CN202129007U - Device for treating dried tail gas of drying system in biopharmaceutical industry - Google Patents
Device for treating dried tail gas of drying system in biopharmaceutical industry Download PDFInfo
- Publication number
- CN202129007U CN202129007U CN201120191991U CN201120191991U CN202129007U CN 202129007 U CN202129007 U CN 202129007U CN 201120191991 U CN201120191991 U CN 201120191991U CN 201120191991 U CN201120191991 U CN 201120191991U CN 202129007 U CN202129007 U CN 202129007U
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- China
- Prior art keywords
- tail gas
- arranged below
- box body
- filter bag
- utility
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
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Abstract
The utility model relates to a device for treating dried tail gas of a drying system in the biopharmaceutical industry. The utility model is characterized in that the device is formed by combining a dedusting system, a dehumidifying system and a heating system sequentially through pipelines, wherein the dedusting system comprises a sealed box body; an air inlet is formed on the side surface of the box body; a lift valve system is arranged at the top of the box body; an air purifying chamber and a pulse blowing system are arranged below the lift valve system; a filter bag is arranged below the pulse blowing system; an ash bucket is arranged below the filter bag; a feed port is formed at the lower part of the ash bucket; the dehumidifying system comprises a condenser box body and a silk screen demister connected with the condenser box body; and a drafting system centrifugal fan is arranged behind the silk screen demister. The utility model integrates high-efficiency dust removal, condensing dehumidification and heating recycling organically, and solves the technical problems of secondary pollution, high operating cost and incomplete treatment in other treatment methods due to adoption of circulative reclamation.
Description
Technical field
The utility model relates to a kind of project of waste gas administration, relates in particular to a kind of bio-pharmaceuticals industry drying system oven dry treating tail gas device.
Background technology
Bio-pharmaceuticals industry drying system is the key link during the sector is produced; Drying system oven dry exhaust gas component is complicated; The particulate component of dried material is brought in more or less meeting in drying course; Like direct discharging, its foul gas that brings will cause bigger pollution to atmospheric environment, and have influence on peripheral resident's living environment.At present; In bio-pharmaceuticals industry drying system oven dry treating tail gas field; Domestic main employing alkali lye spray and charcoal absorption technology, but these two kinds of technology are brought secondary pollution easily, treatment effect is general and operating cost is bigger, so fail thorough contaminated solution problem.
Summary of the invention
The utility model main purpose is: in order to remedy liquid caustic soda spray and charcoal absorption technical deficiency, will recycle the bio-pharmaceuticals industry drying system oven dry treating tail gas device that combines with waste gas pollution control and treatment thereby provide a kind of.
The above-mentioned technical problem of the utility model mainly is able to solve through following technical proposals: a kind of bio-pharmaceuticals industry drying system oven dry treating tail gas device is characterized in that: combined through pipeline in order by dust pelletizing system, dehumidification system and heating system three parts;
Said dust pelletizing system comprises seal case, and there is air inlet the side of said casing, and poppet is arranged at the top; Air-purifying chamber and pulse jet system are arranged below the said poppet; Below the said pulse jet system filter bag is arranged, ash bucket is arranged below the filter bag, feed opening is arranged below the ash bucket;
Said dehumidification system comprises condenser casing and the mesh mist eliminator that is connected with the condenser casing, in the condenser casing, is provided with modularization condensation chunk, is provided with the exhausting system centrifugal blower at the back at mesh mist eliminator;
Said heating system comprises heater, and said heater links to each other with tail gas reuse pipeline.
The flow process of the utility model is:
Tail gas at first gets into air-purifying chamber after the air inlet through the dust pelletizing system casing and the poppet; Dust is separated in the tail gas under the pulse jet system at air-purifying chamber top and bag cage and filter bag effect; Dust after the separation gets into ash bucket, through unloading valve and feed opening it is reclaimed as regenerant; Tail gas after dust pelletizing system is handled gets into the condenser casing of dehumidifying part; By the modularization condensation chunk in the condenser casing with its cool-down dehumidification; The heater of behind the silk screen demister, delivering to heating part through the exhausting system centrifugal blower then is heated to dry temperature required, and it is got into tail gas reuse pipeline as hot-air.
The beneficial effect of the utility model is:
Characteristics to bio-pharmaceuticals industry drying system oven dry tail gas; With high-effective dust-removing, dehumidification by condensation, intensification reuse organic integration in one; Owing to adopt circulating and recovering; Overcome the secondary pollution that other processing methods exist, operating cost height and handled halfway technical barrier, and high-efficiency dust removal system provides the recovery of dried material, has realized economic benefit.The internal structure design of each system of this device is dismountable modular construction all, is convenient to upgrade and repair.Prove through practical experience; Adopt this apparatus processes drying system oven dry tail gas; Environment is significantly improved; Be the Perfected process of administering drying system tail gas such as bio-pharmaceuticals industry spray-drying, circulation baking oven, be adapted at applying in the bio-pharmaceuticals industry drying system oven dry treating tail gas field.
