An integrated absorption and oxidation device

Abstract

The present invention relates to the technical field of absorption and oxidation equipment, and specifically discloses an integrated absorption and oxidation equipment, including an oxidation tank body. A partition is provided on the inner wall of the oxidation tank body. The oxidation tank body is separated by the partition into an absorption zone and an oxidation zone which are distributed vertically. The partition penetrates and fixedly installs an exchange pipe, and the exchange pipe is used to connect the absorption zone and the oxidation zone. A ammonia inlet pipe for conveying ammonia to the absorption zone is provided at the top of the oxidation tank body. A baffle is arranged in the absorption zone, and the baffle and the side wall of the oxidation tank body enclose an ammonia addition area, and the ammonia inlet pipe matches the ammonia addition area. By setting a partition structure in the oxidation tank, the present invention simplifies the ammonia addition structure in the absorption zone, saves floor space, has an automatic simplified type liquid level balance device, ensures component stratification, reduces the failure rate, and improves the oxidation desulfurization efficiency of the desulfurization absorption liquid.

Description

Technical Field

[0001] The present invention relates to the technical field of absorption and oxidation equipment, and particularly relates to an integrated absorption and oxidation equipment. Background Art

[0002] The ammonia desulfurization tower is a device used for flue gas treatment, mainly used to remove sulfur dioxide in the flue gas. This technology uses ammonia or aqueous ammonia as an absorbent to react with sulfur dioxide in the flue gas to generate ammonium sulfite and ammonium sulfate, thereby achieving the purpose of desulfurization. Among them, the oxidation tank used in the desulfurization tower is mainly used for the regeneration treatment of the desulfurization liquid. Through the oxidation reaction, the reduced sulfide in the desulfurization liquid is converted into elemental sulfur, and the activity of the catalyst is restored. The oxidation tank is usually located outside the desulfurization tower, receives the rich liquid discharged from the bottom of the desulfurization tower, sucks in the oxidation air through a ejector, makes the gas-liquid fully contact, and completes the oxidation regeneration process.

[0003] Currently, during the use of the ammonia desulfurization oxidation circulation tank, since the desulfurization and oxidation of the desulfurization absorbent are generally carried out by using an internal barrel-shaped ammonia feeder, small compartments, and a separate external ammonia tank, the external ammonia tank has problems such as large floor space and the need to control the exchange and distribution. The internal ammonia feeder is prone to problems such as high failure rate of the oxidation tank, large construction volume, and large vibration. Summary of the Invention

[0004] To solve the above problems existing in the prior art, the present invention provides an integrated absorption and oxidation equipment, which can solve the problems proposed in the above background art.

[0005] The object of the present invention can be achieved by the following technical solutions:

[0006] An integrated absorption and oxidation equipment, comprising:

[0007] An oxidation tank main body, a partition is provided on the inner wall of the oxidation tank main body, and the oxidation tank main body is divided into an upper and lower distributed absorption area and oxidation area by the partition. The partition penetrates and is fixedly installed with an exchange pipe, and the exchange pipe is used to connect the absorption area and the oxidation area. A feed ammonia pipe for conveying ammonia to the absorption area is provided at the top of the oxidation tank main body. A baffle is provided in the absorption area, and the baffle and the side wall of the oxidation tank main body enclose an ammonia addition area, and the feed ammonia pipe matches the ammonia addition area;

[0008] A feed liquid pipe, which is installed on the side wall of the oxidation tank main body;

[0009] A liquid outlet assembly, the liquid outlet assembly includes a first liquid outlet and a second liquid outlet. The first liquid outlet is installed on the side wall of the oxidation tank main body, the second liquid outlet is installed on the side wall of the oxidation tank main body, and the second liquid outlet is communicated with the oxidation area;

[0010] An oxidation air delivery assembly, the oxidation air delivery assembly includes an inlet pipe which penetrates and is fixedly installed on the side wall of the oxidation tank main body, one end of the inlet pipe away from the oxidation tank main body is connected to an oxidation blower through a flange, and an exhaust assembly for discharging excess oxidation air is arranged in the oxidation area of the oxidation tank main body;

[0011] A distributor which is installed in the oxidation area of the oxidation tank main body;

[0012] A liquid level sensing assembly.

