CN203183915U - Limestone-gypsum wet flue gas desulfurization device - Google Patents
Limestone-gypsum wet flue gas desulfurization device Download PDFInfo
- Publication number
- CN203183915U CN203183915U CN 201320192408 CN201320192408U CN203183915U CN 203183915 U CN203183915 U CN 203183915U CN 201320192408 CN201320192408 CN 201320192408 CN 201320192408 U CN201320192408 U CN 201320192408U CN 203183915 U CN203183915 U CN 203183915U
- Authority
- CN
- China
- Prior art keywords
- flue gas
- limestone
- pump
- gypsum wet
- desulfurizing tower
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000003546 flue gas Substances 0.000 title claims abstract description 41
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 39
- 239000010440 gypsum Substances 0.000 title claims abstract description 14
- 229910052602 gypsum Inorganic materials 0.000 title claims abstract description 14
- 238000006477 desulfuration reaction Methods 0.000 title abstract 8
- 230000023556 desulfurization Effects 0.000 title abstract 8
- 239000002002 slurry Substances 0.000 claims abstract description 40
- 239000007788 liquid Substances 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000007921 spray Substances 0.000 claims abstract description 8
- 230000003009 desulfurizing effect Effects 0.000 claims description 22
- 241000521257 Hydrops Species 0.000 claims description 11
- 206010030113 Oedema Diseases 0.000 claims description 11
- 238000001914 filtration Methods 0.000 abstract description 7
- 239000007789 gas Substances 0.000 abstract description 4
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 231100000614 poison Toxicity 0.000 abstract 2
- 230000007096 poisonous effect Effects 0.000 abstract 2
- 238000005452 bending Methods 0.000 abstract 1
- 239000000706 filtrate Substances 0.000 abstract 1
- 235000019738 Limestone Nutrition 0.000 description 8
- 239000006028 limestone Substances 0.000 description 8
- 239000002341 toxic gas Substances 0.000 description 7
- 238000000746 purification Methods 0.000 description 5
- 239000012530 fluid Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
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- Treating Waste Gases (AREA)
Abstract
The utility model relates to a limestone-gypsum wet flue gas desulfurization device which is provided with a barrel-shaped desulfurization tower; a one-time flue gas purifying area is formed at one side of the lower part of the desulfurization tower in a bending way; the lower part of the desulfurization tower is connected with a liquid storage tank by a communicating pipeline; the lower part of the liquid storage tank is sequentially connected with a pump I, a flow meter I and the lower part of a circulating slurry pool; the circulating slurry pool is isolated from a fresh slurry pool by a clapboard; the fresh slurry pool is communicated with a plurality of spray heads by a pump II and a flow meter II; spray nets are respectively arranged among the spray heads; the spray heads are communicated with a cured liquid pool; the communicating pipeline is provided with a pump III; the upper part of the desulfurization tower is provided with a demister; a water control point is arranged on the inner tower wall at the lower part of the desulfurization tower. The limestone-gypsum wet flue gas desulfurization device can be used for absorbing and filtering poisonous gas for twice, and the filtrate and flue gas are contacted with each other for a long time and have full reaction, so that the content of the poisonous gas in the flue gas is effectively removed, and the health of people can be guaranteed.
Description
Technical field
The utility model relates to a kind of desulfurizer, especially can effectively remove the limestone-gypsum wet flue gas desulfurizer of toxic gas in the flue gas.
Background technology
At present, known desulfurizer generally can only once filter flue gas, and the time that flue gas contacts with filtered fluid is short, can not fully remove the toxic gas in the flue gas, filters incomplete flue gas and enters in the atmosphere, brings threat for people's health.
The utility model content
Can not effectively remove the problem of toxic gas in the flue gas in order to solve existing flue gas desulfur device, the utility model provides a kind of limestone-gypsum wet flue gas desulfurizer, this limestone-gypsum wet flue gas desulfurizer can carry out twice absorption and filtration to toxic gas, the time that filtered fluid contacts with flue gas is long, sufficient reacting, effectively remove to reduce the content of toxic gas in the flue gas, guaranteed people's health.
