CN201880472U - Flue gas desulfurizing and dedusting device for industrial coal-fired boiler - Google Patents
Flue gas desulfurizing and dedusting device for industrial coal-fired boiler Download PDFInfo
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- CN201880472U CN201880472U CN2010206443763U CN201020644376U CN201880472U CN 201880472 U CN201880472 U CN 201880472U CN 2010206443763 U CN2010206443763 U CN 2010206443763U CN 201020644376 U CN201020644376 U CN 201020644376U CN 201880472 U CN201880472 U CN 201880472U
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- alkali lye
- flue gas
- lye
- venturi
- liquid
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 239000003546 flue gas Substances 0.000 title claims abstract description 22
- 230000003009 desulfurizing effect Effects 0.000 title 1
- 238000006477 desulfuration reaction Methods 0.000 claims abstract description 28
- 230000023556 desulfurization Effects 0.000 claims abstract description 28
- 239000000428 dust Substances 0.000 claims abstract description 23
- 239000007788 liquid Substances 0.000 claims abstract description 20
- 239000003513 alkali Substances 0.000 claims abstract description 16
- 238000004062 sedimentation Methods 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000002893 slag Substances 0.000 claims abstract description 10
- 239000003814 drug Substances 0.000 claims description 5
- 229940079593 drug Drugs 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims 3
- 230000008676 import Effects 0.000 claims 3
- 238000007790 scraping Methods 0.000 claims 2
- 125000006850 spacer group Chemical group 0.000 claims 2
- 238000007599 discharging Methods 0.000 claims 1
- 239000000779 smoke Substances 0.000 abstract description 15
- 238000005192 partition Methods 0.000 abstract description 9
- 238000000746 purification Methods 0.000 abstract description 5
- 238000000926 separation method Methods 0.000 abstract description 3
- 239000010797 grey water Substances 0.000 abstract description 2
- 238000001179 sorption measurement Methods 0.000 abstract description 2
- 238000005507 spraying Methods 0.000 abstract 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 9
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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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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- Treating Waste Gases (AREA)
Abstract
采用喷药脱硫、液体吸附、旋风文丘里除尘、水浴气液分离、清水净化、自动出渣的一种工业燃煤锅炉烟气脱硫除尘装置,为一圆形或方形筒状密闭体,其内由上隔板和下隔板分成脱硫室、除尘室,顶部设出烟口,底部连通沉淀池,沉淀池内设刮渣机;设有液位开关、电磁阀、碱液池、沉淀池和过滤池,碱量自动添加,而且清水和碱液均被循环利用,实现灰水、碱液双循环,达到排放标准。
An industrial coal-fired boiler flue gas desulfurization and dust removal device adopts spraying desulfurization, liquid adsorption, cyclone Venturi dust removal, water bath gas-liquid separation, water purification, and automatic slag removal. It is a round or square cylindrical closed body. It is divided into a desulfurization chamber and a dust removal chamber by the upper partition and the lower partition. The top is provided with a smoke outlet, and the bottom is connected to the sedimentation tank. The sedimentation tank is equipped with a slag scraper; In the pool, the amount of alkali is added automatically, and both clear water and lye are recycled to realize double circulation of gray water and lye, meeting the discharge standard.
Description
技术领域technical field
本实用新型涉及一种工业燃煤锅炉烟气的净化装置,尤其涉及采用液体作为分离吸附剂的一种工业燃煤锅炉烟气脱硫除尘装置。The utility model relates to a purification device for flue gas of an industrial coal-fired boiler, in particular to an industrial coal-fired boiler flue gas desulfurization and dust removal device which uses liquid as a separation adsorbent.
