CN204114977U - Steam boiler tail-gas recycling device - Google Patents
Steam boiler tail-gas recycling device Download PDFInfo
- Publication number
- CN204114977U CN204114977U CN201420481838.2U CN201420481838U CN204114977U CN 204114977 U CN204114977 U CN 204114977U CN 201420481838 U CN201420481838 U CN 201420481838U CN 204114977 U CN204114977 U CN 204114977U
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- deduster
- steam boiler
- alkali lye
- heat exchanger
- silk
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Abstract
The utility model relates to one and utilizes steam boiler tail gas thermal source, reduce the steam boiler tail-gas recycling device of steam boiler tail gas dust simultaneously, it is characterized in that: it comprises heat exchanger, alkali lye deduster, silk alkali cleaning pond, wherein heat exchanger is arranged in drying room, and heat exchanger air inlet is connected with the exhaust port of steam boiler, heat exchanger gas outlet is connected with alkali lye deduster, and alkali lye deduster gas outlet is connected with chimney by air-introduced machine; Described alkali lye deduster also comprises alkali lye deduster inlet, and wherein alkali lye deduster inlet is connected by the outlet of water pump with silk alkali cleaning pond.The utility model device takes full advantage of the spent lye in the heat energy of steam boiler tail gas and silk alkali cleaning pond, simultaneously after the process of the utility model device, achieve the zero-emission of steam boiler tail gas dust, can be applied to food factory's food drying, chemical plant material dewatering and silk cocoon reeling mill give up silk dry.
Description
Technical field
The utility model relates to one and utilizes steam boiler tail gas thermal source, reduces the steam boiler tail-gas recycling device of steam boiler tail gas dust simultaneously.
Background technology
Steam boiler is the one of Industrial Boiler, in all trades and professions application all widely.The exhaust temperature that conventional vapor boiler directly discharges reaches 300 ~ 500 DEG C, does not meet national standard control overflow, and containing a large amount of dust in steam boiler tail gas, environmental pollution is serious.How utilizing steam boiler tail gas thermal source fully, realize the zero-emission of steam boiler tail gas dust simultaneously, is a research direction highly significant.
Summary of the invention
The utility model object is to provide one to utilize steam boiler tail gas thermal source, reduces the steam boiler tail-gas recycling device of steam boiler tail gas dust simultaneously.
The technical solution of the utility model is:
Steam boiler tail-gas recycling device, comprise heat exchanger, alkali lye deduster, silk alkali cleaning pond, wherein heat exchanger is arranged in drying room, heat exchanger air inlet is connected with the exhaust port of steam boiler, and heat exchanger gas outlet is connected with alkali lye deduster, and alkali lye deduster gas outlet is connected with chimney by air-introduced machine; Described alkali lye deduster also comprises alkali lye deduster inlet, and wherein alkali lye deduster inlet is connected by the outlet of water pump with silk alkali cleaning pond, and alkali lye deduster bottom has outlet to lead to sewage disposal system.
Described steam boiler is the boiler that bavin, coal or agricultural crop straw can be used to be fuel.
Described alkali lye deduster, the spent lye of being discharged by silk alkali cleaning pond cleaning dedusting, reduces smoke stack emission flue dust and dusty gas.
In order to improve the thermal efficiency in drying room, one or more groups heat exchanger can be set.
The utility model device takes full advantage of the spent lye in the heat energy of steam boiler tail gas and silk alkali cleaning pond, simultaneously after the process of the utility model device, achieves the zero-emission of steam boiler tail gas dust, has good practical value and the value of environmental protection.
The beneficial effects of the utility model:
The utility model can be applied to food factory's food drying, chemical plant material dewatering, silk cocoon reeling mill give up, and silk dries etc. needs dry enterprise, a large amount of energy can be saved, the sulfur dioxide of exhanst gas outlet is neutralized by alkali lye, decreases the pollution of sour gas to air.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure, Each part serial number name is as follows:
1, steam boiler, 2, heat exchanger air inlet, 3, heat exchanger, 4, heat exchanger gas outlet, 5, drying room, 6, alkali lye deduster, 7, alkali lye deduster inlet, 8, silk alkali cleaning pond, 9, spent lye in silk alkali cleaning pond, 10, the outlet in silk alkali cleaning pond, 11, water pump, 12, alkali lye in alkali lye deduster, 13, alkali lye deduster gas outlet, 14, air-introduced machine, 15, chimney.
Detailed description of the invention
In order to make the technical solution of the utility model and advantage clearly, below in conjunction with accompanying drawing of the present utility model, the technical solution of the utility model is clearly and completely described.