The technical scheme that its technical problem that solves the utility model adopts is: this limestone-gypsum wet flue gas desulfurizer is provided with the desulfurizing tower of tubular, bottom one lateral buckling of desulfurizing tower forms the first flue gas purifying area, the bottom of desulfurizing tower links to each other with the hydrops pond by connecting pipe, bottom, hydrops pond is connecting the pump I successively, the bottom of flowmeter I and recycle slurry liquid pool, recycle slurry liquid pool and fresh slurries pond are spaced from each other by dividing plate, dividing plate is provided with the open-work that clear liquid is seen through, be lime stone slurry in the fresh slurries pond, fresh slurries pond is communicated with a plurality of shower nozzles by pump II and flowmeter II, be provided with the spray net between each shower nozzle, shower nozzle also is connected with the slaking liquid pool, be provided with the pump III communicating pipe, in addition, the top of described desulfurizing tower is provided with demister; The inner tower wall of described desulfurizing tower bottom is provided with water yield control point, remind operating personnel with water surface control between two water yield control points, so that gas enters and the resistance when leaving liquid is not too large.During use, coal-fired flue-gas enters the primary purification district from the bottom of desulfurizing tower, reacting in primary purification district and lime stone slurry in the coal-fired flue-gas, enter desulfurizing tower top after filtering, open pump II and pump III, lime stone slurry in the fresh slurries pond and the slaking liquid in the slaking liquid pool mix with flue gas by shower nozzle, carrying out in the flue gas filtered for the second time, the cleaning flue gases that filtration is finished is discharged from desulfurizing tower top, enter atmosphere, the lime stone slurry that falls from shower nozzle enters the hydrops pond, open the pump I, the slurries in the hydrops pond enter in the recycle slurry liquid pool, and in the recycle slurry liquid pool precipitated and separated, the open-work that separated liquid supernatant sees through on the dividing plate enters fresh slurries pond, realizes the recycling of slurries.
The beneficial effects of the utility model are, this limestone-gypsum wet flue gas desulfurizer can carry out twice absorption and filtration to toxic gas, and the time that filtered fluid contacts with flue gas is long, sufficient reacting, effectively remove to reduce the content of toxic gas in the flue gas, guaranteed people's health.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples.
Fig. 1 is structural principle schematic diagram of the present utility model.
Among Fig. 1,1. slaking liquid pool, 2. pump III, 3. desulfurizing tower, 4. demister, 5. shower nozzle, 6. spray net, 7. flowmeter II, 8. pump II, 9. fresh slurries pond, 10. recycle slurry liquid pool, 11. dividing plates, 12. the flowmeter I, 13. pump I, 14. hydrops ponds, 15. primary purification districts, 16. water yield control points.
The specific embodiment
In Fig. 1, this limestone-gypsum wet flue gas desulfurizer is provided with the desulfurizing tower 3 of tubular, bottom one lateral buckling of desulfurizing tower 3 forms first flue gas purifying area 15, the bottom of desulfurizing tower 3 links to each other with hydrops pond 14 by connecting pipe, 14 bottoms, hydrops pond are connecting pump I 13 successively, the bottom of flowmeter I 12 and recycle slurry liquid pool 10, recycle slurry liquid pool 10 is spaced from each other by dividing plate 11 with fresh slurries pond 9, dividing plate 11 is provided with the open-work that clear liquid is seen through, be lime stone slurry in the fresh slurries pond 9, fresh slurries pond 9 is communicated with a plurality of shower nozzles 5 by pump II 8 and flowmeter II 7, be provided with spray net 6 between each shower nozzle 5, shower nozzle 5 also is connected with slaking liquid pool 1, be provided with pump III 2 communicating pipe, in addition, the top of described desulfurizing tower 3 is provided with demister 4; The inner tower wall of described desulfurizing tower 3 bottoms is provided with water yield control point 16, remind operating personnel with water surface control between two water yield control points 16, so that gas enters and the resistance when leaving liquid is not too large.During use, coal-fired flue-gas enters primary purification district 15 from the bottom of desulfurizing tower 3, in the coal-fired flue-gas in the primary purification district 15 with lime stone slurry reaction, enter desulfurizing tower 3 tops after filtering, open pump II 8 and pump III 2, lime stone slurry in the fresh slurries pond 9 and the slaking liquid in the slaking liquid pool 1 mix with flue gas by shower nozzle 5, carrying out in the flue gas filtered for the second time, the cleaning flue gases that filtration is finished is discharged from desulfurizing tower 3 tops, enter atmosphere, the lime stone slurry that falls from shower nozzle 5 enters hydrops pond 14, open pump I 13, the slurries in the hydrops pond 14 enter in the recycle slurry liquid pool 10, and in recycle slurry liquid pool 10 precipitated and separated, the open-work that separated liquid supernatant sees through on the dividing plate 11 enters fresh slurries pond 9, realizes the recycling of slurries.
