CN203610031U - Comprehensive dust and sulfur removal equipment for waste gas - Google Patents
Comprehensive dust and sulfur removal equipment for waste gas Download PDFInfo
- Publication number
- CN203610031U CN203610031U CN201320839062.2U CN201320839062U CN203610031U CN 203610031 U CN203610031 U CN 203610031U CN 201320839062 U CN201320839062 U CN 201320839062U CN 203610031 U CN203610031 U CN 203610031U
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- waste gas
- dust
- spiral case
- housing
- spray
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Abstract
The utility model discloses comprehensive dust and sulfur removal equipment for waste gas. The equipment comprises a cyclone dust remover and a spray type sulfur remover, wherein the cyclone dust remover comprises a volute and a conical body connected to the lower part of the volute; a tangential air inlet is formed in the side surface of the volute; a central pipe is arranged in the middle of the volute; the upper part of the central pipe penetrates out of the volute; a dust outlet is formed in the lower part of the conical body; the spray type sulfur remover comprises a shell and a spraying head in the shell; an air outlet is formed in the upper end of the shell, and a drain outlet is formed in the lower end of the shell; an air inlet pipe penetrates through the side wall of the shell and extends along the center of the shell in a downward bending manner; the upper end of the central pipe of the cyclone dust remover is connected with the outer end of the air inlet pipe of the spray type sulfur remover through a connecting pipe. The equipment can be used for treating high-temperature waste gas and synchronously removing dust and sulfur, and is simple in structure and practical in function.
Description
Technical field
The utility model relates to the technical field of environmental protection, particularly relates to a kind of combined dust-eliminating, desulphurization plant for waste gas.
Background technology
In prior art, generally have through dedusting and desulfurization supervisor for the processing of industrial waste gas, the most of sack cleaner that adopts of existing equipment, sack cleaner can only be tackled the low waste gas of temperature, high-temp waste gas is easy to cloth bag to circulate bad, so just need to be in sack cleaner front portion again according to the equipment of cooling, so not only equipment has increased manyly, cooling simultaneously also will expend the energy, not very economic way, have much room for improvement.
Utility model content
The utility model is for addressing the above problem, and proposes a kind of combined dust-eliminating, desulphurization plant for waste gas.
The technical solution of the utility model is: a kind of combined dust-eliminating, desulphurization plant for waste gas, comprise cyclone dust collectors and spray devulcanizer, described cyclone dust collectors comprise spiral case, are connected to the cone of spiral case bottom, the side of spiral case is provided with tangent air inlet, spiral case middle part is provided with central tube, and central tube top passes spiral case; The bottom of cone is provided with dust-exhausting port, and described spray devulcanizer comprises the spray head in housing, housing, and housing upper end is exhaust outlet, and lower end is sewage draining exit; Blast pipe is through extending along housing center downward bending after the sidewall of housing, and the central tube upper end of cyclone dust collectors is connected by tube connector with the blast pipe outer end of spray devulcanizer.
Described spray devulcanizer middle part is provided with upper and lower two grate plates, is provided with several Ball-type packings between grate plate, and described blast pipe is through upper and lower two grate plates.
Described blast pipe lower end is provided with bar shaped cloth air port for one week.
The beneficial effects of the utility model
Combined dust-eliminating, the desulphurization plant for waste gas of this utility model, can process high-temp waste gas, and synchronously complete dedusting and desulfurization, simple in structure, practical function.
Accompanying drawing explanation
Fig. 1 is the structural principle schematic diagram of this combined dust-eliminating, desulphurization plant for waste gas;
1. air inlets in figure, 2. dust-exhausting port, 3. cone, 4. spiral case, 5. tube connector, 6. central tube, 7. spray head, 8. housing, 9. exhaust outlet, 10. bead, 11. air inlet pipe, 12. cloth air ports, 13. sewage draining exits of spray devulcanizer.
The specific embodiment
Embodiment: referring to Fig. 1, a kind of combined dust-eliminating, desulphurization plant for waste gas in figure, comprise cyclone dust collectors and spray devulcanizer, described cyclone dust collectors comprise spiral case, are connected to the cone of spiral case bottom, the side of spiral case is provided with tangent air inlet, spiral case middle part is provided with central tube, and central tube top passes spiral case; The bottom of cone is provided with dust-exhausting port, and described spray devulcanizer comprises the spray head in housing, housing, and housing upper end is exhaust outlet, and lower end is sewage draining exit; Blast pipe is through extending along housing center downward bending after the sidewall of housing, and the central tube upper end of cyclone dust collectors is connected by tube connector with the blast pipe outer end of spray devulcanizer.Described spray devulcanizer middle part is provided with upper and lower two grate plates, is provided with several Ball-type packings between grate plate, and Ball-type packing can increase the contact area of water and waste gas, promotes reaction efficiency, and described blast pipe is through upper and lower two grate plates.Described blast pipe lower end is provided with bar shaped cloth air port for one week, can make like this waste gas flowing more evenly a bit in housing.
