Integrated pharmaceutical waste gas treatment apparatus and method thereof

The integrated waste gas treatment equipment enables automatic adjustment of filter mesh size and dilution based on waste gas composition and particle size, solving the risks of filter clogging and explosion, improving treatment efficiency and safety, and enhancing heat recovery efficiency.

CN123038588APending Publication Date: 2026-11-06GUANGZHOU AIR ENVIRONMENTAL ENG CO LTD
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Patent Information

Application Number
CN202611497843.6
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2026-09-24
Publication Date
2026-11-06

AI Technical Summary

Technical Problem

Existing pharmaceutical waste gas treatment equipment cannot adjust the filter mesh size in real time, resulting in poor filtration effect or filter clogging, and there is an explosion risk when high-concentration waste gas is burned.

Method used

An integrated waste gas treatment device is adopted, which automatically selects a filter screen with an appropriate mesh size by detecting the composition and particle size of the waste gas, and sets pressure detection devices before and after filtration to judge the blockage. In the case of high-concentration waste gas, it is diluted through a dilution channel, and preheating and oxidation decomposition are carried out by using a rotary valve and a heat storage body.

Benefits of technology

It improves the efficiency and safety of waste gas treatment, ensures that the filter screen does not clog, prevents explosions, and enhances heat recovery efficiency.

✦ Generated by Eureka AI based on patent content.

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Abstract

This invention discloses an integrated waste gas treatment device and method for pharmaceutical applications, relating to the field of pharmaceutical waste gas treatment technology. The integrated waste gas treatment device includes an oxidation furnace with a heat storage body inside. A rotary valve is installed at the bottom of the oxidation furnace, with an inlet channel and an exhaust channel. The inlet channel is connected to a buffer chamber, and a dilution channel is located at the bottom of the buffer chamber. A pipe diameter adjustment device is fixedly installed on the dilution channel, and a gas storage tank is fixedly installed at the end of the dilution channel. An air inlet is provided on the buffer chamber and fixedly connected to a filter assembly. The filter assembly includes a mounting housing and a filter screen. Interfaces are provided on both ends of the mounting housing, and pressure detection devices are provided on the inner walls of the interfaces. The appropriate filter screen is automatically selected based on the size of the particulate matter in the waste gas. Pressure detection devices are installed before and after the filter assembly. The pressure difference before and after the filter assembly can indicate the clogging status of the filter screen and allow for maintenance, thereby improving the overall waste gas treatment effect of the equipment.
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Description

Technical Field

[0001] This invention relates to the field of pharmaceutical waste gas treatment technology, specifically to an integrated waste gas treatment device and method for pharmaceutical applications. Background Technology

[0002] The waste gas generated during pharmaceutical production has a complex composition, typically containing various pollutants such as volatile organic compounds, acidic gases, and particulate matter. How to efficiently and safely treat pharmaceutical waste gas has become a key technical problem that urgently needs to be solved in this field.

[0003] Currently, the pharmaceutical industry primarily employs staged treatment processes for waste gas. For particulate matter in the waste gas, the mainstream solution is to use bag filters or dry filters for interception. However, these methods maintain a constant filter mesh size, making it impossible to adjust in real time when the particle size in the pharmaceutical waste gas changes, thus affecting filtration efficiency. Furthermore, when the concentration of particulate matter in the waste gas is too high, directly introducing it into an oxidation furnace for combustion and oxidation can easily lead to explosions, posing a significant safety hazard.

[0004] Therefore, there is an urgent need in this field for an integrated pharmaceutical waste gas treatment device that can adjust the filter mesh size in real time according to the particle size of the particulate matter in the waste gas, while diluting high-concentration waste gas, thereby ensuring the efficiency and safety of the waste gas treatment process. Summary of the Invention

[0005] The purpose of this invention is to provide an integrated waste gas treatment device and method for pharmaceutical applications, in order to solve the problems raised in the prior art.