Claims (3)
1. limestone-gypsum wet flue gas desulfurizer, this limestone-gypsum wet flue gas desulfurizer is provided with the desulfurizing tower (3) of tubular, it is characterized in that, bottom one lateral buckling of desulfurizing tower (3) forms first flue gas purifying area (15), the bottom of desulfurizing tower (3) links to each other with hydrops pond (14) by connecting pipe, bottom, hydrops pond (14) is connecting pump I (13) successively, the bottom of flowmeter I (12) and recycle slurry liquid pool (10), recycle slurry liquid pool (10) is spaced from each other by dividing plate (11) with fresh slurries pond (9), fresh slurries pond (9) is communicated with a plurality of shower nozzles (5) by pump II (8) and flowmeter II (7), be provided with spray net (6) between each shower nozzle (5), shower nozzle (5) also is connected with slaking liquid pool (1), is provided with pump III (2) communicating pipe.
2. limestone-gypsum wet flue gas desulfurizer according to claim 1 is characterized in that, described dividing plate (11) is provided with the open-work that clear liquid is seen through.
3. limestone-gypsum wet flue gas desulfurizer according to claim 1 is characterized in that, the top of described desulfurizing tower (3) is provided with demister (4); The inner tower wall of described desulfurizing tower (3) bottom is provided with water yield control point (16).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201320192408 CN203183915U (en) | 2013-04-17 | 2013-04-17 | Limestone-gypsum wet flue gas desulfurization device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201320192408 CN203183915U (en) | 2013-04-17 | 2013-04-17 | Limestone-gypsum wet flue gas desulfurization device |
Publications (1)
Publication Number | Publication Date |
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CN203183915U true CN203183915U (en) | 2013-09-11 |
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Family Applications (1)
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CN 201320192408 Expired - Fee Related CN203183915U (en) | 2013-04-17 | 2013-04-17 | Limestone-gypsum wet flue gas desulfurization device |
Country Status (1)
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CN (1) | CN203183915U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103551008A (en) * | 2013-11-13 | 2014-02-05 | 苏州依斯倍化学环保装备科技有限公司 | Washing device of volatile gas |
CN107261807A (en) * | 2017-07-27 | 2017-10-20 | 大唐环境产业集团股份有限公司 | Desulfurization filtrate recycling system |
CN108619885A (en) * | 2017-03-24 | 2018-10-09 | 中国石油化工股份有限公司 | A kind of fume desulfurizing tower and flue gas ash removal, desulfurization and wastewater treatment method |
CN111804131A (en) * | 2020-07-30 | 2020-10-23 | 威海市正大环保设备股份有限公司 | Two-stage desulfurization technology with downstream ash curtain |
-
2013
- 2013-04-17 CN CN 201320192408 patent/CN203183915U/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103551008A (en) * | 2013-11-13 | 2014-02-05 | 苏州依斯倍化学环保装备科技有限公司 | Washing device of volatile gas |
CN108619885A (en) * | 2017-03-24 | 2018-10-09 | 中国石油化工股份有限公司 | A kind of fume desulfurizing tower and flue gas ash removal, desulfurization and wastewater treatment method |
CN108619885B (en) * | 2017-03-24 | 2020-06-05 | 中国石油化工股份有限公司 | Flue gas desulfurization tower and flue gas dedusting, desulfurization and wastewater treatment method |
CN107261807A (en) * | 2017-07-27 | 2017-10-20 | 大唐环境产业集团股份有限公司 | Desulfurization filtrate recycling system |
CN111804131A (en) * | 2020-07-30 | 2020-10-23 | 威海市正大环保设备股份有限公司 | Two-stage desulfurization technology with downstream ash curtain |
CN111804131B (en) * | 2020-07-30 | 2022-02-15 | 威海市正大环保设备股份有限公司 | Downstream ash curtain two-stage desulfurization method |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130911 Termination date: 20140417 |