Description of drawings
Accompanying drawing 1 is a kind of structural representation of the utility model;
Accompanying drawing 2 is vertical views of Fig. 1.
Description of reference numerals: 1. poppet, 2. pulse jet system, 3. air-purifying chamber, 4. cat ladder; 5. dust pelletizing system casing, 6. air inlet, 7. ash bucket, 8. unloading valve and feed opening; 9. bag cage, 10. filter bag, 11. condenser casings, 12. centrifugal blowers; 13. modularization condensation chunk, 14. mesh mist eliminators, 15. heaters, 16. tail gas reuse pipelines.
The specific embodiment
Below through embodiment and combine accompanying drawing, the technical scheme of the utility model is further specified.
Embodiment:
Bio-pharmaceuticals industry drying system oven dry treating tail gas device as depicted in figs. 1 and 2; Tail gas at first gets into air-purifying chamber 3 through the air inlet 6 of dust pelletizing system casing 5 with poppet 1 back; Dust is separated in the tail gas under the pulse jet system at air-purifying chamber 3 tops 2 and bag cage 9 and filter bag 10 effects; Dust after the separation gets into ash bucket 7, through unloading valve and feed opening 8 it is reclaimed as regenerant; Tail gas after dust pelletizing system is handled gets into the condenser casing 11 of dehumidifying part; By the modularization condensation chunk 13 in the condenser casing 11 with its cool-down dehumidification; The heater 15 of behind silk screen demister 14, delivering to heating part through exhausting system centrifugal blower 12 then is heated to dry temperature required, and it is got into tail gas reuse pipeline 16 as hot-air.
Claims (1)
1. a bio-pharmaceuticals industry drying system oven dry treating tail gas device is characterized in that: combined through pipeline in order by dust pelletizing system, dehumidification system and heating system three parts;
Said dust pelletizing system comprises seal case (5); There is air inlet (6) side of said casing (5); Poppet (1) is arranged at the top, and air-purifying chamber (3) and pulse jet system (2) are arranged below the said poppet, filter bag is arranged below the said pulse jet system; Ash bucket (7) is arranged below the filter bag, feed opening (8) is arranged below the ash bucket;
Said dehumidification system comprises condenser casing (11) and the mesh mist eliminator (14) that is connected with the condenser casing, in the condenser casing, is provided with modularization condensation chunk (13), is provided with exhausting system centrifugal blower (12) at the back at mesh mist eliminator;
Said heating system comprises heater (15), and said heater links to each other with tail gas reuse pipeline (16).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201120191991U CN202129007U (en) | 2011-06-09 | 2011-06-09 | Device for treating dried tail gas of drying system in biopharmaceutical industry |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201120191991U CN202129007U (en) | 2011-06-09 | 2011-06-09 | Device for treating dried tail gas of drying system in biopharmaceutical industry |
Publications (1)
Publication Number | Publication Date |
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CN202129007U true CN202129007U (en) | 2012-02-01 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201120191991U Expired - Lifetime CN202129007U (en) | 2011-06-09 | 2011-06-09 | Device for treating dried tail gas of drying system in biopharmaceutical industry |
Country Status (1)
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CN (1) | CN202129007U (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103301743A (en) * | 2013-06-21 | 2013-09-18 | 江苏中金环保科技有限公司 | Flue gas integral dry waste removing system and flue gas waste removing and back washing method |
CN103372353A (en) * | 2012-04-25 | 2013-10-30 | 潘永地 | Quick dehumidification device |
CN104174285A (en) * | 2014-09-02 | 2014-12-03 | 常州宝利环保科技有限公司 | Device for purifying dust and aromatic hydrocarbon organic waste gas and treatment method for device |
CN107140587A (en) * | 2017-06-22 | 2017-09-08 | 江南大学 | Cargo transport hanging basket |
CN108654325A (en) * | 2018-06-14 | 2018-10-16 | 南京安伦化工科技有限公司 | One kind is for exhaust gas processing device and application method in pharmacy procedure |
-
2011
- 2011-06-09 CN CN201120191991U patent/CN202129007U/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103372353A (en) * | 2012-04-25 | 2013-10-30 | 潘永地 | Quick dehumidification device |
CN103301743A (en) * | 2013-06-21 | 2013-09-18 | 江苏中金环保科技有限公司 | Flue gas integral dry waste removing system and flue gas waste removing and back washing method |
CN104174285A (en) * | 2014-09-02 | 2014-12-03 | 常州宝利环保科技有限公司 | Device for purifying dust and aromatic hydrocarbon organic waste gas and treatment method for device |
CN107140587A (en) * | 2017-06-22 | 2017-09-08 | 江南大学 | Cargo transport hanging basket |
CN108654325A (en) * | 2018-06-14 | 2018-10-16 | 南京安伦化工科技有限公司 | One kind is for exhaust gas processing device and application method in pharmacy procedure |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term | ||
CX01 | Expiry of patent term |
Granted publication date: 20120201 |