CN206064045U - A kind of desulfurized dust collection column - Google Patents
A kind of desulfurized dust collection column Download PDFInfo
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- CN206064045U CN206064045U CN201621057068.4U CN201621057068U CN206064045U CN 206064045 U CN206064045 U CN 206064045U CN 201621057068 U CN201621057068 U CN 201621057068U CN 206064045 U CN206064045 U CN 206064045U
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Abstract
本实用新型公开了一种脱硫除尘塔,包括循环水池和塔体,所述塔体安装在循环水池内,所述塔体上端安装有排气筒,所述塔体内上端安装有除雾器,所述塔体内且位于除雾器下方等距离安装有三个支架,所述每个支架上等距离安装有多个螺旋喷嘴,所述塔体外由上向下依次设有检查孔、三级喷淋装置、二级喷淋装置和一级喷淋装置,所述塔体内且位于三个支架下方分别设有三级旋流板、二级旋流板和一级旋流板,所述塔体外右侧表面且位于一级旋流板下方安装烟气进气管。本实用新型的有益效果是,结构简单,实用性强。
The utility model discloses a desulfurization and dust removal tower, which comprises a circulating water pool and a tower body, the tower body is installed in the circulating water pool, an exhaust cylinder is installed on the upper end of the tower body, and a demister is installed on the upper end of the tower body. Three brackets are equidistantly installed in the tower body and below the demister, and multiple spiral nozzles are equidistantly installed on each bracket, and inspection holes, three-stage spray nozzles, and three-stage spray nozzles are sequentially arranged outside the tower body from top to bottom. device, secondary spraying device and primary spraying device, the tower body and below the three brackets are respectively equipped with a third-stage swirl plate, a secondary swirl plate and a first-stage swirl plate, the tower outside the right The flue gas inlet pipe is installed on the side surface and under the primary swirl plate. The beneficial effect of the utility model is that the structure is simple and the practicability is strong.
Description
技术领域technical field
本实用新型涉及脱硫除尘装置,特别是一种脱硫除尘塔。The utility model relates to a desulfurization and dust removal device, in particular to a desulfurization and dust removal tower.
背景技术Background technique
在工业生产中,燃煤锅炉是必不可少的一种设备,然而燃烧产生的二氧化硫是空气污染的一项重要指标,对于地处中心城市附近的生物质锅炉,烟气中 SO2 浓度虽较低约200mg/Nm3,但仍不能满足区域控制要求,如北京市《锅炉大气污染物排放标准》 (DB11/139-2007) 二氧化硫排放浓度要求不超 20mg/Nm3。有建设烟气脱硫装置的需求。 于是,近年来大批的烟气脱硫装置应运而生,结构复杂,运行成本较高。In industrial production, coal-fired boilers are an indispensable equipment, but the sulfur dioxide produced by combustion is an important indicator of air pollution. For biomass boilers located near central cities, the concentration of SO2 in flue gas is relatively low About 200mg/Nm3, but still can not meet the regional control requirements, such as Beijing "Emission Standards of Air Pollutants for Boilers" (DB11/139-2007) the emission concentration of sulfur dioxide requires no more than 20mg/Nm3. There is a demand for the construction of flue gas desulfurization equipment. Therefore, in recent years, a large number of flue gas desulfurization devices have emerged as the times require, with complex structures and high operating costs.
实用新型内容Utility model content
本实用新型的目的是为了解决上述问题,设计了一种脱硫除尘塔。The purpose of this utility model is in order to solve the above-mentioned problem, has designed a kind of desulfurization and dedusting tower.
实现上述目的本实用新型的技术方案为,一种脱硫除尘塔,包括循环水池和塔体,所述塔体安装在循环水池内,所述塔体上端安装有排气筒,所述塔体内上端安装有除雾器,所述塔体内且位于除雾器下方等距离安装有三个支架,所述每个支架上等距离安装有多个螺旋喷嘴,所述塔体外由上向下依次设有检查孔、三级喷淋装置、二级喷淋装置和一级喷淋装置,所述塔体内且位于三个支架下方分别设有三级旋流板、二级旋流板和一级旋流板,所述塔体外右侧表面且位于一级旋流板下方安装烟气进气管。The technical scheme of the utility model to achieve the above object is, a desulfurization and dust removal tower, including a circulating water pool and a tower body, the tower body is installed in the circulating water pool, an exhaust tube is installed on the upper end of the tower body, and the upper end of the tower body is A mist eliminator is installed, and three brackets are equidistantly installed in the tower body and below the mist eliminator, and a plurality of spiral nozzles are equidistantly installed on each of the brackets. Hole, three-stage spraying device, two-stage spraying device and one-stage spraying device, the tower body and below the three brackets are respectively provided with three-stage swirl plate, two-stage swirl plate and first-stage swirl plate , the flue gas inlet pipe is installed on the right side surface of the tower outside and under the primary swirl plate.