[0006] To achieve the above objectives, the present invention provides the following technical solution: The integrated waste gas treatment equipment for pharmaceutical applications includes an oxidation furnace, a heat storage body is provided inside the oxidation furnace, a rotary valve is installed at the bottom of the oxidation furnace, the rotary valve has an air inlet channel and an exhaust channel, the air inlet channel is connected to a buffer chamber, a dilution channel is provided at the bottom of the buffer chamber, a pipe diameter adjustment component is fixedly installed on the dilution channel, a gas storage tank is fixedly installed at the end of the dilution channel, an air inlet is provided on the buffer chamber, the air inlet is fixedly connected to a filter assembly, the filter assembly includes a mounting shell and a filter screen, interfaces are provided on both ends of the mounting shell, and pressure detection components are provided on the inner wall of the interfaces.

[0007] As a preferred technical solution, the side wall of the mounting housing has a notch, the top of the mounting housing is equipped with a rotating motor, the filter assembly also includes a movable baffle, the movable baffle is disposed on the side wall of the mounting housing, the movable baffle blocks the notch, the movable baffle has a collection groove, a rotating shaft is disposed inside the mounting housing, the rotating shaft is connected to the output end of the rotating motor, a partition is provided around the side wall of the rotating shaft, and a sealing strip is provided at the edge of the partition.

[0008] As a preferred technical solution, the rotating shaft is provided with a connecting port, and slots are provided on both sides of the connecting port. A locking spring is installed at the bottom of the slot, and a pin is provided in the slot. The bottom of the pin is fixedly connected to the locking spring. A first inclined surface is provided on the pin facing the connecting port, and a second inclined surface is provided on the top of the pin. A reset spring is fixedly installed on the rear wall of the connecting port. The reset spring is fixedly connected to a reset plate. The filter screen is installed between the two partitions. The filter screen includes an installation sleeve and a filter element. A connecting block is provided on the side wall of the installation sleeve, and connecting grooves are provided on both sides of the connecting block.

[0009] As a preferred technical solution, an adjustment motor is provided at the bottom of the buffer chamber, and an adjustment wheel is provided at the output end of the adjustment motor.

[0010] As a preferred technical solution, the pipe diameter adjusting component includes a rotating seat and a fixed seat. An adjusting plate is arranged in a ring between the rotating seat and the fixed seat. Both the rotating seat and the fixed seat have through holes in their middle parts. The bottom of the rotating seat has evenly formed arc-shaped grooves. The side wall of the rotating seat has circumferential locking teeth. The top of the fixed seat has evenly formed straight grooves. Limiting posts are provided on both ends of the adjusting plate. One limiting post is embedded in the arc-shaped groove, and the other limiting post is embedded in the straight groove. The adjusting wheel meshes with the locking teeth.

[0011] As a preferred technical solution, the oxidation furnace is uniformly surrounded by heat insulation plates, the heat storage body is installed between two heat insulation plates, the top of the heat insulation plates is provided with a combustion chamber, and the bottom of the oxidation furnace is provided with an opening.

[0012] As a preferred technical solution, the rotary valve is provided with a rotating shaft, the rotating shaft is provided with an air supply channel, the connection between the rotating shaft and the air inlet channel is provided with an inlet, the top of the rotating shaft is provided with a distribution chamber, the distribution chamber is connected to the opening, the distribution chamber includes a preheating zone and an air outlet zone, a sealing plate is provided between the air inlet channel and the exhaust channel, the air supply channel is connected to the preheating zone, and the exhaust channel is connected to the air outlet zone.

