Advanced treatment device and method for bulk drug waste gas

Abstract

The invention discloses a deep treatment device and method for raw material medicine waste gas, and belongs to the technical field of waste gas treatment. The device comprises a shell, wherein a photolysis mechanism, a high-temperature combustion mechanism, a spraying reaction mechanism, a dust filtering mechanism and a dust removing mechanism are sequentially arranged in the shell from top to bottom; the dust filtering mechanism is used for primarily filtering input waste gas, and the primarily filtered waste gas sequentially enters the spraying reaction mechanism, the high-temperature combustion mechanism and the photolysis mechanism for deep treatment and purification; and the dust removal mechanism is used for cleaning dust particles filtered on the dust filtering mechanism. Waste gas is decomposed and purified by adopting multiple treatment technologies, the waste gas treatment effect is improved, and the treatment cost is reduced.

Description

Technical Field

[0001] The present invention belongs to the technical field of waste gas treatment, and in particular relates to a device and method for deep treatment of bulk drug waste gas. Background Art

[0002] Compared with organic waste gas from other industries, the composition of pharmaceutical process waste gas is complex. In the production process of the pharmaceutical industry, waste gas is generated from multiple operation units such as raw material input, reaction, solvent recovery, filtration, centrifugation, drying, and discharging; its composition is complex and diverse, including but not limited to volatile organic compounds (VOCs), sulfur-containing compounds, nitrogen-containing compounds, particulate matter (PM), odorous gases, and a small amount of toxic and harmful substances such as heavy metal vapor.

[0003] In the prior art, for example, a Chinese invention patent with application number 2018207153001 discloses a deep treatment and purification device for industrial waste gas, which includes a holding cylinder, a liquid storage box is fixedly installed in the middle of the lower side of the holding cylinder, a through hole is opened on the left side of the liquid storage box, support rods are symmetrically installed on the lower side of the holding cylinder, a support plate is fixedly installed on the lower end of the support rod, guide plates are symmetrically installed on both sides of the inside of the holding cylinder, end covers are symmetrically installed on the left and right ends of the holding cylinder, a second motor is installed on the outside of the end cover, a positioning plate is fixedly installed between the second motor and the end cover, a bearing is installed in the middle of the end cover, a second rotating shaft is arranged on the inside of the second motor, and a fan is fixedly installed on the other end of the second rotating shaft. Leaf, a positioning rod is fixedly installed on the middle part of the upper inner wall of the containing cylinder, a positioning frame is fixedly installed on the lower side of the positioning rod, an extrusion block is symmetrically installed on the inner side of the positioning frame, a mounting plate is fixedly installed on the left side of the positioning rod, a sleeve is installed on the right side of the mounting plate, a rotating plate is sleeved on the surface of the sleeve, an adsorption layer is fixedly installed on the left and right sides of the rotating plate, a third rotating shaft is installed on the right side of the sleeve, a second gear is fixedly installed on the surface of the third rotating shaft, a first motor is fixedly installed on the middle part of the upper side of the containing cylinder, a first rotating shaft is installed on the right side of the first motor, a first gear is sleeved on the surface of the first rotating shaft, a chain is sleeved between the first gear and the second gear, and an air intake pipe is symmetrically installed on the upper wall of the containing cylinder.

[0004] The above-mentioned device adopts the absorption method to purify the waste gas, and uses the liquid absorbent to chemically react or physically dissolve the pollutants in the waste gas, thereby separating them from the waste gas; however, due to the complexity and harmfulness of the pharmaceutical process waste gas, when the above-mentioned device is used to adsorb the raw material waste gas, the waste gas purification treatment is not thorough, and the gas after purification still contains harmful gases. The purification rate of the absorption method is low, and the treatment efficiency cannot be guaranteed in industrial applications of high-concentration waste gas treatment.

[0005] Therefore, a device for deep treatment of bulk drug waste gas is needed to improve the above problems. Summary of the invention

[0006] In response to the problems mentioned in the background technology, the present invention proposes a device and method for deep treatment of bulk drug waste gas, which adopts multiple treatment technologies to decompose and purify the waste gas, thereby improving the waste gas treatment effect and reducing the treatment cost.

