CN202237757U - 一种燃煤烟气旋流除尘脱硫装置 - Google Patents
一种燃煤烟气旋流除尘脱硫装置 Download PDFInfo
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- CN202237757U CN202237757U CN2011203391530U CN201120339153U CN202237757U CN 202237757 U CN202237757 U CN 202237757U CN 2011203391530 U CN2011203391530 U CN 2011203391530U CN 201120339153 U CN201120339153 U CN 201120339153U CN 202237757 U CN202237757 U CN 202237757U
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- 230000003009 desulfurizing Effects 0.000 title claims abstract description 37
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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- 239000003546 flue gases Substances 0.000 title claims abstract description 20
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- 238000006477 desulfuration reactions Methods 0.000 claims abstract description 30
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- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nMzAwcHgnIGhlaWdodD0nMzAwcHgnIHZpZXdCb3g9JzAgMCAzMDAgMzAwJz4KPCEtLSBFTkQgT0YgSEVBREVSIC0tPgo8cmVjdCBzdHlsZT0nb3BhY2l0eToxLjA7ZmlsbDojRkZGRkZGO3N0cm9rZTpub25lJyB3aWR0aD0nMzAwJyBoZWlnaHQ9JzMwMCcgeD0nMCcgeT0nMCc+IDwvcmVjdD4KPHRleHQgeD0nMzguNzI2JyB5PScxNzAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5IPC90ZXh0Pgo8dGV4dCB4PSc2NC4zMzk0JyB5PScxNzAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5PPC90ZXh0Pgo8dGV4dCB4PSc5MS45Mzk0JyB5PScxNTQnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6MjZweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID4tPC90ZXh0Pgo8dGV4dCB4PScyMDAuNzAzJyB5PScxNzAnIGNsYXNzPSdhdG9tLTEnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiMzQjQxNDMnID5OPC90ZXh0Pgo8dGV4dCB4PScyMjguMzAzJyB5PScxNzAnIGNsYXNzPSdhdG9tLTEnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiMzQjQxNDMnID5hPC90ZXh0Pgo8dGV4dCB4PScyNDkuNTU3JyB5PScxNTQnIGNsYXNzPSdhdG9tLTEnIHN0eWxlPSdmb250LXNpemU6MjZweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiMzQjQxNDMnID4rPC90ZXh0Pgo8L3N2Zz4K data:image/svg+xml;base64,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 [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 14
- 238000004140 cleaning Methods 0.000 description 8
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound 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- 239000000428 dust Substances 0.000 description 7