[0013] This application provides a waste gas treatment method for an integrated waste gas treatment device used in pharmaceutical manufacturing, the steps of which are as follows: S1: Introduce pharmaceutical waste gas into the filter assembly and switch to a filter screen with an appropriate mesh size according to the particle size in the pharmaceutical waste gas. S2: By comparing the pressure difference between the two ports on both sides of the filter assembly using the pressure detection device, it can be determined whether the filter screen is clogged, which makes it easier to determine the replacement cycle of the filter screen. S3: After filtration, the concentration of pharmaceutical waste gas is detected. When the concentration is too high, the dilution channel is opened through the pipe diameter adjustment component to dilute the high concentration of pharmaceutical waste gas in the buffer chamber. S4: The pretreated pharmaceutical waste gas is distributed in the oxidation furnace through a rotary valve for oxidation and decomposition, and finally discharged as pollution-free gas.

[0014] Compared with the prior art, the beneficial effects of the present invention are: 1. Before the pharmaceutical waste gas is introduced into the treatment equipment, the composition of the pharmaceutical waste gas is detected. The appropriate mesh size of the filter screen is automatically selected according to the size of the particulate matter in the waste gas to avoid poor filtration effect or filter screen blockage. At the same time, pressure detection devices are installed before and after the filter components. The pressure difference before and after can reflect the blockage of the filter screen, making it easy to determine the replacement cycle of the filter screen and improve the overall waste gas treatment effect and maintenance efficiency of the equipment. 2. After filtration, the concentration of pharmaceutical waste gas continues to be monitored. The opening size of the pipe diameter regulating component is adjusted in real time according to the concentration of pharmaceutical waste gas. Low-concentration fresh air is introduced into the buffer chamber through the dilution channel to dilute the pharmaceutical waste gas, preventing explosions of high-concentration waste gas during oxidation and ensuring the safety of waste gas treatment. 3. After the preceding pretreatment, the pharmaceutical waste gas enters the rotary valve through the inlet channel. The rotation of the rotary shaft continuously distributes the pharmaceutical waste gas to different heat storage bodies for preheating, and the gas after oxidation and combustion passes through the heat storage body for discharge. During the discharge process, the high-temperature gas transfers heat to the heat storage body, improving the heat recovery efficiency. Attached Figure Description

[0015] Figure 1 This is a schematic diagram of the main structure of the present invention; Figure 2 This is a cross-sectional structural diagram of the main body of the present invention; Figure 3 This is a cross-sectional structural diagram of the main body of the invention from another perspective; Figure 4 This is a cross-sectional structural diagram of the filter assembly of the present invention; Figure 5 This is a schematic diagram of the cross-section of the filter assembly of the present invention; Figure 6 This is a schematic diagram of the structure of the rotating shaft of the present invention; Figure 7 This is a schematic diagram of the buffer chamber of the present invention; Figure 8 This is an exploded structural diagram of the pipe diameter adjusting component of the present invention; Figure 9 This is a schematic diagram of the rotating base of the present invention; Figure 10 yes Figure 5 Enlarged structural diagram at point A in the diagram; Figure 11 yes Figure 6A magnified structural diagram at point B in the diagram.

[0016] In the diagram: 1. Oxidation furnace; 2. Rotary valve; 3. Buffer chamber; 4. Dilution channel; 5. Pipe diameter adjustment component; 6. Filter assembly; 11. Heat storage body; 12. Heat insulation plate; 13. Combustion chamber; 14. Opening; 21. Intake passage; 22. Exhaust passage; 23. Rotating shaft; 24. Distribution chamber; 25. Sealing plate; 31. Air inlet; 32. Adjusting motor; 41. Air tank; 51. Rotating seat; 52. Fixed seat; 53. Adjusting plate; 54. Through hole; 61. Mounting housing; 62. Movable baffle; 63. Rotating shaft; 64. Connection port; 65. Pin; 66. Filter screen; 2301. Gas supply channel; 2302. Inlet; 2401. Preheating zone; 2402. Gas outlet zone; 3201. Adjusting wheel; 5101. Arc groove; 5102. Clamping tooth; 5201. Straight groove; 5301. Limiting post; 6101. Interface; 6102. Pressure detection element; 6103. Notch; 6104. Rotating motor; 6201. Collection tank; 6301. Partition plate; 6302. Sealing strip; 6401. Slot; 6402. Locking spring; 6403. Return spring; 6404. Return plate; 6501. First inclined surface; 6502. Second inclined surface; 6601. Mounting sleeve; 6602. Filter element; 6603. Connecting block; 6604. Connecting groove. Detailed Implementation

[0017] The technical solutions of the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some embodiments of the present invention, and not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those skilled in the art without creative effort are within the scope of protection of the present invention.