[0007] Technical solution: In order to solve the above technical problems, the technical solution adopted by the present invention is as follows:

[0008] A device for deep treatment of bulk drug waste gas comprises a shell, wherein a photolysis mechanism, a high-temperature combustion mechanism, a spray reaction mechanism, a dust filtering mechanism and a dust removal mechanism are arranged in the shell from top to bottom in sequence; the dust filtering mechanism is used to perform primary filtration on input waste gas, and the waste gas after the primary filtration enters the spray reaction mechanism, the high-temperature combustion mechanism and the photolysis mechanism in sequence for deep treatment and purification; the dust removal mechanism cleans the dust particles filtered by the dust filtering mechanism.

[0009] Preferably, the photolysis mechanism includes an ultraviolet lamp, a transparent spiral reaction tube, a photolysis chamber, an air outlet one and an air inlet one; the ultraviolet lamp and the transparent spiral reaction tube are both arranged in the photolysis chamber, the air inlet one is arranged at the lower end of the photolysis chamber and is connected to the inlet of the transparent spiral reaction tube, and the air outlet one is arranged at the side end of the shell and is connected to the outlet of the transparent spiral reaction tube.

[0010] Preferably, the high-temperature combustion mechanism includes a combustion chamber and a heating rod and a partition plate arranged in the combustion chamber; the upper end of the combustion chamber is provided with two air outlets, the lower end of the combustion chamber is provided with two air inlets, and a heater is provided on the outside of the shell, and the heater is electrically connected to the heating rod.

[0011] Preferably, the spray reaction mechanism includes a reaction liquid tank and a spray rod, a hollow rotating shaft, a reaction filler, a baffle, and a through pipe arranged in the reaction liquid tank; the hollow rotating shaft passes through the reaction filler and is movably connected with the transfer box, the spray rod is arranged at the top of the hollow rotating shaft, the baffle is arranged on the surface of the hollow rotating shaft, and a through pipe is provided at the lower end of the baffle, and the through pipe is fixedly arranged at the bottom of the reaction liquid tank.

[0012] Preferably, a water pump is provided at the side end of the shell, one end of the water pump is connected to the reaction liquid tank, and the other end of the water pump is connected to the transfer box.

[0013] Preferably, the dust filtering mechanism includes three air outlets, a rotating dust filter plate, three air inlets, and a dust filter bin; three air outlets and three air inlets are provided at the upper end of the dust filter bin, a rotating dust filter plate is provided between the three air outlets and the three air inlets, and the rotating dust filter plate is fixedly arranged on the surface of the hollow rotating shaft.

[0014] Preferably, the dust removal mechanism includes a bevel gear assembly, a dustproof bin, a gear assembly and a motor; the gear assembly includes gear one and gear two; the motor is located at the upper end of the transfer box, and the output end transmission of the motor is provided with gear one, and the gear two is arranged on the surface of the hollow shaft; the bevel gear assembly is arranged on the surface of the hollow shaft and is connected to the dust removal bin.

[0015] Preferably, the bevel gear assembly includes bevel gear one and bevel gear two; bevel gear two is arranged on the surface of the hollow rotating shaft; a brush, a funnel and a dust collecting box are provided in the dust removal bin; the brush is in contact with the lower surface of the rotating dust filter plate, and one end of the brush passes through the dust removal bin and is connected to bevel gear one; the funnel is located at the lower end of the brush, and the dust collecting box is located below the funnel.

[0016] Preferably, the gear one is meshedly connected with the gear two; the bevel gear two is meshedly connected with the bevel gear one.

[0017] A method for deep treatment of bulk drug waste gas, using the bulk drug waste gas deep treatment device described in any of the above items, comprising the following steps:

[0018] Step 1: The waste gas enters the dust filter bin from the inlet, passes through the air inlet 3, filters the dust particles in the waste gas by rotating the dust filter plate, and then passes through the air outlet 3 to enter the reaction liquid bin;

[0019] Step 2: After the primary filtration, the exhaust gas undergoes a preliminary reaction with the reaction filler in the reaction liquid chamber, and then enters the combustion chamber through the second air inlet;

[0020] Step 3: Start the heater to control the heating rod to heat the air to burn the exhaust gas in the combustion chamber, and use the partition plate in the combustion chamber to increase the exhaust gas combustion reaction time;

[0021] Step 4: The exhaust gas after full combustion and decomposition is discharged, or continues to enter the condenser for cooling, or enters the photolysis chamber through the second outlet;

[0022] Step 5: The waste gas enters the transparent spiral reaction tube in the photolysis chamber through the air inlet 1, and the ultraviolet light emitted by the ultraviolet lamp is used to irradiate, decompose and purify the waste gas inside the transparent spiral reaction tube, and finally discharged through the air outlet 1.