背景技术Background technique
燃煤/重油锅炉所产生的废气中的二氧化硫、氮氧化物和粉尘等对环境造成严重的污染,一直是环境治理的重点之一,也是环境治理中的一个难题,特别是废气中的二氧化硫和氮氧化物是很难控制的主要污染物。我国20世纪90年代上马的许多中、小型企业,例如纺织印染企业等在生产中大量使用燃油锅炉。燃油锅炉在生产过程中产生的烟尘、二氧化硫和氮氧化物给周边地区造成环境污染,根据环保要求,必须对污染的设备特别是燃油锅炉所产生的烟气进行治理。Sulfur dioxide, nitrogen oxides and dust in the waste gas produced by coal-fired/heavy oil boilers have caused serious pollution to the environment. Nitrogen oxides are major pollutants that are difficult to control. Many small and medium-sized enterprises launched in the 1990s in our country, such as textile printing and dyeing enterprises, used a large number of oil-fired boilers in production. The soot, sulfur dioxide and nitrogen oxides produced by the oil-fired boiler during the production process have caused environmental pollution to the surrounding areas. According to environmental protection requirements, the polluted equipment, especially the flue gas produced by the oil-fired boiler, must be treated.
发明内容Contents of the invention
本实用新型的目的在于针对工业燃煤锅炉烟气排放问题,提供一种脱硫除尘效果较好的工业燃煤锅炉烟气脱硫除尘装置。设有进烟口、本体、除尘室、上隔板、碱液喷雾器、工作口、脱硫室、水液喷雾器、净化室、除雾器、出烟口、进水口、碱液进口、旋风文丘管、出液口、电磁阀、液位开关、加药斗、碱液池、搅拌器、第1溶液泵、液位开关、第2溶液泵、过滤池、过滤板、沉淀池、刮渣机、转运车、聚灰斗和下搁板等。本发明为一圆形或方形筒状密闭体,顶部设出烟口,底部连通沉淀池;本体内由上隔板和下隔板分成脱硫室、除尘室;旋风文丘管上端接上隔板,旋风文丘管下端接下隔板,碱液喷雾器装于旋风文丘管上方,出烟口下方设除雾器;旋风文丘管下端出口对准聚灰斗,聚灰斗出口对准设于沉淀池内的刮渣机,沉淀池与过滤池由过滤板分隔,过滤池内溶液经第2溶液泵、电磁阀接至脱硫室的碱液进口,进碱液喷雾器;碱液池内溶液由第1溶液泵经电磁阀接至脱硫室的碱液进口,进碱液喷雾器;碱液池设搅拌器、液位开关、加药斗和电池阀;除尘室内溶液从出液口经管道流入碱液池,加药斗与碱液池之间设电池阀。The purpose of the utility model is to provide an industrial coal-fired boiler flue gas desulfurization and dust removal device with better desulfurization and dust removal effects for the problem of flue gas emission from industrial coal-fired boilers. It is equipped with smoke inlet, body, dust removal chamber, upper partition, lye sprayer, working port, desulfurization chamber, water liquid sprayer, purification room, demister, smoke outlet, water inlet, lye inlet, cyclone venturi tube , liquid outlet, solenoid valve, liquid level switch, dosing hopper, lye pool, agitator, first solution pump, liquid level switch, second solution pump, filter tank, filter plate, sedimentation tank, slag scraper, Transfer carts, ash hoppers and lower shelves, etc. The present invention is a circular or square cylindrical airtight body, with a smoke outlet at the top and a sedimentation tank at the bottom; the body is divided into a desulfurization chamber and a dust removal chamber by an upper partition and a lower partition; the upper end of the cyclone venturi tube is connected to the upper partition, The lower end of the cyclone Venturi tube is connected to the lower partition, the lye sprayer is installed above the cyclone Venturi tube, and the mist eliminator is installed under the smoke outlet; the outlet at the lower end of the cyclone Venturi tube is aligned with the ash collecting bucket, and the outlet of the ash collecting bucket is aligned with the ash collecting bucket in the sedimentation tank. The slag scraper, the sedimentation tank and the filter tank are separated by a filter plate, and the solution in the filter tank is connected to the lye inlet of the desulfurization chamber through the second solution pump and the solenoid valve, and then enters the lye sprayer; the solution in the lye pool is passed through the electromagnetic The valve is connected to the lye inlet of the desulfurization chamber and enters the lye sprayer; the lye pool is equipped with agitator, liquid level switch, dosing hopper and battery valve; A battery valve is provided between the lye pool and the lye pool.
