CN201880454U - 双循环烟气脱硫除尘器 - Google Patents
双循环烟气脱硫除尘器 Download PDFInfo
- Publication number
- CN201880454U CN201880454U CN2010205296305U CN201020529630U CN201880454U CN 201880454 U CN201880454 U CN 201880454U CN 2010205296305 U CN2010205296305 U CN 2010205296305U CN 201020529630 U CN201020529630 U CN 201020529630U CN 201880454 U CN201880454 U CN 201880454U
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- CN
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- Prior art keywords
- case
- dust
- flue gas
- desulfurization
- alkali
- Prior art date
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- 238000006477 desulfuration reactions Methods 0.000 title claims abstract description 32
- 230000003009 desulfurizing Effects 0.000 title claims abstract description 31
- 239000000428 dust Substances 0.000 title claims abstract description 30
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 239000003546 flue gases Substances 0.000 title claims abstract description 21
- 239000003513 alkali Substances 0.000 claims abstract description 37
- 239000011901 water Substances 0.000 claims abstract description 28
- 239000007788 liquids Substances 0.000 claims abstract description 16
- 239000000953 sodium hydroxide Substances 0.000 claims description 17
- 229910001856 sodium hydroxide Inorganic materials 0.000 claims description 17
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 17
- 238000004140 cleaning Methods 0.000 claims description 14
- 238000001914 filtration Methods 0.000 claims description 13
- 239000007921 sprays Substances 0.000 claims description 13
- 230000004087 circulation Effects 0.000 claims description 10
- 238000007790 scraping Methods 0.000 claims description 8
- 239000002893 slag Substances 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 5
- 238000004062 sedimentation Methods 0.000 claims description 2
- 239000003921 oils Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 4
- 239000007789 gases Substances 0.000 abstract description 2
- 238000000746 purification Methods 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract 2
- 230000002745 absorbent Effects 0.000 abstract 1
- 239000002250 absorbents Substances 0.000 abstract 1
- 239000010797 grey water Substances 0.000 abstract 1
- 238000005192 partition Methods 0.000 abstract 1
- 229910001890 sulfur dioxide Inorganic materials 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound 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O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 229910001874 nitric oxide Inorganic materials 0.000 description 3
- 229910052813 nitrogen oxides Inorganic materials 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- 239000003344 environmental pollutants Substances 0.000 description 2
- 239000003500 flue dust Substances 0.000 description 2
- GQPLMRYTRLFLPF-UHFFFAOYSA-N nitrous Oxide Chemical compound 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- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitric oxide Chemical compound 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O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000007787 solids 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
Abstract
一种采用液体作为分离吸附剂的双循环烟气脱硫除尘器。其本体内由隔板、搁板分隔成第1除尘箱、第2除尘箱、水浴除尘箱、脱硫箱和净化箱等。本实用新型针对燃油锅炉烟气采用多级文丘里除尘，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。