Steam boiler tail-gas recycling device, comprise heat exchanger 3, alkali lye deduster 6, silk alkali cleaning pond 8, wherein heat exchanger 3 is arranged in drying room 5, heat exchanger air inlet 4 is connected with the exhaust port of steam boiler 1, and heat exchanger gas outlet 4 is connected with alkali lye deduster 6, and alkali lye deduster gas outlet 13 is connected with chimney 15 by air-introduced machine 14; Described alkali lye deduster 6 also comprises alkali lye deduster inlet 7, and wherein alkali lye deduster inlet 7 is connected by the outlet 10 of water pump 11 with silk alkali cleaning pond, and alkali lye deduster bottom has outlet to lead to sewage disposal system.
Described steam boiler 1 uses the boiler that bavin, coal or agricultural crop straw are fuel.
Alkali lye 12 in described alkali lye deduster is the spent lye of discharge in silk alkali cleaning pond 8.
Described heat exchanger 3, in order to improve the thermal efficiency in drying room, can arrange one or more groups.
The course of work: first by water pump 11, the spent lye 9 in silk alkali cleaning pond to be drained in alkali lye deduster 6 by alkali lye deduster inlet 7, the tail gas containing a large amount of heat energy discharged by steam boiler 1 again enters in drying room heat exchanger 3 and heats to drying room 5, tail gas is by after heat exchanger 3, pass into the alkali lye 12 li in alkali lye deduster, dedusting is cleaned in alkali lye 12 in alkali lye deduster, cooling further, in company with the steam produced, causes chimney 15 by air-introduced machine 14 and emits simultaneously.
Claims (4)
1. a steam boiler tail-gas recycling device, it is characterized in that: it comprises heat exchanger (3), alkali lye deduster (6) and silk alkali cleaning pond (8), wherein heat exchanger (3) is arranged in drying room (5), heat exchanger air inlet (4) is connected with the exhaust port of steam boiler (1), heat exchanger gas outlet (4) is connected with alkali lye deduster (6), and alkali lye deduster gas outlet (13) is connected with chimney (15) by air-introduced machine (14); Described alkali lye deduster (6) also comprises alkali lye deduster inlet (7), wherein alkali lye deduster inlet (7) is connected with the outlet (10) in silk alkali cleaning pond by water pump (11), and alkali lye deduster (6) bottom has outlet to lead to sewage disposal system.
2. steam boiler tail-gas recycling device according to claim 1, is characterized in that: described steam boiler (1) uses the boiler that bavin, coal or agricultural crop straw are fuel.
3. steam boiler tail-gas recycling device according to claim 1, is characterized in that: the alkali lye (12) in described alkali lye deduster is the spent lye of discharge in silk alkali cleaning pond (8).
4. steam boiler tail-gas recycling device according to claim 1, is characterized in that: described heat exchanger (3) is one or more groups.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420481838.2U CN204114977U (en) | 2014-08-26 | 2014-08-26 | Steam boiler tail-gas recycling device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420481838.2U CN204114977U (en) | 2014-08-26 | 2014-08-26 | Steam boiler tail-gas recycling device |
Publications (1)
Publication Number | Publication Date |
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CN204114977U true CN204114977U (en) | 2015-01-21 |
Family
ID=52332281
Family Applications (1)
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CN201420481838.2U Active CN204114977U (en) | 2014-08-26 | 2014-08-26 | Steam boiler tail-gas recycling device |
Country Status (1)
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CN (1) | CN204114977U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104971572A (en) * | 2015-06-29 | 2015-10-14 | 蚌埠市现代环保设备有限公司 | Dust/waste gas purifying device |
CN107816731A (en) * | 2017-11-21 | 2018-03-20 | 无锡市洗选设备厂 | A kind of coal particles drying process device |
-
2014
- 2014-08-26 CN CN201420481838.2U patent/CN204114977U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104971572A (en) * | 2015-06-29 | 2015-10-14 | 蚌埠市现代环保设备有限公司 | Dust/waste gas purifying device |
CN107816731A (en) * | 2017-11-21 | 2018-03-20 | 无锡市洗选设备厂 | A kind of coal particles drying process device |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder |
Address after: 546300 Yizhou Zhuangge Cocoon Silk Co., Ltd. No. 68, Chengxi Development Zone, Hechi City, Guangxi Zhuang Autonomous Region Patentee after: Guangxi Zhuang Ge Cocoon Silk Co., Ltd. Address before: 546300 Yizhou Zhuangge Cocoon Silk Co., Ltd. No. 68, Chengxi Development Zone, Hechi City, Guangxi Zhuang Autonomous Region Patentee before: YIZHOU ZHUANGGE SILK CO., LTD. |
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CP01 | Change in the name or title of a patent holder |