The course of work:
Waste gas enters cyclone dust collectors by the air inlet on cyclone dust collectors, centrifugal action by High Rotation Speed in cyclone dust collectors is discharged most dust separation from the dust-exhausting port of bottom, waste gas after dedusting passes through central tube, tube connector enters into the blast pipe of spray devulcanizer, scatter and waft to surrounding uniformly from the bar shaped cloth air port of blast pipe lower end, the limewash of the now spray head on top ejection just flows downward along bead surface, on the waste gas that wafts and dirty limewash at the surface conjunction of bead, complete the desulfurization of waste gas, simultaneously can also be by remaining dust absorption, processing clean waste gas upwards emits through exhaust outlet, limewash is carrying reacted dirt and mud shape dust is descending, discharge by sewage draining exit.
Claims (3)
1. a combined dust-eliminating for waste gas, desulphurization plant, comprise cyclone dust collectors and spray devulcanizer, it is characterized in that: described cyclone dust collectors comprise spiral case, are connected to the cone of spiral case bottom, and the side of spiral case is provided with tangent air inlet, spiral case middle part is provided with central tube, and central tube top passes spiral case; The bottom of cone is provided with dust-exhausting port, and described spray devulcanizer comprises the spray head in housing, housing, and housing upper end is exhaust outlet, and lower end is sewage draining exit; Blast pipe is through extending along housing center downward bending after the sidewall of housing, and the central tube upper end of cyclone dust collectors is connected by tube connector with the blast pipe outer end of spray devulcanizer.
2. combined dust-eliminating, desulphurization plant for waste gas according to claim 1, is characterized in that: described spray devulcanizer middle part is provided with upper and lower two grate plates, is provided with several Ball-type packings between grate plate, and described blast pipe is through upper and lower two grate plates.
3. combined dust-eliminating, desulphurization plant for waste gas according to claim 1, is characterized in that: described blast pipe lower end is provided with bar shaped cloth air port for one week.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201320839062.2U CN203610031U (en) | 2013-12-19 | 2013-12-19 | Comprehensive dust and sulfur removal equipment for waste gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320839062.2U CN203610031U (en) | 2013-12-19 | 2013-12-19 | Comprehensive dust and sulfur removal equipment for waste gas |
Publications (1)
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CN203610031U true CN203610031U (en) | 2014-05-28 |
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Family Applications (1)
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CN201320839062.2U Expired - Fee Related CN203610031U (en) | 2013-12-19 | 2013-12-19 | Comprehensive dust and sulfur removal equipment for waste gas |
Country Status (1)
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CN (1) | CN203610031U (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107497277A (en) * | 2017-10-10 | 2017-12-22 | 佛山市宝粤美科技有限公司 | A kind of desulfurizer |
CN111013388A (en) * | 2019-12-30 | 2020-04-17 | 上海德创海洋环境科技有限公司 | Ship tail gas washing tower with direct discharging function |
CN112535939A (en) * | 2020-11-24 | 2021-03-23 | 安徽格绿恩环保工程科技有限公司 | Circulating desulfurizing tower for double-alkali desulfurization for sludge brickmaking |
CN112535938A (en) * | 2020-11-24 | 2021-03-23 | 安徽格绿恩环保工程科技有限公司 | Boiling type dust removal desulfurizing tower for dual-alkali desulfurization |
CN112588093A (en) * | 2020-11-24 | 2021-04-02 | 安徽格绿恩环保工程科技有限公司 | Double-alkali desulfurization process |
-
2013
- 2013-12-19 CN CN201320839062.2U patent/CN203610031U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107497277A (en) * | 2017-10-10 | 2017-12-22 | 佛山市宝粤美科技有限公司 | A kind of desulfurizer |
CN111013388A (en) * | 2019-12-30 | 2020-04-17 | 上海德创海洋环境科技有限公司 | Ship tail gas washing tower with direct discharging function |
CN112535939A (en) * | 2020-11-24 | 2021-03-23 | 安徽格绿恩环保工程科技有限公司 | Circulating desulfurizing tower for double-alkali desulfurization for sludge brickmaking |
CN112535938A (en) * | 2020-11-24 | 2021-03-23 | 安徽格绿恩环保工程科技有限公司 | Boiling type dust removal desulfurizing tower for dual-alkali desulfurization |
CN112588093A (en) * | 2020-11-24 | 2021-04-02 | 安徽格绿恩环保工程科技有限公司 | Double-alkali desulfurization process |
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Legal Events
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140528 Termination date: 20171219 |
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CF01 | Termination of patent right due to non-payment of annual fee |