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 gas Substances 0.000 title claims abstract description 20
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- 239000007788 liquid Substances 0.000 claims abstract description 21
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000004140 cleaning Methods 0.000 claims abstract description 14
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 13
- 238000001914 filtration Methods 0.000 claims abstract description 12
- 238000007790 scraping Methods 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 6
- 239000007921 spray Substances 0.000 claims description 19
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- 235000011121 sodium hydroxide Nutrition 0.000 claims description 17
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- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitric oxide Chemical compound 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O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 9
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound 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- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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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 (9)
| Publication number | Priority date | Publication date | Assignee | Title |
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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 |
| CN107029522A (zh) * | 2017-05-31 | 2017-08-11 | 四川省阳子森环保设备有限公司 | 一种烟气脱硫处理一体化装置 |
| CN108014605A (zh) * | 2017-12-14 | 2018-05-11 | 缪宜霖 | 一种废气处理系统及废气处理方法 |
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| CN109499237A (zh) * | 2018-11-19 | 2019-03-22 | 刘燕红 | 一种燃煤烟气除尘设备 |
| CN110314520A (zh) * | 2019-08-02 | 2019-10-11 | 台州锐祥机械设备有限公司 | 酸性烟气处理中和装置 |
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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 |
| CN107029522A (zh) * | 2017-05-31 | 2017-08-11 | 四川省阳子森环保设备有限公司 | 一种烟气脱硫处理一体化装置 |
| CN108014605A (zh) * | 2017-12-14 | 2018-05-11 | 缪宜霖 | 一种废气处理系统及废气处理方法 |
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| CN109499237A (zh) * | 2018-11-19 | 2019-03-22 | 刘燕红 | 一种燃煤烟气除尘设备 |
| CN110314520A (zh) * | 2019-08-02 | 2019-10-11 | 台州锐祥机械设备有限公司 | 酸性烟气处理中和装置 |
| CN113069902A (zh) * | 2021-03-31 | 2021-07-06 | 沈少华 | 一种高压细水雾脱硫处理设备 |
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