[0018] Example: Figures 1-11 As shown, the present invention provides a technical solution for an integrated waste gas treatment device for pharmaceutical applications. This integrated waste gas treatment device includes an oxidizer 1, a heat storage body 11 inside the oxidizer 1, a rotary valve 2 installed at the bottom of the oxidizer 1, the rotary valve 2 having an inlet channel 21 and an exhaust channel 22, the inlet channel 21 being connected to a buffer chamber 3, a dilution channel 4 at the bottom of the buffer chamber 3, a pipe diameter adjustment component 5 fixedly installed on the dilution channel 4, a gas storage tank 41 fixedly installed at the end of the dilution channel 4, an air inlet 31 on the buffer chamber 3, the air inlet 31 being fixedly connected to a filter assembly 6, the filter assembly 6 including a mounting housing 61 and a filter screen 66, interfaces 6101 on both ends of the mounting housing 61, and pressure detection components 6102 on the inner wall of the interfaces 6101.

[0019] Before the pharmaceutical waste gas enters the treatment equipment, the composition of the waste gas is detected. The appropriate mesh size of the filter screen 66 is automatically selected according to the size of the particulate matter in the waste gas to avoid poor filtration effect or filter screen blockage. At the same time, pressure detection devices 6102 are set before and after the filter component 6. The pressure difference before and after can reflect the blockage of the filter screen 66, which makes it easy to determine the replacement cycle of the filter screen 66, improve the overall waste gas treatment effect and maintenance efficiency of the equipment.

[0020] After filtration, the concentration of pharmaceutical waste gas is monitored. The opening 14 of the pipe diameter regulating component 5 is adjusted in real time according to the concentration of pharmaceutical waste gas. Low-concentration fresh air is introduced into the buffer chamber 3 through the dilution channel 4 to dilute the pharmaceutical waste gas, preventing high-concentration waste gas from exploding during oxidation and ensuring the safety of waste gas treatment.

[0021] After undergoing pretreatment, the pharmaceutical waste gas enters the rotary valve 2 through the inlet channel 21. The rotation of the rotary shaft 23 continuously distributes the pharmaceutical waste gas to different heat storage bodies 11 for preheating, and the gas after oxidation and combustion passes through the heat storage body 11 and is discharged. During the discharge process, the high-temperature gas transfers heat to the heat storage body 11, thereby improving the heat recovery efficiency.

[0022] The mounting housing 61 has a notch 6103 on its side wall and a rotating motor 6104 is mounted on the top of the mounting housing 61. The filter assembly 6 also includes a movable baffle 62, which is located on the side wall of the mounting housing 61 and blocks the notch 6103. A collection groove 6201 is provided on the movable baffle 62. A rotating shaft 63 is provided inside the mounting housing 61 and is connected to the output end of the rotating motor 6104. A partition 6301 is provided around the side wall of the rotating shaft 63, and a sealing strip 6302 is provided at the edge of the partition 6301.