Description
双循环烟气脱硫除尘器
技术领域
[0001] 本实用新型涉及一种脱硫除尘装置，尤其是涉及一种采用液体作为分离吸附剂的 双循环烟气脱硫除尘器。
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提供一种脱硫除尘效果较好的双循环烟气脱硫除尘器。
[0004] 本实用新型设有本体、排尘文丘管、排气文丘管、隔离板、进烟口、喷淋器、进水口、 搁板、碱液进口、间阀、工作口、溶液混合泵、加碱斗、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、沉淀池和转运车等。
[0005] 本实用新型本体内由隔板、搁板分隔成第1除尘箱、第2除尘箱、水浴除尘箱、脱硫 箱和净化箱。第1除尘箱内的排气文丘管上端与第2隔板连接，下端与第1隔板连接；第2 除尘箱内的排尘文丘管的上端与第1隔板连接，下端朝水浴除尘箱；由搁板将净化箱与脱 硫箱分开，脱硫箱内碱液喷淋器接碱液进口，水液喷淋器接进水口 ；净化箱内活性炭脱硫环 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；净化箱顶设出烟口 ； 水浴除尘箱设于第2除尘箱下面，水浴除尘箱与过滤池相通，由过滤板隔开；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 机设于水浴除尘箱内；刮渣机出口处设转运车；净化箱、第1除尘箱和第2除尘箱均设工作
[0006] 与现有的锅炉脱硫除尘装置相比，本实用新型针对燃油锅炉烟气采用多级文丘里 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。整个除尘系统运行费用低，并消除了二 次污染。
附图说明
[0007] 图1为本实用新型实施例的结构及其配套设备的连接示意图。
[0008] 图2为图1的K—K视图。具体实施方式
[0009] 参见图1〜2，本实用新型设有本体1、排尘文丘管2、第1隔板3、排气文丘管4、进 烟口 5、第2隔板6、喷淋器(7、12、16、)工作口（8、22、25、）活性炭脱硫环9、出烟口 10、进 水口 (13,170搁板15、碱液进口 20、闸阀(14,180电磁阀（19、28、31、35)溶液混合泵洸、 加碱斗27、循环碱池四、搅拌器30、溶液输送泵32、电动碟阀33、止回阀34、液位开关36、过 滤池37、过滤板38、刮渣机39、水浴除尘箱40和转运车41等。
[0010] 烟气从进烟口 5进入第1除尘箱（均压箱）23，烟气经出尘文丘管2进入水浴除 尘箱40，尘粒沉入刮渣机39，烟气在抽风（出烟口外）作用下，经出气除尘管4进入脱硫箱 21，烟气与碱液喷淋器7所喷出的脱硫剂混合，烟气中的二氧化硫被吸收清除。脱硫后的尘 粒水滴沿出气文丘管4回落至水浴除尘箱40。
[0011 ] 水浴除尘箱40内的灰渣由刮渣机39输送至转运车41，碱液经过滤板38过滤进入 过滤池37，实现碱液循环使用。过滤池37内设液位开关36，用于控制电磁阀19、31和35， 确保脱硫箱21、水浴除尘箱40内的碱液循环。循环碱池四内设有搅拌器30、加碱斗27和 电磁阀观，根据回流碱液的PH值自动控制补碱量。
[0012] 在脱硫箱21内脱硫后的烟气经搁板15进入活性炭脱硫环9，经水液喷淋器12、16 清洗，得到进一步净化，净化后的烟气由出烟口 10排出，水液喷淋器12、16的另一作用是清 洗活性炭脱硫环9。
[0013] 水浴除尘箱40内的碱液经过滤板38过滤后进入过滤池37，实现碱液循环使用。
[0014] 经测试，本实用新型实施例可达到以下主要参数。
[0015] 烟气技术参数：
[0016] 1.烟气成分：烟尘、SO2 ；
[0017] 2.烟气温度：130 〜250°C ；
[0018] 3.粉尘浓度：1200 〜1500mg/Nm3。
[0019] 处理后烟气中污染物浓度（按国标GB13271-2001)：
[0020] 1.烟尘排放浓度彡200〜150mg/m3 ；
[0021] 2.林格曼黑度：1级；
[0022] 3. 二氧化硫排放浓度彡1200〜900mg/m3。
Claims (1)
1.双循环烟气脱硫除尘器，其特征在于设有本体、排尘文丘管、排气文丘管、隔离板、进 烟口、喷淋器、进水口、搁板、碱液进口、闸阀、工作口、溶液混合泵、加碱斗、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；本实用新型本体内由隔板、搁板分隔成第1除尘箱、第2除尘箱、水浴除尘箱、脱硫箱 和净化箱；第1除尘箱内的排气文丘管上端与第2隔板连接，下端与第1隔板连接；第2除 尘箱内的排尘文丘管的上端与第1隔板连接，下端朝水浴除尘箱；由搁板将净化箱与脱硫 箱分开，脱硫箱内碱液喷淋器接碱液进口，水液喷淋器接进水口 ；净化箱内活性炭脱硫环置 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；净化箱顶设出烟口 ；水 浴除尘箱设于第2除尘箱下面，水浴除尘箱与过滤池相通，由过滤板隔开；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 于水浴除尘箱内。
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102380304A (zh) * | 2011-09-12 | 2012-03-21 | 张步芳 | 工业煤炉脱硫除尘装置 |
| CN102389696A (zh) * | 2011-09-12 | 2012-03-28 | 张步芳 | 燃煤烟气旋流除尘脱硫装置 |
| CN102671493A (zh) * | 2012-05-28 | 2012-09-19 | 长城汽车股份有限公司 | 一种可移动自动除尘装置 |
| CN103372359A (zh) * | 2012-04-25 | 2013-10-30 | 陈坚诚 | 烟雾净化系统 |
| CN108954343A (zh) * | 2018-07-04 | 2018-12-07 | 福建省东南电化股份有限公司 | 一种污泥焚烧处理系统 |
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2010
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102380304A (zh) * | 2011-09-12 | 2012-03-21 | 张步芳 | 工业煤炉脱硫除尘装置 |
| CN102389696A (zh) * | 2011-09-12 | 2012-03-28 | 张步芳 | 燃煤烟气旋流除尘脱硫装置 |
| CN103372359A (zh) * | 2012-04-25 | 2013-10-30 | 陈坚诚 | 烟雾净化系统 |
| CN102671493A (zh) * | 2012-05-28 | 2012-09-19 | 长城汽车股份有限公司 | 一种可移动自动除尘装置 |
| CN108954343A (zh) * | 2018-07-04 | 2018-12-07 | 福建省东南电化股份有限公司 | 一种污泥焚烧处理系统 |
| CN108954343B (zh) * | 2018-07-04 | 2019-12-06 | 福建省东南电化股份有限公司 | 一种污泥焚烧处理系统 |
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