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitric oxide Inorganic materials 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O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 7
- 239000003921 oil Substances 0.000 description 4
- 239000000779 smoke Substances 0.000 description 4
- 239000003245 coal Substances 0.000 description 3
- 229910052813 nitrogen oxide Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000003500 flue dust Substances 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- GQPLMRYTRLFLPF-UHFFFAOYSA-N nitrous Oxide Chemical compound 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- 239000007787 solid Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Abstract
一种采用液体作为吸附剂的燃煤烟气旋流除尘脱硫装置,用于燃煤锅炉烟气的净化处理。设有本体、两个旋流盘、第1除尘室、第2除尘室、水浴除尘室、脱硫室、净化室、碱液喷淋器、水液喷淋器、活性炭脱硫环、溶液混合泵、电磁阀、循环碱池、搅拌器、溶液输送泵、过滤池、刮渣机和转运车等。针对燃油锅炉烟气采用两级旋流除尘,水浴固气分离、喷淋碱液、液体吸附脱硫,湿式净化,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、碱液双循环并自动排渣。
Description
一种燃煤烟气旋流除尘脱硫装置
技术领域
[0001] 本实用新型涉及一种燃煤锅炉烟气净化装置,尤其涉及采用液体作为吸附剂的一种燃煤烟气旋流除尘脱硫装置。
背景技术
[0002] 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。
发明内容
[0003] 本实用新型的目的在于针对燃煤锅炉烟气排放问题,提供除尘脱硫效果较好的一种燃煤烟气旋流除尘脱硫装置。
[0004] 本实用新型为一圆形筒体结构,设有本体、出烟口、进烟口、工作口、旋流盘、第1 除尘室、第2除尘室、水浴除尘室、脱硫室、净化室、碱液喷淋器、水液喷淋器、活性炭脱硫环、闸阀、溶液混合泵、电磁阀、循环碱池、搅拌器、溶液输送泵、电动碟阀、止回阀、液位开关、过滤池、过滤板、刮渣机和转运车等。本实用新型本体内由活性炭脱硫环、旋流盘分隔成净化室、脱硫室、第1除尘室和第2除尘室。第2除尘室下部与水浴除尘室连通,水浴除尘室经过滤板与过滤池连通;水浴除尘室设有导流板。进烟口接入两旋流盘之间;脱硫室内碱液喷淋器接碱液进口,水液喷淋器接进水口 ;净化室内活性炭脱硫环置于搁板上,搁板平面内设有过水通孔,活性炭脱硫环上下设喷淋器;净化室顶部设出烟口 ;循环碱池的出液口经截流阀、溶液输送泵、电动碟阀、止回阀、溶液混合泵与碱液入口相接,在止回阀与过滤池之间设截流阀,循环碱池设有搅拌器、加碱斗和电磁阀。过滤池内设液位开关。刮渣机设于水浴除尘室内;刮渣机出口处设转运车;净化室、脱硫室、第1除尘室和第2除尘室均设工作口。
[0005] 与现有锅炉烟气除尘脱硫装置相比,本实用新型针对燃油锅炉烟气采用两级旋流除尘,水浴固气分离、喷淋碱液、液体吸附脱硫,湿式净化,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、自动出渣。整个除尘脱硫系统运行费用低,并消除了二次污染。
附图说明
[0006] 图1为本实用新型实施例的结构示意图。
[0007] 图2为图1的A-A向视图。
[0008] 图3为本实用新型实施例旋流盘结构示意图。[0009] 图4为本实用新型实施例叶片结构示意图。
[0010] 图5为本实用新型实施例盲板结构示意图。
[0011] 图6为本实用新型实施例挂钩结构示意图。
具体实施方式
[0012] 参见图1〜6,本实用新型设有本体1、进烟口 2、旋流盘3、脱硫室4、碱液喷淋器 5、工作口 6、8、20、22、活性炭脱硫环7、出烟口 9、净化室10、水液喷淋器11、15、进水口 12、 16、闸阀13、17、搁板14、电磁阀18、27、30、34、碱液进口 19、第1除尘室21、支撑件23、第2 除尘室24、溶液混合泵25、加碱斗26、循环碱池28、搅拌器29、溶液输送泵31、电动碟阀32、 止回阀33、液位开关35、过滤池36、过滤板37、刮渣机38、水浴除尘室39、转运车40和导流板41。