[0023] Beneficial effects: Compared with the prior art, the present invention has the following advantages:

[0024] (1) The present invention allows waste gas to enter the dust filter bin, pass through the air inlet three through the rotating dust filter plate to filter out dust particles and other debris, thereby preventing such debris from affecting subsequent reactions and clogging reaction facilities, and then be discharged through the air outlet three.

[0025] (2) In the present invention, the waste gas enters the reaction liquid tank through the through pipe, the water pump draws the reaction liquid in the reaction liquid tank into the transfer box, and then enters the spray rod through the hollow shaft. The motor drives the gear 1 to rotate, thereby acting on the gear 2 on the surface of the hollow shaft, driving the spray rod to rotate and spray on the reaction filler, and the waste gas passes through the reaction filler to react.

[0026] (3) The hollow rotating shaft of the present invention drives the rotating dust filter plate to rotate, and the bevel gear 2 on the surface of the hollow rotating shaft drives the bevel gear 1 to rotate, thereby driving the brush to rotate, so as to clean the surface of the rotating dust filter plate to avoid excessive clogging by dust particles and reducing the air intake. The cleaned dust is collected by the funnel and enters the dust collecting box.

[0027] (4) In the present invention, the waste gas can be discharged after the initial reaction, or continue to enter the combustion chamber, and the heater controls the heating rod to heat the air to burn the waste gas. The waste gas passes through the partition plate in the combustion chamber to increase the residence time of the waste gas, so that the waste gas can be fully burned and decomposed.

[0028] (5) In the present invention, the waste gas can be discharged after the reaction, or continue to enter the condenser for cooling, or skip the combustion chamber and directly enter the photolysis chamber, where the high-intensity ultraviolet rays of a high-power ultraviolet lamp are used to irradiate and decompose the waste gas for purification inside the transparent spiral reaction tube. BRIEF DESCRIPTION OF THE DRAWINGS

[0029] Figure 1 It is a schematic diagram of the overall internal structure of the present invention;

[0030] Figure 2 It is a schematic diagram of the three-dimensional structure of the photolysis mechanism of the present invention;

[0031] Figure 3 It is a schematic diagram of the three-dimensional structure of the high-temperature combustion mechanism of the present invention;

[0032] Figure 4 It is a schematic diagram of the top view of the high temperature combustion mechanism of the present invention;

[0033] Figure 5 It is a structural schematic diagram of the dust removal mechanism of the present invention;

[0034] In the figure: 1. Photolysis mechanism; 11. High-power ultraviolet lamp; 12. Transparent spiral reaction tube; 13. Photolysis chamber; 14. Air outlet 1; 15. Air inlet 1; 2. High-temperature combustion mechanism; 21. Air outlet 2; 22. Heater; 23. Heating rod; 24. Partition plate; 25. Combustion chamber; 26. Air inlet 2; 3. Spray reaction mechanism; 31. Spray rod; 32. Hollow shaft; 33. Reaction filler; 34. Shed; 35. Water pump; 36. Through pipe; 37. Reaction liquid bin; 38. Transfer box; 4. Dust filtering mechanism; 41. Air outlet three; 42. Rotating dust filter plate; 43. Air inlet three; 44. Dust filtering bin; 5. Dust removal mechanism; 51. Bevel gear one; 52. Bevel gear two; 53. Dust removal bin; 54. Gear two; 55. Gear one; 56. Motor; 57. Brush; 58. Funnel; 59. Dust collecting box; 6. Shell. DETAILED DESCRIPTION

[0035] The present invention is further illustrated below in conjunction with specific examples. The examples are implemented based on the technical solutions of the present invention. It should be understood that these examples are only used to illustrate the present invention and are not used to limit the scope of the present invention.