[0013] Preferably, the ammonia inlet pipe penetrates and is fixedly installed at the top of the oxidation tank main body, the ammonia inlet pipe is communicated with the absorption area, the baffle is bent, the bottom end of the baffle is fixedly connected to the top end of the partition plate, and the top end of the baffle is lower than the top end of the exchange pipe.

[0014] Preferably, the exhaust assembly includes an exhaust pipe which penetrates and is installed on the side wall of the oxidation tank main body, the exhaust pipe is higher than the bottom end of the exchange pipe, and a third solenoid valve is arranged on the side wall of the exhaust pipe.

[0015] Preferably, a support assembly which is used to support the oxidation tank main body, the support assembly includes three support feet which are fixedly installed at the bottom end of the oxidation tank main body, and a cross bar is fixedly installed between the plurality of support feet.

[0016] Preferably, the liquid inlet pipe is communicated with the absorption area, a first pump body is arranged on the side wall of the liquid inlet pipe, and a first solenoid valve is arranged on the side wall of the liquid inlet pipe.

[0017] Preferably, the first liquid outlet is communicated with the absorption area, one end of the first liquid outlet away from the oxidation tank main body is connected to a first liquid outlet pipe through a flange, the first liquid outlet pipe is used to transport liquid to the desulfurization tower, a main absorption pump is arranged on the side wall of the first liquid outlet pipe, and a main solenoid valve is arranged on the side wall of the first liquid outlet pipe.

[0018] Preferably, one end of the second liquid outlet away from the oxidation tank main body is connected to a second liquid outlet pipe through a flange, the second liquid outlet pipe is used to transport liquid to the desulfurization tower, a secondary absorption pump is arranged on the side wall of the second liquid outlet pipe, and a secondary solenoid valve is arranged on the side wall of the second liquid outlet pipe.

[0019] Preferably, the inlet pipe is matched with the oxidation area, a flow meter is arranged on the side wall of the inlet pipe, and a second solenoid valve is arranged on the side wall of the inlet pipe.

[0020] Preferably, a square groove is provided at the bottom end of the distributor. The square groove is arranged in parallel with the intake pipe. One end of the intake pipe located inside the oxidation tank body is located in the square groove. A plurality of annular grooves are provided at the bottom end of the square groove. The plurality of annular grooves are located at the same horizontal height and are coaxially arranged. The outer diameters of the plurality of annular grooves are arranged to increase at equal intervals. A plurality of air holes are provided on the top walls of the plurality of annular grooves.

[0021] Preferably, the liquid level sensing assembly includes a first liquid level sensor and a second liquid level sensor. The first liquid level sensor is installed at the top end of the oxidation tank body and is used to monitor the liquid level in the absorption area. The second liquid level sensor is installed at the bottom end of the oxidation tank body and is used to monitor the liquid level in the oxidation area. The second liquid level sensor is arranged to penetrate through the distributor.

[0022] The beneficial effects of the present invention are as follows:

[0023] 1. By providing a liquid outlet assembly and an oxidation air delivery assembly, the beneficial effects that can be obtained are as follows: a partition plate is provided on the inner wall of the oxidation tank body. The oxidation tank body is separated into an upper and lower distributed absorption area and oxidation area by the partition plate. The partition plate is penetrated and fixedly installed with an exchange pipe for communicating the absorption area and the oxidation area. An ammonia inlet pipe for delivering ammonia to the absorption area is provided at the top end of the oxidation tank body. A baffle is provided in the absorption area. The baffle and the side wall of the oxidation tank body enclose an ammonia addition area. The ammonia inlet pipe is matched with the ammonia addition area;