[0023] A connecting port 64 is provided on the upper ring of the rotating shaft 63. Slots 6401 are provided on both side walls of the connecting port 64. A locking spring 6402 is installed at the bottom of the slot 6401. A pin 65 is provided inside the slot 6401, with its bottom fixedly connected to the locking spring 6402. A first inclined surface 6501 is provided on the pin 65 facing the connecting port 64, and a second inclined surface 6502 is provided on the top of the pin 65. A return spring 6403 is fixedly installed on the rear wall of the connecting port 64, and is fixedly connected to a return plate 6404. A filter screen 66 is installed between two partitions 6301. The filter assembly 6 includes an installation sleeve 6601 and a filter element 6602. The side wall of the installation sleeve 6601 is provided with a connecting block 6603. Both sides of the connecting block 6603 are provided with connecting grooves 6604. The filter element 6602 with a mesh size matching can not only improve the filtration effect of exhaust gas, but also slow down the clogging speed of the filter element 6602 and improve its service life. Pressure detection elements 6102 are provided in the front and rear interfaces 6101 of the filter assembly 6. The clogging status of the filter element 6602 is judged according to the pressure difference before and after the exhaust gas, which makes it easier for the staff to judge the replacement cycle of the filter element 6602, thereby improving the efficiency of subsequent maintenance.

[0024] Press the filter screen 66 downwards. Under pressure, the pin 65 is pressed back into the slot 6401 along the second inclined surface 6502. The connecting block 6603, no longer restrained by the pin 65, is ejected by the return spring 6403, completing the disassembly of the filter screen 66. To install a new filter screen 66, simply insert the connecting block 6603 into the connecting port 64. The pin 65 is pressed into the slot 6401 along the first inclined surface 6501 until the connecting groove 6604 connects with the slot 6401. The pin 65 then pops out again, completing the fixing of the new filter screen 66.

[0025] In addition, during the process of switching the filter screen 66 by rotating shaft 63, the edge sealing strip 6302 continuously scrapes away the impurities attached to the inner wall of the mounting housing 61. Finally, these impurities are collected by the collection groove 6201 and removed when the movable baffle 62 is removed, thus completing the self-cleaning of the filter assembly 6.

[0026] An adjustment motor 32 is installed at the bottom of the buffer chamber 3, and an adjustment wheel 3201 is installed at the output end of the adjustment motor 32.

[0027] The pipe diameter adjusting component 5 includes a rotating seat 51 and a fixed seat 52. An adjusting plate 53 is arranged circumferentially between the rotating seat 51 and the fixed seat 52. Both the rotating seat 51 and the fixed seat 52 have through holes 54 in the middle. The bottom of the rotating seat 51 is uniformly provided with arc-shaped grooves 5101, and the side wall of the rotating seat 51 is provided with retaining teeth 5102. The top of the fixed seat 52 is uniformly provided with straight grooves 5201. Both ends of the adjusting plate 53 are provided with limit posts 5301. One limit post 5301 is embedded in the arc-shaped groove 5101, and the other limit post 5301 is embedded in the straight groove 5201. The adjusting wheel 3201 meshes with the retaining teeth 5102. The concentration is detected before the exhaust gas enters the buffer chamber 3. When the concentration is too high, the adjusting motor 32 is started. Motor 32 drives the adjusting wheel 3201 to rotate, and the adjusting wheel 3201 meshes with the locking tooth 5102. Therefore, the adjusting motor 32 can drive the rotating seat 51 to rotate. When the rotating seat 51 rotates, the limiting posts 5301 on both sides of the adjusting plate 53 move in the straight groove 5201 and the arc groove 5101 respectively. This allows the adjusting plate 53 to move along the direction of the straight groove 5201, opening the through hole 54 and allowing the low-concentration fresh air in the gas storage tank 41 to enter the buffer chamber 3 and mix with the high-concentration exhaust gas to complete the dilution, thereby reducing the exhaust gas concentration. The size of the through hole 54 is adjusted in real time according to the concentration entering the buffer chamber 3, thereby ensuring that the exhaust gas concentration entering the oxidation furnace 1 is basically consistent and maintaining the stability of the combustion temperature in the combustion chamber 13.

[0028] The oxidizing furnace 1 is uniformly surrounded by heat insulation plates 12, and the heat storage body 11 is installed between the two heat insulation plates 12. The top of the heat insulation plate 12 is provided with a combustion chamber 13, and the bottom of the oxidizing furnace 1 is provided with an opening 14.