[0036] like Figure 1-Figure 5 As shown, the deep treatment device for bulk drug waste gas provided in this embodiment mainly comprises a shell 6, and a photolysis mechanism 1, a high-temperature combustion mechanism 2, a spray reaction mechanism 3, a dust filtering mechanism 4 and a dust removal mechanism 5 which are arranged in sequence from top to bottom in the shell 6.

[0037] like Figure 1 , Figure 2 As shown, the photolysis mechanism 1 includes an ultraviolet lamp 11, a transparent spiral reaction tube 12, a photolysis chamber 13, an air outlet 14 and an air inlet 15; the photolysis chamber 13 is located at the top of the shell 6, and a plurality of high-power ultraviolet lamps 11 are arranged in the photolysis chamber 13, the transparent spiral reaction tube 12 is arranged in the photolysis chamber 13, and an air outlet 14 and an air inlet 15 are respectively arranged at both ends of the transparent spiral reaction tube 12, the air outlet 14 penetrates the shell 6 and is placed outside the shell 6, and the air inlet 15 is connected to the high-temperature combustion mechanism 2 therebelow.

[0038] The waste gas enters the transparent spiral reaction tube 12 through the air inlet 15, and is irradiated by the high-intensity ultraviolet light of the high-power ultraviolet lamp 11 inside the transparent spiral reaction tube 12 to decompose and purify the waste gas.

[0039] like Figure 1 , Figure 3 , Figure 4As shown, the high-temperature combustion mechanism 2 includes an air outlet 21, a heater 22, a heating rod 23, a partition plate 24, a combustion chamber 25, and an air inlet 26; the combustion chamber 25 is located below the photolysis chamber 13, and the air outlet 21 is arranged through the upper end of the combustion chamber 25, and is connected to the air inlet 15 of the photolysis chamber 13 through a pipeline; the heater 22 is fixedly arranged on the outer side of the shell 6, and a plurality of partition plates 24 are arranged in an upper and lower staggered manner inside the combustion chamber 25, and a plurality of heating rods 23 are fixedly arranged inside the combustion chamber 25; the heater 22 is electrically connected to the heating rod 23; the air inlet 26 is arranged at the lower end of the combustion chamber 25, and penetrates into the spray reaction mechanism 3.

[0040] In this embodiment, the air inlet 15 and the air outlet 21 of the combustion chamber 25 are both connected to the condenser through pipelines.

[0041] like Figure 1 As shown, the spray reaction mechanism 33 includes a spray rod 31 , a hollow rotating shaft 32 , a reaction filler 33 , a baffle 34 , a water pump 35 , a through pipe 36 , a reaction liquid bin 37 , and a transfer box 38 .

[0042] The reaction filler 33 is arranged in the reaction liquid bin 37, the hollow rotating shaft 32 passes through the reaction filler 33 and is movably connected with the transfer box 38, the transfer box 38 is arranged at the bottom of the shell 6, and a spray rod 31 is fixedly provided at the top of the hollow rotating shaft 32. The water pump 35 is arranged at the side end of the shell 6, the water inlet of the water pump 35 is connected to the reaction liquid bin 37 through a pipeline, and the water outlet of the water pump 35 is connected to the transfer box 38 through a pipeline; the baffle 34 is arranged on the surface of the hollow rotating shaft 32 and is located below the reaction filler 33. A through pipe 36 is provided at the lower end of the baffle 34, and the through pipe 36 is fixedly arranged at the bottom of the reaction liquid bin 37.

[0043] In this embodiment, the interior of the hollow shaft 32 is hollow; the through pipe 36 is connected to the baffle 34 via a plurality of support rods; and the air inlet 26 of the combustion chamber 25 is connected to the reaction liquid chamber 37 .

[0044] The waste gas enters the reaction liquid tank 37 through the through pipe 36, and the water pump 35 draws the reaction liquid in the reaction liquid tank 37 into the transfer box 38, and then enters the spray rod 31 through the hollow shaft 32. The spray rod 31 sprays the reaction liquid on the reaction filler 33, and the waste gas passes through the reaction filler 33 to react.

[0045] like Figure 1 As shown, the dust filtering mechanism 4 includes an air outlet 3 41, a rotating dust filter plate 42, an air inlet 3 43, and a dust filter bin 44; the dust filter bin 44 is arranged at the bottom of the shell 6, and the air outlet 3 41 and the air inlet 3 43 are arranged at the upper end of the dust filter bin 44, and a rotating dust filter plate 42 is arranged between the air outlet 3 41 and the air inlet 3 43, and the rotating dust filter plate 42 is fixedly arranged on the surface of the hollow rotating shaft 32.