烟气从进烟口进入除尘箱,在风压作用下,推动旋风文丘管旋转,烟气进入旋风文丘管后,在文丘里作用下,产尘尘降,灰尘颗粒通过旋风文丘管下端进到聚灰斗,落至沉淀池内刮渣机;而烟气从旋风文丘管上端被引至脱硫室;烟气在脱硫室与碱液喷雾混和,产生脱硫效果,烟气从脱硫室经除雾器得到进一步水洗净化从出烟口排出。经碱液进口进入脱硫室的碱液来自碱液池和过滤池,除尘室底部出液口与碱液池连接,旋风文丘管旋转所带出的溶液,回流至碱液池;经聚灰斗流入沉淀池的溶液,由第2溶液泵从过滤池经电磁阀、碱液进口、碱液喷雾器吸至脱硫室;碱液池加药斗根据碱液的PH值大小通过电磁阀控制而添加药粉。The flue gas enters the dust removal box from the smoke inlet, and under the action of wind pressure, the cyclone Venturi tube is driven to rotate. After the flue gas enters the cyclone Venturi tube, under the action of Venturi, dust falls, and the dust particles enter through the lower end of the cyclone Venturi tube. The ash collecting hopper falls to the slag scraper in the sedimentation tank; the flue gas is led from the upper end of the cyclone Venturi tube to the desulfurization chamber; the flue gas is mixed with the lye spray in the desulfurization chamber to produce desulfurization effect, and the flue gas passes through the demister from the desulfurization chamber It is further washed and purified and discharged from the smoke outlet. The lye that enters the desulfurization chamber through the lye inlet comes from the lye pool and the filter pool. The liquid outlet at the bottom of the dust removal chamber is connected to the lye pool, and the solution brought out by the rotation of the cyclone Venturi tube flows back to the lye pool; The solution flowing into the sedimentation tank is sucked by the second solution pump from the filter tank to the desulfurization chamber through the solenoid valve, the lye inlet, and the lye sprayer; the lye pool dosing bucket is controlled by the solenoid valve to add powder according to the PH value of the lye .
本实用新型针对燃油锅炉烟气采用喷药脱硫、液体吸附,水浴气液分离、旋风文丘里除尘,清水净化,自动出渣。不仅其排放达到环保标准,而且清水和碱液均被循环利用,实现灰水、碱液双循环。整个除尘系统运行费用低,并消除了二次污染。The utility model adopts chemical spray desulfurization, liquid adsorption, water bath gas-liquid separation, cyclone Venturi dust removal, clear water purification and automatic slag removal for the flue gas of the oil-fired boiler. Not only does its discharge meet environmental protection standards, but both clean water and lye are recycled to realize double circulation of gray water and lye. The entire dust removal system has low operating costs and eliminates secondary pollution.
附图说明Description of drawings
图1为本实用新型实施例的结构及其配套设备的连接关系示意图。Fig. 1 is a schematic diagram of the structure of the utility model embodiment and the connection relation of its supporting equipment.
图2为图1的K--K视图。Fig. 2 is a K--K view of Fig. 1 .
图3为本实用新型实施例旋风文丘管的结构示意图。Fig. 3 is a schematic structural diagram of a cyclone venturi tube according to an embodiment of the present invention.
