CN203315923U - Spraying type rotary acanthus water-film desulfurization dust remover - Google Patents
Spraying type rotary acanthus water-film desulfurization dust remover Download PDFInfo
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- CN203315923U CN203315923U CN2013202462010U CN201320246201U CN203315923U CN 203315923 U CN203315923 U CN 203315923U CN 2013202462010 U CN2013202462010 U CN 2013202462010U CN 201320246201 U CN201320246201 U CN 201320246201U CN 203315923 U CN203315923 U CN 203315923U
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- acanthus
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Abstract
Description
技术领域 technical field
本实用新型涉及一种脱硫除尘器,尤其涉及一种喷淋式旋转叶板水膜脱硫除尘器。 The utility model relates to a desulfurization and dust remover, in particular to a spray type rotary blade water film desulfurization and dust remover.
背景技术 Background technique
常见的湿法脱硫除尘净化设备有喷雾式、旋风式、塔板式、文丘里等。通常由于烟气中含硫,与水接触后使得除尘设备容易腐蚀。其次由于受各种因素的限制,单个除尘器的除尘效率不是很高。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 wet desulfurization dust removal and purification equipment include spray type, cyclone type, tray type, Venturi type, etc. Usually, due to the sulfur in the flue gas, the dust removal equipment is easy to corrode after contacting with water. Secondly, due to the limitation of various factors, the dust removal efficiency of a single dust collector is not very high. In order to improve the dust removal efficiency, people usually use them in series, or modify them, but often make the area occupied or the production cost greatly increased, which is not conducive to production, nor can it coordinate and maintain various desulfurization and dust collector equipment well. The stoppage rate in actual production 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喷淋式旋转叶板水膜脱硫除尘器,它具有脱硫除尘效果高,结构简单和操作使用方便的优点。 The purpose of the utility model is to provide a spray type rotary blade water film desulfurization and dust collector, which has the advantages of high desulfurization and dust removal effect, simple structure and convenient operation and use.
本实用新型是这样来实现的,它包括电机、进气口、旋转叶板、圆柱形脱尘除硫室、出气口、喷淋管和储水箱,其特征在于电机的输出轴与圆柱形脱尘除硫室内的旋转叶板的一端相连,进气口和出气口分别与圆柱形脱尘除硫室的两端连通,位于旋转叶板正上方的圆柱形脱尘除硫室内壁上连有若干个喷淋管,位于旋转叶板正下方的圆柱形脱尘除硫室内设有储水箱。 The utility model is achieved in this way, it includes a motor, an air inlet, a rotating vane, a cylindrical dedusting and desulfurizing chamber, an air outlet, a spray pipe and a water storage tank, and is characterized in that the output shaft of the motor is in contact with the cylindrical desulfurization chamber. One end of the rotating vane in the dust and desulfurization chamber is connected, and the air inlet and outlet are respectively connected with the two ends of the cylindrical dedusting and desulfurizing chamber. There are several spray pipes, and a water storage tank is arranged in the cylindrical dedusting and desulfurization chamber directly below the rotating vane.
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,有效提高锅炉除尘效率,它不仅外型结构简单紧凑,使得设备成本大为降低,并且脱硫除尘效率高,能耗低。 The technical effect of the utility model is: the utility model effectively improves the dust removal efficiency of the boiler through the combination of various dust removal methods. It not only has a simple and compact appearance structure, greatly reduces the equipment cost, but also has high desulfurization and dust removal efficiency and low energy consumption.
附图说明 Description of drawings
图1为本实用新型的俯视结构示意图。 Fig. 1 is a top view structural diagram of the utility model.
图2为本实用新型的仰视结构示意图。 Fig. 2 is a structural schematic diagram of the utility model viewed from above.
在图中,1、电机 2、进气口 3、旋转叶板 4、圆柱形脱尘除硫室 5、出气口 6、喷淋管 7、储水箱。
In the figure, 1.
具体实施方式 Detailed ways
如图1和图2所示,本实用新型是这样来实现的,它包括电机1、进气口2、旋转叶板3、圆柱形脱尘除硫室4、出气口5、喷淋管6和储水箱7,其结构特点是电机1的输出轴与圆柱形脱尘除硫室4内的旋转叶板3的一端相连,进气口2和出气口5分别与圆柱形脱尘除硫室4的两端连通,位于旋转叶板3正上方的圆柱形脱尘除硫室4内壁上连有若干个喷淋管6,位于旋转叶板3正下方的圆柱形脱尘除硫室4内设有储水箱7。
As shown in Figure 1 and Figure 2, the utility model is realized in this way, it includes a
本实用新型的工作过程是这样的,含尘气体进入进气口2之后,被旋转叶板3逆向冲击带入水中,喷淋管6喷出的除尘剂使尘粒和气体分离,气流中的粉尘粒子则被储水箱7的水膜捕获,气体通过出气口5排出圆柱形脱尘除硫室4,达到高效净化。
The working process of the utility model is such that after the dust-laden gas enters the
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Application Number | Priority Date | Filing Date | Title |
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CN2013202462010U CN203315923U (en) | 2013-05-09 | 2013-05-09 | Spraying type rotary acanthus water-film desulfurization dust remover |
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CN2013202462010U CN203315923U (en) | 2013-05-09 | 2013-05-09 | Spraying type rotary acanthus water-film desulfurization dust remover |
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CN2013202462010U Expired - Fee Related CN203315923U (en) | 2013-05-09 | 2013-05-09 | Spraying type rotary acanthus water-film desulfurization dust remover |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103752181A (en) * | 2014-01-03 | 2014-04-30 | 南昌航空大学 | Preparation method and equipment of composite hollow fiber membrane |
CN109675385A (en) * | 2019-01-16 | 2019-04-26 | 黄婷静 | A kind of moisture film method chemical industrial waste gas purifying device |
-
2013
- 2013-05-09 CN CN2013202462010U patent/CN203315923U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103752181A (en) * | 2014-01-03 | 2014-04-30 | 南昌航空大学 | Preparation method and equipment of composite hollow fiber membrane |
CN103752181B (en) * | 2014-01-03 | 2016-01-13 | 南昌航空大学 | A kind of preparation method and equipment of hollow fiber composite membrane |
CN109675385A (en) * | 2019-01-16 | 2019-04-26 | 黄婷静 | A kind of moisture film method chemical industrial waste gas purifying device |
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Date | Code | Title | Description |
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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: 20131204 Termination date: 20140509 |