[0046] The waste gas enters the dust filter bin 44 , passes through the air inlet 3 43 and through the rotating dust filter plate 42 to filter out dust particles and other debris to prevent such debris from affecting subsequent reactions and clogging reaction facilities, and is then discharged through the air outlet 3 41 .

[0047] like Figure 1 , Figure 5 As shown, the dust removal mechanism 5 includes a bevel gear assembly, a dustproof bin 53, a gear assembly and a motor 56;

[0048] The bevel gear assembly includes bevel gear 1 51 and bevel gear 2 52 ; the gear assembly includes gear 2 54 and gear 1 55 .

[0049] A brush 57 is rotatably provided at the inner top of the dust removal bin 53, and the brush 57 is in contact with the lower surface of the rotating dust filter plate 42. One end of the brush 57 passes through the dust removal bin 53 and is connected to bevel gear 1 51. Bevel gear 1 51 is meshed with bevel gear 2 52, and bevel gear 2 52 is fixedly arranged on the surface of the hollow rotating shaft 32.

[0050] The funnel 58 is disposed below the brush 57 , and a dust collecting box 59 is provided below the funnel 58 .

[0051] The motor 56 is located at the upper end of the transfer box 38 , and the output end of the motor 56 is provided with a gear 1 55 , which is meshedly connected with a gear 2 54 , and the gear 2 54 is fixedly disposed on the surface of the hollow rotating shaft 32 .

[0052] The motor 56 drives the gear 1 55 to rotate, thereby acting on the gear 2 54 on the surface of the hollow shaft 32, so that the hollow shaft 32 drives the rotating dust filter plate 42 to rotate, and the bevel gear 2 52 on the surface of the hollow shaft 32 drives the bevel gear 1 51 to rotate, thereby driving the brush 57 to rotate, and cleaning the surface of the rotating dust filter plate 42 to avoid excessive clogging by dust particles and reducing the air intake. The cleaned dust is collected by the funnel 58 and enters the dust collecting box 59.

[0053] The method for deep treatment of API waste gas provided in this embodiment adopts the above-mentioned API waste gas deep treatment device, and comprises the following steps:

[0054] Step 1: The waste gas enters the dust filter bin from the inlet for preliminary filtration, passes through the air inlet 3 43 and filters the dust particles in the waste gas by rotating the dust filter plate 42; then passes through the air outlet 3 41 and enters the reaction liquid bin.

[0055] Step 2: The waste gas after the initial filtration reacts with the reaction filler in the reaction liquid chamber and continues to enter the combustion chamber 25 through the second air inlet 26;

[0056] The waste gas after the initial filtration enters the reaction liquid tank 37 through the through pipe 36, and the water pump 35 draws the reaction liquid in the reaction liquid tank 37 into the transfer box 38, and then enters the spray rod 31 through the hollow shaft 32. The motor 56 drives the gear 1 55 to rotate, thereby acting on the gear 2 54 on the surface of the hollow shaft 32, driving the spray rod 31 to rotate and spray on the reaction filler 33. The waste gas passes through the reaction filler 33 to react. The reaction liquid is any one or more of sodium hydroxide absorption liquid, VOCs (volatile organic compounds) absorbent or VOCs remover.

[0057] Step 3: Start the heater 22 to control the heating rod 23 to heat the air to burn the exhaust gas in the combustion chamber 25, and use the partition plate 24 in the combustion chamber 25 to increase the exhaust gas combustion reaction time;

[0058] Reduce carbon emissions through complete combustion.

[0059] Step 4: The exhaust gas after full combustion and decomposition can be discharged, or continue to enter the condenser for cooling, or enter the photolysis chamber 13 through the second outlet 21;

[0060] The condenser can recover the reaction liquid.

[0061] Step 5: The waste gas enters the transparent spiral reaction tube 12 in the photolysis chamber 13 through the air inlet 15. The waste gas inside the transparent spiral reaction tube 12 is irradiated, decomposed and purified by the ultraviolet light emitted by the ultraviolet lamp 11, and finally discharged through the air outlet 14. Photolysis degrades organic matter into small molecular harmless substances such as CO2 (carbon dioxide) and H2O (water).

