CN203370420U - Reciprocating plate type water film desulphurization dust collector - Google Patents
Reciprocating plate type water film desulphurization dust collector Download PDFInfo
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- CN203370420U CN203370420U CN201320285700.0U CN201320285700U CN203370420U CN 203370420 U CN203370420 U CN 203370420U CN 201320285700 U CN201320285700 U CN 201320285700U CN 203370420 U CN203370420 U CN 203370420U
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- dust removal
- chamber
- spraying
- pipeline
- removal chamber
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 18
- 239000000428 dust Substances 0.000 title abstract description 30
- 239000007921 spray Substances 0.000 claims abstract description 28
- 238000000746 purification Methods 0.000 claims abstract description 21
- 238000005507 spraying Methods 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims 5
- 238000010410 dusting Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 11
- 230000018044 dehydration Effects 0.000 abstract description 10
- 238000006297 dehydration reaction Methods 0.000 abstract description 10
- 238000006477 desulfuration reaction Methods 0.000 abstract description 9
- 230000023556 desulfurization Effects 0.000 abstract description 9
- 238000004140 cleaning Methods 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 9
- 238000005192 partition Methods 0.000 description 5
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000010438 granite Substances 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
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- Treating Waste Gases (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
一种往复板式水膜脱硫除尘器,其结构特点是冲击混合净化管道的顶部连有进气口和进液口,冲击混合净化管道内侧壁上连有若干个倾斜向下的往复板,冲击混合净化管道的底部与喷淋除尘室的底部相连通,喷淋除尘室的顶部连有喷淋头,位于喷淋头下方的喷淋除尘室侧壁上设有若干个交错排布的倾斜向下的隔板,喷淋除尘室的上部与脱水室的上部相连通,脱水室的下部设有出气口,冲击混合净化管道和喷淋除尘室的正下方为沉灰池,沉灰池侧部连有水位控制闸阀,沉灰池顶部还连有清泥盖。它能有效提高锅炉除尘脱硫效率,设备简单易操作,材料便宜降低了设备一次性投资及运行成本。
A reciprocating plate type water film desulfurization dust collector, its structural feature is that the top of the impact mixing purification pipeline is connected with an air inlet and a liquid inlet, and the inner wall of the impact mixing purification pipeline is connected with several reciprocating plates inclined downward, and the impact mixing The bottom of the purification pipe is connected with the bottom of the spray dust removal chamber, and the top of the spray dust removal chamber is connected with a sprinkler head, and the side wall of the spray dust removal chamber below the sprinkler head is provided with several staggered downward slopes. The upper part of the spray dust removal chamber is connected with the upper part of the dehydration chamber, and the lower part of the dehydration chamber is provided with an air outlet. The impact mixing purification pipe and the spray dust removal chamber are directly below the ash settling tank, and the side of the ash settling tank is connected. There is a water level control gate valve, and a mud cleaning cover is connected to the top of the ash sink. It can effectively improve the dust removal and desulfurization efficiency of the boiler, the equipment is simple and easy to operate, and the materials are cheap, which reduces the one-time investment and operation cost of the equipment.
Description
技术领域 technical field
本实用新型涉及一种脱硫除尘器,尤其涉及一种往复板式水膜脱硫除尘器。 The utility model relates to a desulfurization dust remover, in particular to a reciprocating plate type water film desulfurization dust remover.
背景技术 Background technique
常见的燃煤锅炉烟气脱硫除尘装置有喷淋式、文丘里管式、冲击净化式等,为提高除尘效率人们通常将其串联使用,或对其进行改装但往往使其占地面积或制作成本大大提高。这样既不利于生产,也不能很好地协调维护各种脱硫除尘器设备,在实际生产中停产率非常高,这类设备的实际推广应用价值不大。 Common flue gas desulfurization and dust removal devices for coal-fired boilers include spray type, Venturi tube type, impact purification type, etc. In order to improve the dust removal efficiency, people usually use them in series, or modify them, but often make the floor area or production The cost is greatly increased. This is not conducive to production, nor can it coordinate and maintain various desulfurization and dust collector equipment well. In actual production, the shutdown rate is very high, and the actual promotion and application value of this type of equipment is not great.