[0024] The liquid inlet pipe, in cooperation with the first pump body and the first solenoid valve, pumps the desulfurization absorption liquid in the desulfurization tower into the absorption area of the oxidation tank body. The desulfurization absorption liquid in the absorption area flows into the oxidation area through the exchange pipe. The liquid level of the desulfurization absorption liquid in the oxidation area is higher than the bottom end of the exchange pipe, and the liquid level of the desulfurization absorption liquid in the absorption area is higher than the top end of the exchange pipe. The first liquid outlet, the first liquid outlet pipe, in cooperation with the main absorption pump and the main solenoid valve, pump the desulfurization absorption liquid in the absorption area into the desulfurization tower. The second liquid outlet, the second liquid outlet pipe, in cooperation with the auxiliary absorption pump and the auxiliary solenoid valve, pump the desulfurization absorption liquid in the oxidation area into the desulfurization tower. A cycle is established between the oxidation tank body and the desulfurization tower to ensure that the desulfurization absorption liquid continuously circulates in the system, and at the same time, replenish the concentrated section of the desulfurization tower to ensure the stable operation of the system. By setting a partitioned structure in the oxidation tank, the ammonia addition structure in the absorption area is simplified, the floor area is saved, and an automatic simplified liquid level balancing device is provided, ensuring component stratification and reducing the failure rate.

[0025] 2. By providing a distributor, the beneficial effects that can be obtained are as follows: a square groove is provided at the bottom end of the distributor. The square groove is arranged in parallel with the intake pipe. One end of the intake pipe located inside the oxidation tank body is located in the square groove. A plurality of annular grooves are provided at the bottom end of the square groove. The plurality of annular grooves are located at the same horizontal height and are coaxially arranged. The outer diameters of the plurality of annular grooves are arranged to increase at equal intervals. A plurality of air holes are provided on the top walls of the plurality of annular grooves;

[0026] The oxidation blower, intake pipe, flowmeter, and second solenoid valve cooperate to introduce oxidation air into the oxidation zone of the oxidation tank main body. The oxidation air first flows into the square tank, then enters multiple annular tanks, and finally flows into the desulfurization absorption liquid in the oxidation zone through multiple air holes. The gas-liquid two-phase fully contacts under the state of high-speed turbulence to carry out the oxidation regeneration reaction, increasing the gas-liquid contact area and prolonging the air residence time, thereby improving the oxidation desulfurization efficiency of the desulfurization absorption liquid. Description of the Drawings

[0027] For the convenience of those skilled in the art to understand, the present invention will be further described below in conjunction with the drawings.

[0028] Figure 1 Schematic diagram of the overall structure of the present invention;

[0029] Figure 2 Installation structure diagram of the baffle and partition in the present invention;

[0030] Figure 3 Cross-sectional view of the present invention;

[0031] Figure 4 Installation structure diagram of the distributor in the present invention;

[0032] Figure 5 Installation structure diagram of the annular tank and air holes in the present invention;

[0033] Figure 6 Bottom view of the distributor in the present invention.

[0034] Explanation of the reference numerals in the drawings:

[0035] In the figure: 1. Oxidation tank main body; 11. Partition; 12. Absorption zone; 13. Oxidation zone; 14. Exchange pipe; 15. Ammonia inlet pipe; 16. Baffle; 21. Support feet; 22. Cross bar; 31. Liquid inlet pipe; 32. First pump body; 33. First solenoid valve; 41. First liquid outlet; 42. First liquid outlet pipe; 43. Main absorption pump; 44. Main solenoid valve; 45. Second liquid outlet; 46. Second liquid outlet pipe; 47. Sub-absorption pump; 48. Sub-solenoid valve; 51. Intake pipe; 52. Flowmeter; 53. Second solenoid valve; 54. Oxidation blower; 55. Exhaust pipe; 56. Third solenoid valve; 6. Distributor; 61. Square tank; 62. Annular tank; 63. Air holes; 71. First liquid level sensor; 72. Second liquid level sensor. Detailed Embodiments

[0036] To further elaborate on the technical means and effects adopted by the present invention to achieve the predetermined invention purpose, the following clearly and completely describes the specific implementation manners, structures, features and their effects of the present invention in conjunction with the accompanying drawings and preferred embodiments. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. All other embodiments obtained by those of ordinary skill in the art based on the embodiments of the present invention without creative efforts belong to the scope of protection of the present invention.