[0062] The working principle or use process of the present invention is as follows: when in use, the exhaust gas enters the dust filter bin 44, passes through the rotating dust filter plate 42 along the air inlet three 43, and filters out dust particles and other debris by rotating the dust filter plate 42 to prevent such debris from affecting subsequent reactions and clogging reaction facilities, and then is discharged through the air outlet three 41.

[0063] The waste gas after the initial filtration enters the reaction liquid bin 37 through the through pipe 36, and the water pump 35 draws the reaction liquid in the reaction liquid bin 37 into the transfer box 38, and then enters the spray rod 31 through the hollow shaft 32. The motor 56 drives the gear 1 55 to rotate, thereby acting on the gear 2 54 on the surface of the hollow shaft 32, driving the spray rod 31 to rotate and spray on the reaction filler 33, and the waste gas passes through the reaction filler 33 for reaction; at the same time, the hollow shaft 32 drives the rotating dust filter plate 42 to rotate, and the bevel gear 2 52 on the surface of the hollow shaft 32 drives the bevel gear 1 51 to rotate, thereby driving the brush 57 to rotate, and the surface of the rotating dust filter plate 42 is cleaned to avoid excessive clogging of dust particles resulting in a reduction in air intake. The cleaned dust is collected through the funnel 58 and enters the dust collecting box 59.

[0064] The exhaust gas can be discharged after the initial reaction, or continue to enter the combustion chamber 25 through the air inlet 26. The heater 22 controls the heating rod 23 to heat the air to burn the exhaust gas. The exhaust gas passes through the partition plate 24 in the combustion chamber 25 to increase the residence time of the exhaust gas, so that the exhaust gas can be fully burned and decomposed.

[0065] The waste gas can be discharged after the reaction, or continue to enter the condenser for cooling, or skip the combustion chamber 25 for combustion and directly enter the photolysis chamber 13 through the air outlet 21. The waste gas enters the transparent spiral reaction tube 12 along the air inlet 15, and is decomposed and purified by the high-intensity ultraviolet light of the high-power ultraviolet lamp 11 inside the transparent spiral reaction tube 12, and is finally discharged through the air outlet 14.

[0066] The above is only a preferred embodiment of the present invention. It should be pointed out that for ordinary technicians in this technical field, several improvements and modifications can be made without departing from the principle of the present invention. These improvements and modifications should also be regarded as the scope of protection of the present invention.

Claims

1. A device for deep treatment of bulk drug waste gas, comprising a housing (6), characterized in that: The housing (6) is provided with a photolysis mechanism (1), a high-temperature combustion mechanism (2), a spray reaction mechanism (3), a dust filtering mechanism (4) and a dust removal mechanism (5) in order from top to bottom; the dust filtering mechanism (4) is used to perform primary filtration on the input waste gas, and the waste gas after the primary filtration enters the spray reaction mechanism (3), the high-temperature combustion mechanism (2) and the photolysis mechanism (1) in order for deep treatment and purification; the dust removal mechanism (5) cleans the dust particles filtered by the dust filtering mechanism (4).

2. The device for deep treatment of bulk drug waste gas according to claim 1, characterized in that: The photolysis mechanism (1) comprises an ultraviolet lamp (11), a transparent spiral reaction tube (12), a photolysis chamber (13), an air outlet (14) and an air inlet (15); the ultraviolet lamp (11) and the transparent spiral reaction tube (12) are both arranged in the photolysis chamber (13), the air inlet (15) is arranged at the lower end of the photolysis chamber (13) and is connected to the inlet of the transparent spiral reaction tube (12), and the air outlet (14) is arranged at the side end of the shell (6) and is connected to the outlet of the transparent spiral reaction tube (12).

3. The device for deep treatment of bulk drug waste gas according to claim 1, characterized in that: The high-temperature combustion mechanism (2) comprises a combustion chamber (25) and a heating rod (23) and a partition plate (24) arranged in the combustion chamber (25); an air outlet (21) is arranged at the upper end of the combustion chamber (25), an air inlet (26) is arranged at the lower end of the combustion chamber (25), and a heater (22) is arranged on the outer side of the shell (6), and the heater (22) is electrically connected to the heating rod (23).