[0029] A rotating shaft 23 is provided inside the rotating valve 2. An air supply channel 2301 is provided inside the rotating shaft 23. An inlet 2302 is provided at the connection between the rotating shaft 23 and the air inlet channel 21. A distribution chamber 24 is provided at the top of the rotating shaft 23. The distribution chamber 24 is connected to the opening 14. The distribution chamber 24 includes a preheating zone 2401 and an air outlet zone 2402. A sealing plate 25 is provided between the air inlet channel 21 and the exhaust channel 22. The air supply channel 2301 is connected to the preheating zone 2401, and the exhaust channel 22 is connected to the air outlet zone 2402.

[0030] This application provides a waste gas treatment method for an integrated waste gas treatment device used in pharmaceutical manufacturing, the steps of which are as follows: S1: Introduce pharmaceutical exhaust gas into the filter assembly 6, and switch the filter screen 66 with the appropriate mesh size according to the particle size in the pharmaceutical exhaust gas. S2: By comparing the pressure difference between the two ports 6101 on both sides of the filter assembly 6 using the pressure detection element 6102, it can be determined whether the filter screen 66 is blocked, which makes it easier to determine the replacement cycle of the filter screen 66. S3: After filtration, the concentration of pharmaceutical waste gas is detected. When the concentration is too high, the dilution channel 4 is opened through the pipe diameter adjustment component 5 to dilute the high concentration of pharmaceutical waste gas in the buffer chamber 3. S4: The pretreated pharmaceutical waste gas is distributed in the oxidation furnace 1 through the rotary valve 2 for oxidation and decomposition, and finally discharged as pollution-free gas.

[0031] Working principle of the invention: Before treating pharmaceutical waste gas, the main components and particle size of the waste gas are detected. Based on the components, a suitable alkaline washing method is selected to reduce the corrosiveness of the waste gas. Then, the gas is introduced into the filter assembly 6 through interface 6101. The filter assembly 6 contains filter elements 6602 with different mesh sizes. The appropriate filter element 6602 is selected based on the previously detected particle size and connected to interface 6101. After prolonged use, the filter screen 66 needs to be replaced. First, the filter screen 66 to be replaced is moved to the notch 6103 by rotating the motor 6104. Then, the movable baffle 62 is removed. Simply press the filter screen 66 downwards; under pressure, the pin 65 is pressed back into the slot 6401 along the second inclined surface 6502. When the connecting block 6603 loses the limit of the pin 65, it is ejected under the push of the return spring 6403, completing the disassembly of the filter screen 66. To install the new filter screen 66, simply insert the connecting block 6603 into the connecting port 64, and the pin 65 is pressed into the slot 6401 along the first inclined surface 6501 until the connecting groove 6604 is connected to the slot 6401. The pin 65 then pops out again to fix the new filter screen 66. In addition, during the process of switching the filter screen 66 by rotating the shaft 63, the edge sealing strip 6302 continuously scrapes away the impurities attached to the inner wall of the mounting housing 61. Finally, these impurities are collected by the collection groove 6201 and removed when the movable baffle 62 is removed, completing the self-cleaning of the filter assembly 6.

[0032] After the exhaust gas is filtered, a concentration test is required to prevent high-concentration exhaust gas from exploding during combustion oxidation. When the concentration is detected to be too high, the regulating motor 32 is activated, which drives the regulating wheel 3201 to rotate. The regulating wheel 3201 engages with the locking tooth 5102, so the regulating motor 32 can drive the rotating seat 51 to rotate. When the rotating seat 51 rotates, the limiting posts 5301 on both sides of the regulating plate 53 move in the straight groove 5201 and the arc groove 5101 respectively. This allows the regulating plate 53 to move along the direction of the straight groove 5201, opening the through hole 54 and allowing the low-concentration fresh air in the gas storage tank 41 to enter the buffer chamber 3 and mix with the high-concentration exhaust gas to dilute it, thereby reducing the exhaust gas concentration. The size of the through hole 54 is adjusted in real time according to the concentration entering the buffer chamber 3 to ensure that the concentration of exhaust gas entering the oxidizer 1 is basically consistent and to maintain the stability of the combustion temperature in the combustion chamber 13.