[0037] In the description of the present application, it should be understood that the orientation or positional relationship indicated by terms such as "inside", "outside", etc. is based on the orientation or position shown in the drawings. It is only for the convenience of describing the present application and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, a specific orientation structure and operation. Therefore, it should not be construed as a limitation to the present application.

[0038] Referring to Figures 1-6 , an integrated absorption and oxidation device disclosed by the present invention includes an oxidation tank main body 1. A partition 11 is provided on the inner wall of the oxidation tank main body 1. The oxidation tank main body 1 is divided into an absorption area 12 and an oxidation area 13 which are distributed up and down by the partition 11. The partition 11 penetrates and fixedly installs an exchange pipe 14. The exchange pipe 14 is used to connect the absorption area 12 and the oxidation area 13. A ammonia inlet pipe 15 for delivering ammonia to the absorption area 12 is provided at the top end of the oxidation tank main body 1. The ammonia inlet pipe 15 penetrates and is fixedly installed at the top end of the oxidation tank main body 1. The ammonia inlet pipe 15 is communicated with the absorption area 12. A baffle 16 is provided in the absorption area 12. The baffle 16 is bent. The bottom end of the baffle 16 is fixedly connected to the top end of the partition 11. The top end of the baffle 16 is lower than the top end of the exchange pipe 14. The baffle 16 and the side wall of the oxidation tank main body 1 enclose an ammonia addition area. The ammonia inlet pipe 15 matches the ammonia addition area;

[0039] A support assembly for supporting the oxidation tank main body 1. The support assembly includes three support feet 21. The support feet 21 are fixedly installed at the bottom end of the oxidation tank main body 1. A cross bar 22 is fixedly installed between the multiple support feet 21;

[0040] A liquid inlet pipe 31 is installed on the side wall of the oxidation tank main body 1. The liquid inlet pipe 31 is communicated with the absorption area 12. A first pump body 32 is provided on the side wall of the liquid inlet pipe 31. A first solenoid valve 33 is provided on the side wall of the liquid inlet pipe 31;

[0041] Liquid outlet assembly. The liquid outlet assembly includes a first liquid outlet 41 and a second liquid outlet 45. The first liquid outlet 41 is installed on the side wall of the oxidation tank body 1. The first liquid outlet 41 is communicated with the absorption area 12. One end of the first liquid outlet 41 away from the oxidation tank body 1 is connected with a first liquid outlet pipe 42 through a flange. The first liquid outlet pipe 42 is used to transport liquid to the desulfurization tower. A main absorption pump 43 is arranged on the side wall of the first liquid outlet pipe 42. A main solenoid valve 44 is arranged on the side wall of the first liquid outlet pipe 42. The second liquid outlet 45 is installed on the side wall of the oxidation tank body 1. The second liquid outlet 45 is communicated with the oxidation area 13. One end of the second liquid outlet 45 away from the oxidation tank body 1 is connected with a second liquid outlet pipe 46 through a flange. The second liquid outlet pipe 46 is used to transport liquid to the desulfurization tower. A sub-absorption pump 47 is arranged on the side wall of the second liquid outlet pipe 46. A sub-solenoid valve 48 is arranged on the side wall of the second liquid outlet pipe 46;

[0042] Oxidation air delivery assembly. The oxidation air delivery assembly includes an air inlet pipe 51. The air inlet pipe 51 penetrates and is fixedly installed on the side wall of the oxidation tank body 1. The air inlet pipe 51 is matched with the oxidation area 13. A flow meter 52 is arranged on the side wall of the air inlet pipe 51. A second solenoid valve 53 is arranged on the side wall of the air inlet pipe 51. One end of the air inlet pipe 51 away from the oxidation tank body 1 is connected with an oxidation blower 54 through a flange. An exhaust assembly for discharging excess oxidation air is arranged in the oxidation area 13 of the oxidation tank body 1. The exhaust assembly includes an exhaust pipe 55. The exhaust pipe 55 penetrates and is installed on the side wall of the oxidation tank body 1. The exhaust pipe 55 is higher than the bottom end of the exchange pipe 14. A third solenoid valve 56 is arranged on the side wall of the exhaust pipe 55;