4. The device for deep treatment of bulk drug waste gas according to claim 1, characterized in that: The spray reaction mechanism (3) comprises a reaction liquid bin (37) and a spray rod (31), a hollow rotating shaft (32), a reaction filler (33), a baffle (34), and a through pipe (36) arranged in the reaction liquid bin (37); the hollow rotating shaft (32) penetrates the reaction filler (33) and is movably connected to the transfer box (38); the spray rod (31) is arranged at the top end of the hollow rotating shaft (32); the baffle (34) is arranged on the surface of the hollow rotating shaft (32); a through pipe (36) is arranged at the lower end of the baffle (34); and the through pipe (36) is fixedly arranged at the bottom of the reaction liquid bin (37).

5. The device for deep treatment of bulk drug waste gas according to claim 4 is characterized in that: A water pump (35) is provided at the side end of the housing (6), one end of the water pump (35) is connected to the reaction liquid tank (37), and the other end is connected to the transfer box (38).

6. The device for deep treatment of bulk drug waste gas according to claim 1, characterized in that: The dust filtering mechanism (4) comprises an air outlet three (41), a rotating dust filter plate (42), an air inlet three (43), and a dust filter bin (44); the air outlet three (41) and the air inlet three (43) are provided at the upper end of the dust filter bin (44); a rotating dust filter plate (42) is provided between the air outlet three (41) and the air inlet three (43); and the rotating dust filter plate (42) is fixedly arranged on the surface of the hollow rotating shaft (32).

7. The device for deep treatment of bulk drug waste gas according to claim 1, characterized in that: The dust removal mechanism (5) comprises a bevel gear assembly, a dustproof bin (53), a gear assembly and a motor (56); the gear assembly comprises a gear 1 (55) and a gear 2 (54); the motor (56) is located at the upper end of the transfer box (38), the output end of the motor (56) is provided with a gear 1 (55), and the gear 2 (54) is arranged on the surface of the hollow rotating shaft (32); the bevel gear assembly is arranged on the surface of the hollow rotating shaft (32) and is connected to the dust removal bin (53).

8. The device for deep treatment of bulk drug waste gas according to claim 7, characterized in that: The bevel gear assembly comprises a bevel gear 1 (51) and a bevel gear 2 (52); the bevel gear 2 (52) is arranged on the surface of the hollow rotating shaft (32); a brush (57), a funnel (58) and a dust collecting box (59) are arranged in the dust removal bin (53); the brush (57) is in contact with the lower surface of the rotating dust filter plate (42), and one end of the brush (57) passes through the dust removal bin (53) and is connected to the bevel gear 1 (51); the funnel (58) is located at the lower end of the brush (57), and the dust collecting box (59) is located below the funnel (58).

9. The device for deep treatment of bulk drug waste gas according to claim 8, characterized in that: The gear one (55) is meshedly connected with the gear two (54); the bevel gear two (52) is meshedly connected with the bevel gear one (51).

10. A method for deep treatment of bulk drug waste gas, using the apparatus for deep treatment of bulk drug waste gas according to claims 1 to 9, characterized in that: The following steps are involved: Step 1: The waste gas enters the dust filter bin from the inlet, passes through the air inlet three (43), filters the dust particles in the waste gas by rotating the dust filter plate (42), and then passes through the air outlet three (41) into the reaction liquid bin; Step 2: After the primary filtration, the waste gas undergoes a preliminary reaction with the reaction filler in the reaction liquid chamber, and then enters the combustion chamber (25) through the second air inlet (26); Step 3: Start the heater (22) to control the heating rod (23) to heat the air to burn the waste gas in the combustion chamber (25), and use the partition plate (24) in the combustion chamber (25) to increase the combustion reaction time of the waste gas; Step 4: The waste gas after full combustion and decomposition is discharged, or continues to enter the condenser for cooling, or enters the photolysis chamber (13) through the second outlet (21); Step 5: The waste gas enters the transparent spiral reaction tube (12) in the photolysis chamber (13) through the air inlet 1 (15), and the waste gas inside the transparent spiral reaction tube (12) is irradiated and decomposed and purified by the ultraviolet light emitted by the ultraviolet lamp (11), and finally discharged through the air outlet 1 (14).

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