first air inlet channel B (33c) and a second air outlet end B (36b) arranged on the lower end of the second air outlet channel B (33b); The first carbon layer A (22a), the second carbon layer A (22b), the first carbon layer B (32a) and the second carbon layer B (32b) are all provided with a nozzle (100).
2. The organic waste treatment apparatus according to claim 1, wherein The first air inlet end A (24a) and one end of the electric heater (5) are connected by a first air inlet valve A (28a), the second air inlet end A (24b) and one end of the electric heater (5) are connected by a second air inlet valve A (28b), and the first air outlet end A (27a) and the second air outlet end A (27b) are connected with the main fan (6); The first air inlet end B (34a) and one end of the electric heater (5) are connected by a first air inlet valve B (38a), the second air inlet end B (34b) and one end of the electric heater (5) are connected by a second air inlet valve B (38b), and the first air outlet end B (37a) and the second air outlet end B (37b) are connected with the main fan (6).
3. The organic waste treatment device of claim 1, wherein The first air outlet channel A (23a) is connected with a first pressure transmitter A (201a) and a first safety valve A (202a), the second air outlet channel A (23b) is connected with a second pressure transmitter A (201b) and a second safety valve A (202b), the first air outlet channel B (33a) is connected with a first pressure transmitter B (301a) and a first safety valve B (302a), and the second air outlet channel B (33b) is connected with a second pressure transmitter B (301b) and a second safety valve B (302b).
4. The organic waste treatment apparatus of claim 1, wherein The first carbon layer A (22a) is connected with a first temperature transmitter A (203a), the second carbon layer A (22b) is connected with a second temperature transmitter A (203b), the first carbon layer B (32a) is connected with a first temperature transmitter B (303a), and the second carbon layer B (32b) is connected with a second temperature transmitter B (303b).
5. The organic waste treatment device of claim 1, wherein The first air outlet end A (26a) is connected with a first emergency pressure relief valve A (204a) and a first air outlet valve A (205a), the second air outlet end A (26b) is connected with a second emergency pressure relief valve A (204b) and a second air outlet valve A (205b), the first air outlet end B (36a) is connected with a first emergency pressure relief valve B (304a) and a first air outlet valve B (305a), and the second air outlet end B (36b) is connected with a second emergency pressure relief valve B (304b) and a second air outlet valve B (305b).
6. The organic waste treatment device of claim 1, wherein The front treatment device (1) is connected with an air inlet valve A (206) between an air inlet end A (21), and is connected with an air inlet valve B (306) between an air inlet end B (31).
7. The organic waste treatment apparatus of claim 1, wherein The heat circulation fan (7) is connected with a first valve and a second valve (412) at two ends, the vacuum pump (8) is connected with a third valve (413) and a fourth valve (414) at two ends, a fifth valve (415) is arranged between the third end of the heat circulation fan (7) and the vacuum pump (8) in parallel and the electric heater (5), the nitrogen source (4) is connected with a nitrogen pipeline, and the nitrogen pipeline is connected with a nitrogen on-off valve (418).
8. The organic waste treatment apparatus of claim 1, wherein The oxidation device (10) is connected with a sixth valve (416) in parallel, one end of the oxidation device (10) is connected with the second condenser (12) through a first fire arrester (419) and a seventh valve (417) in sequence, and the sixth valve (416) and the other end of the oxidation device (10) are connected with a tail gas treatment device (13) through a second fire arrester (420).
Citation Information
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