发明内容 Contents of the invention
本实用新型的目的在于提供了一种往复板式水膜脱硫除尘器,它具有结构紧凑,净化效率高和使用方便的优点。 The purpose of the utility model is to provide a reciprocating plate water film desulfurization dust collector, which has the advantages of compact structure, high purification efficiency and convenient use.
本实用新型是这样来实现的,它包括进气口、冲击混合净化管道、往复板、隔板、喷淋除尘室、脱水室、出气口、清泥盖、水位控制闸阀、进液口、喷淋头和沉灰池,其特征在于冲击混合净化管道的顶部连有进气口和进液口,冲击混合净化管道内侧壁上连有若干个倾斜向下的往复板,冲击混合净化管道的底部与喷淋除尘室的底部相连通,喷淋除尘室的顶部连有喷淋头,位于喷淋头下方的喷淋除尘室侧壁上设有若干个交错排布的倾斜向下的隔板,喷淋除尘室的上部与脱水室的上部相连通,脱水室的下部设有出气口,冲击混合净化管道和喷淋除尘室的正下方为沉灰池,沉灰池侧部连有水位控制闸阀,沉灰池顶部还连有清泥盖。 The utility model is realized in this way, which includes an air inlet, an impact mixing and purification pipeline, a reciprocating plate, a partition, a spray dust removal chamber, a dehydration chamber, an air outlet, a mud cleaning cover, a water level control gate valve, a liquid inlet, a spray The shower head and ash sink are characterized in that the top of the impact mixing and purification pipeline is connected with an air inlet and a liquid inlet, and the inner wall of the impact mixing and purification pipeline is connected with several reciprocating plates inclined downward, and the bottom of the impact mixing and purification pipeline It is connected with the bottom of the spray dust removal chamber, and the top of the spray dust removal chamber is connected with a sprinkler head. The side wall of the spray dust removal chamber under the sprinkler head is provided with several staggered slanted downward partitions. The upper part of the spray dedusting chamber is connected with the upper part of the dehydration chamber, and the lower part of the dehydration chamber is provided with an air outlet. The ash sink is directly below the impact mixing purification pipeline and the spray dedust chamber, and the side of the ash sink is connected with a water level control gate valve. , There is also a clear mud cover on the top of the ash sink.
本实用新型的技术效果是:本实用新型通过多种除尘方法相结合,有效提高锅炉除尘脱硫效率,除尘器全部采用花岗岩材料,降低了设备投资成本,不仅结构劲抽,体积轻巧,还有效提高了脱硫除尘的效率,使用操作方便。 The technical effect of the utility model is: the utility model effectively improves the dust removal and desulfurization efficiency of the boiler through the combination of various dust removal methods. The dust collectors are all made of granite materials, which reduces the equipment investment cost. It improves the efficiency of desulfurization and dust removal, and is easy to use and operate.
附图说明 Description of drawings
图1为本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model.
在图中,1、进气口 2、冲击混合净化管道 3、往复板 4、隔板 5、喷淋除尘室 6、脱水室 7、出气口 8、清泥盖 9、水位控制闸阀 10、进液口 11、喷淋头 12、沉灰池。
In the figure, 1.