[0043] Distributor 6. The distributor 6 is installed in the oxidation area 13 of the oxidation tank body 1. A square groove 61 is arranged at the bottom end of the distributor 6. The square groove 61 is arranged in parallel with the air inlet pipe 51. One end of the air inlet pipe 51 located inside the oxidation tank body 1 is located inside the square groove 61. A plurality of annular grooves 62 are arranged at the bottom end of the square groove 61. The plurality of annular grooves 62 are located at the same horizontal height and are coaxially arranged. The outer diameters of the plurality of annular grooves 62 are increased at equal intervals. A plurality of air holes 63 are arranged on the top walls of the plurality of annular grooves 62;

[0044] Liquid level sensing assembly. The liquid level sensing assembly includes a first liquid level sensor 71 and a second liquid level sensor 72. The first liquid level sensor 71 is installed at the top end of the oxidation tank body 1. The first liquid level sensor 71 is used to monitor the liquid level of the absorption area 12. The second liquid level sensor 72 is installed at the bottom end of the oxidation tank body 1. The second liquid level sensor 72 is used to monitor the liquid level of the oxidation area 13. The second liquid level sensor 72 is arranged in a penetrating manner with the distributor 6.

[0045] Working principle and usage process of the present invention: The liquid inlet pipe 31, in cooperation with the first pump body 32 and the first solenoid valve 33, pumps the desulfurization absorption liquid in the desulfurization tower into the absorption area 12 of the oxidation tank main body 1. The desulfurization absorption liquid in the absorption area 12 flows into the oxidation area 13 through the exchange pipe 14. The liquid level of the desulfurization absorption liquid in the oxidation area 13 is higher than the bottom end of the exchange pipe 14, and the liquid level of the desulfurization absorption liquid in the absorption area 12 is higher than the top end of the exchange pipe 14. The first liquid outlet 41 and the first liquid outlet pipe 42, in cooperation with the main absorption pump 43 and the main solenoid valve 44, pump the desulfurization absorption liquid in the absorption area 12 into the desulfurization tower. The second liquid outlet 45 and the second liquid outlet pipe 46, in cooperation with the auxiliary absorption pump 47 and the auxiliary solenoid valve 48, pump the desulfurization absorption liquid in the oxidation area 13 into the desulfurization tower. A cycle is established between the oxidation tank main body 1 and the desulfurization tower to ensure that the desulfurization absorption liquid continuously circulates in the system, while replenishing the concentrated section of the desulfurization tower to ensure the stable operation of the system. At the same time, the oxidation blower 54 and the air inlet pipe 51, in cooperation with the flow meter 52 and the second solenoid valve 53, introduce oxidation air into the oxidation area 13 of the oxidation tank main body 1. The oxidation air first flows into the square tank 61, then enters a plurality of annular tanks 62, and finally flows into the desulfurization absorption liquid in the oxidation area 13 through a plurality of air holes 63. The gas-liquid two phases are in full contact under the state of high-speed turbulence to carry out the oxidation regeneration reaction, increasing the gas-liquid contact area and prolonging the air residence time. Ammonia water is the absorbent for ammonia-based desulfurization. The ammonia water enters the absorption area 12 from the ammonia inlet pipe 15 to absorb sulfur dioxide in the desulfurization absorption liquid. The desulfurization absorption liquid in the absorption area 12 and the desulfurization absorption liquid in the oxidation area 13 are exchanged through the exchange pipe 14. The excess oxidation air is discharged from the oxidation area 13 through the exhaust pipe 55 and the third solenoid valve 56. By combining physical partitioning and chemical partitioning, the component stratification is ensured.