[0033] After the preceding pretreatment, the pharmaceutical waste gas enters the rotary valve 2 through the inlet channel 21. The waste gas then passes through the inlet 2302 and the gas delivery channel 2301 into the preheating zone 2401 of the distribution chamber 24. Subsequently, as the rotating shaft 23 rotates, the waste gas is passed into different heat storage bodies 11 for preheating. Afterward, it enters the combustion chamber 13 at the top of the oxidizer 1 for complete combustion to generate carbon dioxide and water. The purified gas passes through the heat storage body 11 and enters the outlet zone 2402 in the distribution chamber 24. During the process of passing through the heat storage body 11, the high-temperature purified gas transfers heat to the relatively low-temperature heat storage body 11, achieving full heat recovery and improving energy utilization. The outlet zone 2402 is connected to the exhaust channel 22, which is set to negative pressure. Finally, the purified gas is spontaneously discharged through the exhaust channel 22 due to the pressure difference, completing the treatment of the pharmaceutical waste gas.

[0034] It will be apparent to those skilled in the art that the present invention is not limited to the details of the exemplary embodiments described above, and that the invention can be implemented in other specific forms without departing from its spirit or essential characteristics. Therefore, the embodiments should be considered in all respects as exemplary and non-limiting, and the scope of the invention is defined by the appended claims rather than the foregoing description. Thus, all variations falling within the meaning and scope of equivalents of the claims are intended to be included within the present invention. No reference numerals in the claims should be construed as limiting the scope of the claims.

Claims

1. An integrated waste gas treatment device for pharmaceutical applications, characterized in that: The integrated waste gas treatment equipment for pharmaceutical use includes an oxidation furnace (1), a heat storage body (11) is provided inside the oxidation furnace (1), a rotary valve (2) is installed at the bottom of the oxidation furnace (1), the rotary valve (2) has an air inlet channel (21) and an exhaust channel (22), the air inlet channel (21) is connected to a buffer chamber (3), a dilution channel (4) is provided at the bottom of the buffer chamber (3), a pipe diameter adjustment component (5) is fixedly installed on the dilution channel (4), a gas storage tank (41) is fixedly installed at the end of the dilution channel (4), an air inlet (31) is provided on the buffer chamber (3), the air inlet (31) is fixedly connected to a filter assembly (6), the filter assembly (6) includes a mounting shell (61) and a filter screen (66), both ends of the mounting shell (61) are provided with an interface (6101), and the inner wall of the interface (6101) is provided with a pressure detection component (6102).

2. The integrated waste gas treatment equipment for pharmaceutical applications according to claim 1, characterized in that: The mounting housing (61) has a notch (6103) on its side wall. A rotating motor (6104) is installed on the top of the mounting housing (61). The filter assembly (6) also includes a movable baffle (62). The movable baffle (62) is disposed on the side wall of the mounting housing (61) and blocks the notch (6103). A collection groove (6201) is provided on the movable baffle (62). A rotating shaft (63) is provided inside the mounting housing (61). The rotating shaft (63) is connected to the output end of the rotating motor (6104). A partition (6301) is provided around the side wall of the rotating shaft (63). A sealing strip (6302) is provided at the edge of the partition (6301).