具体实施方式 Detailed ways
如图1所示,本实用新型是这样来实现的,它包括进气口1、冲击混合净化管道2、往复板3、隔板4、喷淋除尘室5、脱水室6、出气口7、清泥盖8、水位控制闸阀9、进液口10、喷淋头11和沉灰池12,其结构特点是冲击混合净化管道2的顶部连有进气口1和进液口10,冲击混合净化管道2内侧壁上连有若干个倾斜向下的往复板3,冲击混合净化管道2的底部与喷淋除尘室5的底部相连通,喷淋除尘室5的顶部连有喷淋头11,位于喷淋头11下方的喷淋除尘室5侧壁上设有若干个交错排布的倾斜向下的隔板4,喷淋除尘室5的上部与脱水室6的上部相连通,脱水室6的下部设有出气口7,冲击混合净化管道2和喷淋除尘室5的正下方为沉灰池12,沉灰池12侧部连有水位控制闸阀9,沉灰池12顶部还连有清泥盖8。
As shown in Figure 1, the utility model is realized in this way, it comprises
本实用新型的实施和工作原理是这样的,水和气体分别从进气口1和进液口10进入,一同高速进入冲击混合净化管道2,优于往复板3的作用,使得气体和水并充分的接触,有利于粉尘和二氧化硫的吸收。再冲击沉灰池12水面,然后从下进入喷淋除尘室5。经喷淋头11逆向喷淋后,气体从喷淋除尘室5上方进入脱水室6,从出气口7排出。其中,冲击化混合净化管道:气液一同从正上方冲击左边45度往复板3,反弹到右边往复板3。如此气体迅速改变方向,粉尘碰撞带除尘液的斜板被吸附。二氧化硫也被液气吸收。管道不应过粗,视气体流量而定;喷淋区:液体从上方喷淋,经过隔板4,形成水膜。气体从下而上,充分与水膜接触,除去杂质。
The implementation and working principle of the present utility model are such that water and gas enter from the
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104307331A (en) * | 2014-10-08 | 2015-01-28 | 泰州明锋资源再生科技有限公司 | Exhaust purification and discharge device in stainless steel acid washing sludge treatment process |
CN104436971A (en) * | 2014-12-06 | 2015-03-25 | 桂林市宏发环保设备工程有限公司 | Wet method type flue gas desulfurization, denitrification and demercuration integrated granite dust remover |
CN107469507A (en) * | 2017-01-05 | 2017-12-15 | 杨万芬 | A kind of air purifier |
CN108379971A (en) * | 2018-05-15 | 2018-08-10 | 上海卓鼎模具有限公司 | A kind of rinsing type air purifier |
CN109224697A (en) * | 2018-08-21 | 2019-01-18 | 苏州敬天爱人环境科技有限公司 | A kind of equipment for treating industrial waste gas |
CN109985465A (en) * | 2019-04-17 | 2019-07-09 | 济南邦科清洗设备有限公司 | A kind of humidifying dedusting and purifying device for road-cleaning machinery |
CN112283848A (en) * | 2020-09-23 | 2021-01-29 | 福建求真求实科技有限公司 | Air purifier using circulating water |
-
2013
- 2013-05-23 CN CN201320285700.0U patent/CN203370420U/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104307331A (en) * | 2014-10-08 | 2015-01-28 | 泰州明锋资源再生科技有限公司 | Exhaust purification and discharge device in stainless steel acid washing sludge treatment process |
CN104436971A (en) * | 2014-12-06 | 2015-03-25 | 桂林市宏发环保设备工程有限公司 | Wet method type flue gas desulfurization, denitrification and demercuration integrated granite dust remover |
CN104436971B (en) * | 2014-12-06 | 2016-05-04 | 桂林市宏发环保设备工程有限公司 | The integrated granite duster of wet method formula flue gas desulfurization and denitrification demercuration |
CN107469507A (en) * | 2017-01-05 | 2017-12-15 | 杨万芬 | A kind of air purifier |
CN108379971A (en) * | 2018-05-15 | 2018-08-10 | 上海卓鼎模具有限公司 | A kind of rinsing type air purifier |
CN109224697A (en) * | 2018-08-21 | 2019-01-18 | 苏州敬天爱人环境科技有限公司 | A kind of equipment for treating industrial waste gas |
CN109985465A (en) * | 2019-04-17 | 2019-07-09 | 济南邦科清洗设备有限公司 | A kind of humidifying dedusting and purifying device for road-cleaning machinery |
CN112283848A (en) * | 2020-09-23 | 2021-01-29 | 福建求真求实科技有限公司 | Air purifier using circulating water |
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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: 20140101 Termination date: 20140523 |