[0046] Refer to Figure 3, the intake pipe 51 and the oxidation blower 54 cooperate with the second solenoid valve 53 to deliver gas to the oxidation zone 13. The oxidation air is discharged from the oxidation zone 13 through the exhaust pipe 55 and the third solenoid valve 56 to maintain the air pressure in the oxidation zone 13. When the liquid level of the desulfurization liquid in the oxidation zone 13 drops, the air pressure in the oxidation zone 13 decreases, and the pressure difference between the oxidation zone 13 and the absorption zone 12 increases, driving the desulfurization liquid in the absorption zone 12 to flow into the oxidation zone 13. The liquid inlet pipe 31 and the first pump body 32 cooperate with the first solenoid valve 33 to drain the desulfurization liquid into the absorption zone 12 at a set flow rate. The first liquid outlet 41, the first liquid outlet pipe 42 cooperate with the main absorption pump 43 and the main solenoid valve 44 to drain the desulfurization absorption liquid in the absorption zone 12 to the desulfurization tower at a set flow rate to maintain the liquid level of the desulfurization liquid in the absorption zone 12. The excess oxidation air is discharged from the oxidation zone 13 through the exhaust pipe 55 and the third solenoid valve 56. The intake pipe 51 and the oxidation blower 54 cooperate with the second solenoid valve 53 to deliver gas to the oxidation zone 13 to maintain the air pressure in the oxidation zone 13. The second liquid outlet 45, the second liquid outlet pipe 46 cooperate with the auxiliary absorption pump 47 and the auxiliary solenoid valve 48 to drain the desulfurization absorption liquid in the oxidation zone 13 to the desulfurization tower at a set flow rate to ensure the liquid level difference between the absorption zone 12 and the oxidation zone 13. The desulfurization liquid in the absorption zone 12 and the oxidation zone 13 is exchanged through the exchange pipe 14, and the liquid levels of the desulfurization liquid in the absorption zone 12 and the oxidation zone 13 are in a balanced state.

[0047] The above are only the preferred embodiments of the present invention and do not impose any form of limitation on the present invention. Although the present invention has been disclosed above with the preferred embodiments, it is not intended to limit the present invention. Any person skilled in the art can make some changes or modifications to the above-disclosed technical content to form equivalent embodiments with equivalent changes within the scope of the technical solution of the present invention. However, as long as it does not depart from the content of the technical solution of the present invention, any brief modifications, equivalent changes and modifications made to the above embodiments based on the technical essence of the present invention still fall within the scope of the technical solution of the present invention.

Claims

1. An integrated absorption and oxidation device, characterized in that: include: An oxidation tank body (1), wherein a partition (11) is provided on the inner wall of the oxidation tank body (1), and the oxidation tank body (1) is divided into an absorption zone (12) and an oxidation zone (13) which are arranged in an upper and lower manner by the partition (11); an exchange tube (14) is passed through and fixedly installed on the partition (11); the exchange tube (14) is used to connect the absorption zone (12) and the oxidation zone (13); an ammonia inlet pipe (15) for conveying ammonia to the absorption zone (12) is provided at the top of the oxidation tank body (1); a baffle (16) is provided in the absorption zone (12); the baffle (16) and the side wall of the oxidation tank body (1) enclose an ammonia addition zone; and the ammonia inlet pipe (15) matches the ammonia addition zone; A liquid inlet pipe (31), wherein the liquid inlet pipe (31) is installed on a side wall of the oxidation tank body (1); a liquid outlet assembly, the liquid outlet assembly comprising a first liquid outlet (41) and a second liquid outlet (45), the first liquid outlet (41) being mounted on a side wall of the oxidation tank body (1), the second liquid outlet (45) being mounted on a side wall of the oxidation tank body (1), the second liquid outlet (45) being arranged in communication with the oxidation zone (13); An oxidation air delivery assembly, the oxidation air delivery assembly comprising an air inlet pipe (51), the air inlet pipe (51) penetrating through and fixedly mounted on a side wall of an oxidation tank body (1), an end of the air inlet pipe (51) away from the oxidation tank body (1) being connected to an oxidation fan (54) via a flange, and an oxidation zone (13) of the oxidation tank body (1) being provided with an exhaust assembly for discharging excess oxidation air; A distributor (6), wherein the distributor (6) is installed in the oxidation zone (13) of the oxidation tank body (1); Liquid level sensing assembly.