3. The integrated waste gas treatment equipment for pharmaceutical applications according to claim 2, characterized in that: The rotating shaft (63) is provided with a connecting port (64) on its ring. Slots (6401) are provided on both sides of the connecting port (64). A locking spring (6402) is installed at the bottom of the slot (6401). A pin (65) is provided inside the slot (6401). The bottom of the pin (65) is fixedly connected to the locking spring (6402). A first inclined surface (6501) is provided on the pin (65) facing the connecting port (64). A second inclined surface (6501) is provided on the top of the pin (65). The inclined surface (6502) has a reset spring (6403) fixedly installed on the rear wall of the connection port (64). The reset spring (6403) is fixedly connected to the reset plate (6404). The filter screen (66) is installed between the two partitions (6301). The filter screen (66) includes an installation sleeve (6601) and a filter element (6602). The side wall of the installation sleeve (6601) is provided with a connecting block (6603). The connecting block (6603) has connecting grooves (6604) on both sides.

4. The integrated waste gas treatment equipment for pharmaceutical applications according to claim 3, characterized in that: The bottom of the buffer chamber (3) is provided with an adjustment motor (32), and the output end of the adjustment motor (32) is provided with an adjustment wheel (3201).

5. The integrated waste gas treatment equipment for pharmaceutical applications according to claim 4, characterized in that: The pipe diameter adjusting component (5) includes a rotating seat (51) and a fixed seat (52). An adjusting plate (53) is arranged in a ring between the rotating seat (51) and the fixed seat (52). A through hole (54) is provided in the middle of both the rotating seat (51) and the fixed seat (52). An arc-shaped groove (5101) is evenly opened at the bottom of the rotating seat (51). A retaining tooth (5102) is arranged around the side wall of the rotating seat (51). A straight groove (5201) is evenly arranged at the top of the fixed seat (52). Limiting posts (5301) are provided on both ends of the adjusting plate (53). One limiting post (5301) is embedded in the arc-shaped groove (5101), and the other limiting post (5301) is embedded in the straight groove (5201). The adjusting wheel (3201) meshes with the retaining tooth (5102).

6. The integrated waste gas treatment equipment for pharmaceutical applications according to claim 1, characterized in that: The oxidation furnace (1) is uniformly surrounded by heat insulation plates (12), the heat storage body (11) is installed between the two heat insulation plates (12), the top of the heat insulation plate (12) is provided with a combustion chamber (13), and the bottom of the oxidation furnace (1) is provided with an opening (14).

7. The integrated waste gas treatment equipment for pharmaceutical applications according to claim 6, characterized in that: The rotary valve (2) is provided with a rotating shaft (23), and the rotating shaft (23) is provided with an air supply channel (2301). An inlet (2302) is provided at the connection between the rotating shaft (23) and the air inlet channel (21). A distribution chamber (24) is provided at the top of the rotating shaft (23). The distribution chamber (24) is connected to the opening (14). The distribution chamber (24) includes a preheating zone (2401) and an air outlet zone (2402). A sealing plate (25) is provided between the air inlet channel (21) and the exhaust channel (22). The air supply channel (2301) is connected to the preheating zone (2401), and the exhaust channel (22) is connected to the air outlet zone (2402).

8. The waste gas treatment method of the integrated waste gas treatment equipment for pharmaceutical use according to any one of claims 1-7, wherein the steps are as follows: S1: Introduce pharmaceutical waste gas into the filter assembly (6) and switch the filter screen (66) with the appropriate mesh size according to the particle size in the pharmaceutical waste gas. S2: By comparing the pressure difference between the two ports (6101) of the filter assembly (6) with the pressure detection device (6102), it can be determined whether the filter screen (66) is blocked, so as to determine the replacement cycle of the filter screen (66). S3: After filtration, the concentration of pharmaceutical waste gas is detected. When the concentration is too high, the dilution channel (4) is opened through the pipe diameter adjustment component (5) to dilute the high concentration of pharmaceutical waste gas in the buffer chamber (3). S4: The pretreated pharmaceutical waste gas is distributed in the oxidation furnace (1) through the rotary valve (2) for oxidation and decomposition, and finally discharged as pollution-free gas.