具体实施方式Detailed ways
参见图1~3,本实用新型设有进烟口1、本体2、除尘室3、上隔板4、碱液喷雾器5、工作口6、15、脱硫室7、水液喷雾器8、净化室9、除雾气10、出烟口11、进水口12、碱液进口13、旋风文丘管14、出液口16、电磁阀17、18、20、液位开关19、25、加药斗21、碱液池22、搅拌器23、第1溶液泵24、第2溶液泵26、过滤池27、过滤板28、沉淀池29、刮渣机30、转运车31、聚灰斗32和下隔板等。Referring to Figures 1 to 3, the utility model is provided with a smoke inlet 1, a
烟气从进烟口1进入除尘室3,在风压作用下,推动旋风文丘管14的叶片144使之旋转,烟气从旋风文丘管14的进烟口142进入,在文丘里作用下,灰尘颗粒通过旋风文丘管14的排灰口141下进到聚灰斗32,落入刮渣机30,由转运车31外运;而烟气从旋风文丘管14的排气口143引至脱硫室7;烟气在脱硫室7与碱液喷雾器5喷出的碱雾混和,产生脱硫效果,烟气从脱硫室7经除雾器10得到进一步水洗净化并从出烟口11排放。经碱液进口13进入脱硫室7的碱液来自碱液池22和过滤池27;除尘室7底部出液口16与碱液池22连接,旋风文丘管14旋转所带出的溶液,回流至碱液池22;经聚灰斗32流入沉淀池29的溶液,由第2溶液泵26从过滤池27经电磁阀17、碱液进口13、碱液喷雾器5至脱硫室7;碱液池加药斗21根据碱液的PH值大小通过电磁阀20控制而添加药粉。碱液、清水得到循环使用。The smoke enters the
经测试,本实用新型实施例可达到以下主要参数。After testing, the embodiment of the utility model can achieve the following main parameters.
烟气技术参数:Flue gas technical parameters:
1.烟气成分:烟尘、SO2;1. Flue gas composition: soot, SO 2 ;
2.烟气温度:130~250℃;2. Flue gas temperature: 130~250℃;
3.粉尘浓度:1200~1500mg/Nm3。3. Dust concentration: 1200~1500mg/Nm 3 .
处理后烟气中污染物浓度(按国标GB13271-2001):Concentration of pollutants in flue gas after treatment (according to national standard GB13271-2001):
1.烟尘排放浓度≤200~150mg/m3;1. Smoke and dust emission concentration ≤ 200 ~ 150mg/m 3 ;
2.林格曼黑度:1级;2. Ringelmann blackness: level 1;
3.二氧化硫排放浓度≤1200~900mg/m3。3. Sulfur dioxide emission concentration ≤ 1200-900mg/m 3 .
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102380304A (en) * | 2011-09-12 | 2012-03-21 | 张步芳 | Desulfuration and dust removal device of industrial coal furnace |
CN102485321A (en) * | 2010-12-06 | 2012-06-06 | 张步芳 | Industrial fire coal boiler smoke desulphurization dedusting device |
CN103214118A (en) * | 2013-04-03 | 2013-07-24 | 国家电网公司 | Method for treating waste water by utilizing dust-containing smoke gas of coal-fired boiler |
WO2014079172A1 (en) * | 2012-11-23 | 2014-05-30 | 华南再生资源(中山)有限公司 | Exhaust gas treatment system |
-
2010
- 2010-12-06 CN CN2010206443763U patent/CN201880472U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102485321A (en) * | 2010-12-06 | 2012-06-06 | 张步芳 | Industrial fire coal boiler smoke desulphurization dedusting device |
CN102380304A (en) * | 2011-09-12 | 2012-03-21 | 张步芳 | Desulfuration and dust removal device of industrial coal furnace |
WO2014079172A1 (en) * | 2012-11-23 | 2014-05-30 | 华南再生资源(中山)有限公司 | Exhaust gas treatment system |
CN103214118A (en) * | 2013-04-03 | 2013-07-24 | 国家电网公司 | Method for treating waste water by utilizing dust-containing smoke gas of coal-fired boiler |
CN103214118B (en) * | 2013-04-03 | 2015-04-01 | 国家电网公司 | Method for treating waste water by utilizing dust-containing smoke gas of coal-fired boiler |
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