2. The absorption and oxidation integrated equipment according to claim 1, characterized in that: The ammonia inlet pipe (15) passes through and is fixedly installed on the top of the oxidation tank body (1); the ammonia inlet pipe (15) is arranged in communication with the absorption zone (12); the baffle (16) is arranged in a bent manner; the bottom end of the baffle (16) is fixedly connected to the top end of the partition (11); and the top end of the baffle (16) is lower than the top end of the exchange tube (14).

3. The absorption and oxidation integrated equipment according to claim 1, characterized in that: The exhaust assembly comprises an exhaust pipe (55), the exhaust pipe (55) penetrates through and is installed on the side wall of the oxidation tank body (1), the exhaust pipe (55) is higher than the bottom end of the exchange pipe (14), and a third solenoid valve (56) is provided on the side wall of the exhaust pipe (55).

4. The absorption and oxidation integrated device according to claim 1, characterized in that: A support assembly, the support assembly is used to support the oxidation tank body (1), the support assembly comprises three support legs (21), the support legs (21) are fixedly mounted on the bottom end of the oxidation tank body (1), and a cross bar (22) is fixedly mounted between the plurality of support legs (21).

5. The absorption and oxidation integrated equipment according to claim 1, characterized in that: The liquid inlet pipe (31) is arranged in communication with the absorption area (12); a first pump body (32) is arranged on the side wall of the liquid inlet pipe (31); and a first solenoid valve (33) is arranged on the side wall of the liquid inlet pipe (31).

6. The absorption and oxidation integrated equipment according to claim 1, characterized in that: The first liquid outlet (41) is arranged in communication with the absorption zone (12); one end of the first liquid outlet (41) away from the oxidation tank body (1) is connected to a first liquid outlet pipe (42) via a flange; the first liquid outlet pipe (42) is used to transport liquid to a desulfurization tower; a main absorption pump (43) is arranged on a side wall of the first liquid outlet pipe (42); and a main solenoid valve (44) is arranged on a side wall of the first liquid outlet pipe (42).

7. The absorption and oxidation integrated equipment according to claim 1, characterized in that: One end of the second liquid outlet (45) away from the oxidation tank body (1) is connected to a second liquid outlet pipe (46) via a flange. The second liquid outlet pipe (46) is used to transport liquid to the desulfurization tower. A secondary absorption pump (47) is provided on the side wall of the second liquid outlet pipe (46). A secondary solenoid valve (48) is provided on the side wall of the second liquid outlet pipe (46).

8. The absorption and oxidation integrated equipment according to claim 1, characterized in that: The air intake pipe (51) matches the oxidation zone (13); a flow meter (52) is provided on the side wall of the air intake pipe (51); and a second solenoid valve (53) is provided on the side wall of the air intake pipe (51).

9. The absorption and oxidation integrated equipment according to claim 1, characterized in that: A square groove (61) is provided at the bottom end of the distributor (6), the square groove (61) is arranged in parallel with the air inlet pipe (51), one end of the air inlet pipe (51) located in the oxidation tank body (1) is located in the square groove (61), and a plurality of annular grooves (62) are provided at the bottom end of the square groove (61), the plurality of annular grooves (62) are located at the same horizontal height and are coaxially arranged, the outer diameters of the plurality of annular grooves (62) are arranged to increase at equal intervals, and the top walls of the plurality of annular grooves (62) are each provided with a plurality of air holes (63).

10. The absorption and oxidation integrated equipment according to claim 1, characterized in that: The liquid level sensor assembly comprises a first liquid level sensor (71) and a second liquid level sensor (72), wherein the first liquid level sensor (71) is installed at the top end of the oxidation tank body (1), and the first liquid level sensor (71) is used to monitor the liquid level of the absorption zone (12); the second liquid level sensor (72) is installed at the bottom end of the oxidation tank body (1), and the second liquid level sensor (72) is used to monitor the liquid level of the oxidation zone (13); the second liquid level sensor (72) and the distributor (6) are arranged to penetrate each other.

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