[0013] 烟气从进烟口 2进入第1除尘室21,含尘烟气进入旋流盘时产生惯性旋流,粉尘靠重力而下沉,去除粉尘后的烟气在抽风(出烟口外)作用下,进入脱硫室4,烟气与碱液喷淋器5所喷出的脱硫剂混合,烟气中的二氧化硫被吸收清除。脱硫后的粉尘回落至水浴除尘室39。
[0014] 水浴除尘室39内的灰渣由刮渣机38输送至转运车40,水浴除尘室39设有导流板41,从第2除尘室24落入的粉尘经导流板41集聚落入刮渣机,所产生的剩余烟气经第2 除尘室24、旋流盘3、第1除尘室21、旋流盘3、脱硫室4、搁板14、活性炭脱硫环7至出烟口 9 ;工作口 8、6用于装卸活性炭脱硫环7及检修水液喷淋器11 ;工作口 20、22用于检修旋流盘3及水液喷淋器15、碱液喷淋器5 ;水浴除尘池39中的碱液经过滤板37进入过滤池36, 实现碱液循环使用。过滤池36内设液位开关35,用于控制电磁阀18、30和34,确保脱硫室 4、水浴除尘室39内的碱液循环。循环碱池28内设有搅拌器29、加碱斗26和电磁阀27,根据回流碱液的PH值自动控制并添补碱量。
[0015] 在脱硫室4内脱硫后的烟气经搁板14进入活性炭脱硫环7,经水液喷淋器11、15 清洗,得到进一步净化,净化后的烟气由出烟口 9排出,水液喷淋器11、15的另一作用是清洗活性炭脱硫环7。
[0016] 参见图3〜6,两件完全相同的旋流盘3,安装方向相反,置于支撑件23上。旋流盘3设有盲板31、叶片32、箍圈33和挂钩34。挂钩34固定于盲板31上,叶片32小头插入挂钩34,叶片大头端面被两半圆型箍圈33紧固。
[0017] 经测试,本实用新型实施例可达到以下主要参数。
[0018] 烟气技术参数:
[0019] 1.烟气成分:烟尘、SO2;
[0020] 2.烟气温度:130 〜250°C ;
[0021] 3.粉尘浓度:1200 〜1500 mg/Nm3。
[0022] 处理后烟气中污染物浓度(按国标GB13271-2001):
[0023] 1.烟尘排放浓度彡200〜150mg/m3 ;
[0024] 2.林格曼黑度:1级;
[0025] 3. 二氧化硫排放浓度彡1200〜900mg/m3。
Claims (2)
1. 一种燃煤烟气旋流除尘脱硫装置,其特征在于设有本体、出烟口、进烟口、工作口、 旋流盘、第1除尘室、第2除尘室、水浴除尘室、脱硫室、净化室、碱液喷淋器、水液喷淋器、活性炭脱硫环、间阀、溶液混合泵、电磁阀、循环碱池、搅拌器、溶液输送泵、电动碟阀、止回阀、 液位开关、过滤池、过滤板、刮渣机、沉淀池和转运车;本体内由活性炭脱硫环、旋流盘分隔成净化室、脱硫室、第1除尘室和第2除尘室;第2除尘室下部与水浴除尘室连通,水浴除尘室经过滤板与过滤池连通;水浴除尘室设有导流板;进烟口接入两旋流盘之间;脱硫室内碱液喷淋器接碱液进口,水液喷淋器接进水口 ;净化室内活性炭脱硫环置于搁板上,搁板平面内设有过水通孔,活性炭脱硫环上下设喷淋器;净化室顶部设出烟口 ;循环碱池的出液口经截流阀、溶液输送泵、电动碟阀、止回阀、溶液混合泵与碱液入口相接,在止回阀与过滤池之间设截流阀,循环碱池设有搅拌器、加碱斗和电磁阀;过滤池内设液位开关,刮渣机设于水浴除尘室内,刮渣机出口处设转运车;净化室、脱硫室、第1除尘室和第2除尘室均设工作口。
2.如权利要求1所述的一种燃煤烟气旋流除尘脱硫装置,其特征在于结构相同的两个旋流盘,安装方向相反;旋流盘设有盲板、叶片、箍圈和挂购;挂钩固定于盲板上,叶片小头插入挂钩,叶片大头端面被两半圆型箍圈紧固。
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Cited By (7)
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CN102389696A (zh) * | 2011-09-12 | 2012-03-28 | 张步芳 | 燃煤烟气旋流除尘脱硫装置 |
CN103225021A (zh) * | 2013-04-28 | 2013-07-31 | 北京科技大学 | 一种粉尘提浸装置 |
CN104147878A (zh) * | 2014-07-11 | 2014-11-19 | 中国恩菲工程技术有限公司 | 湿式除尘脱硫一体化烟气净化系统、装置和方法 |
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CN102389696A (zh) * | 2011-09-12 | 2012-03-28 | 张步芳 | 燃煤烟气旋流除尘脱硫装置 |
CN103225021A (zh) * | 2013-04-28 | 2013-07-31 | 北京科技大学 | 一种粉尘提浸装置 |
CN104147878A (zh) * | 2014-07-11 | 2014-11-19 | 中国恩菲工程技术有限公司 | 湿式除尘脱硫一体化烟气净化系统、装置和方法 |
CN104147878B (zh) * | 2014-07-11 | 2016-04-13 | 中国恩菲工程技术有限公司 | 湿式除尘脱硫一体化烟气净化系统和方法 |
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