所述每个支架上的螺旋喷嘴的个数为3个。The number of spiral nozzles on each support is 3.
所述三级喷淋装置、二级喷淋装置和一级喷淋装置之间的距离相同。The distances between the tertiary spraying device, the secondary spraying device and the primary spraying device are the same.
所述三级喷淋装置、二级喷淋装置和一级喷淋装置分别位于三个支架一侧。The third-stage spraying device, the second-stage spraying device and the first-stage spraying device are respectively located on one side of the three supports.
利用本实用新型的技术方案制作的脱硫除尘塔,此脱硫除尘塔外壳为钢制,塔体内上部布置有除雾器。塔体下部共有三级喷淋、除尘装置和旋流板组成。塔体底部与循环水池连通,这样可以有效的降低运行成本,且结构相对简单,此装置操作简单,实用性强。The desulfurization and dust removal tower manufactured by the technical scheme of the utility model has a steel outer shell, and a demister is arranged on the upper part of the tower body. The lower part of the tower consists of three stages of spraying, dust removal device and swirl plate. The bottom of the tower body is connected with the circulating water pool, which can effectively reduce the operating cost, and the structure is relatively simple. The device is easy to operate and has strong practicability.
附图说明Description of drawings
图1是本实用新型所述脱硫除尘塔的结构示意图;Fig. 1 is the structural representation of the desulfurization and dedusting tower described in the utility model;
图中,1、循环水池;2、塔体;3、排气筒;4、除雾器;5、支架;6、螺旋喷嘴;7、检查孔;8、三级喷淋装置;9、二级喷淋装置;10、一级喷淋装置;11、三级旋流板;12、二级旋流板;13、一级旋流板;14、进气管。In the figure, 1. Circulating pool; 2. Tower body; 3. Exhaust tube; 4. Demister; 5. Support; 6. Spiral nozzle; 7. Inspection hole; 10. First-level spraying device; 11. Third-level swirl plate; 12. Second-level swirl plate; 13. First-level swirl plate; 14. Air intake pipe.
具体实施方式detailed description
下面结合附图对本实用新型进行具体描述,如图1所示,一种脱硫除尘塔,包括循环水池(1)和塔体(2),所述塔体(2)安装在循环水池(1)内,所述塔体(2)上端安装有排气筒(3),所述塔体(2)内上端安装有除雾器(4),所述塔体(2)内且位于除雾器(4)下方等距离安装有三个支架(5),所述每个支架(5)上等距离安装有多个螺旋喷嘴(6),所述塔体(2)外由上向下依次设有检查孔(7)、三级喷淋装置(8)、二级喷淋装置(9)和一级喷淋装置(10),所述塔体(2)内且位于三个支架(5)下方分别设有三级旋流板(11)、二级旋流板(12)和一级旋流板(13),所述塔体(2)外右侧表面且位于一级旋流板(13)下方安装烟气进气管(14);所述每个支架(5)上的螺旋喷嘴(6)的个数为3个;所述三级喷淋装置(8)、二级喷淋装置(9)和一级喷淋装置(10)之间的距离相同;所述三级喷淋装置(8)、二级喷淋装置(9)和一级喷淋装置(10)分别位于三个支架(5)一侧。The utility model will be described in detail below in conjunction with the accompanying drawings. As shown in Figure 1, a desulfurization and dust removal tower includes a circulating water pool (1) and a tower body (2), and the tower body (2) is installed on the circulating water pool (1) Inside, the upper end of the tower body (2) is equipped with an exhaust tube (3), and the upper end of the tower body (2) is equipped with a demister (4), and the tower body (2) is located in the demister (4) Three brackets (5) are installed equidistantly below each bracket (5), and a plurality of spiral nozzles (6) are installed equidistantly on each bracket (5), and the tower body (2) is sequentially arranged from top to bottom Inspection hole (7), tertiary spraying device (8), secondary spraying device (9) and primary spraying device (10), inside the tower body (2) and below the three brackets (5) The third-stage swirl plate (11), the second-stage swirl plate (12) and the first-stage swirl plate (13) are respectively provided. The outer right side surface of the tower body (2) is located on the first-stage swirl plate (13 ) to install the flue gas inlet pipe (14); the number of spiral nozzles (6) on each bracket (5) is 3; the third-stage spraying device (8), the second-stage spraying device ( The distance between 9) and the first-level spraying device (10) is the same; the third-level spraying device (8), the second-level spraying device (9) and the first-level spraying device (10) are respectively located in three brackets (5) One side.
本实施方案的特点为,塔体安装在循环水池内,塔体上端安装有排气筒,塔体内上端安装有除雾器,塔体内且位于除雾器下方等距离安装有三个支架,每个支架上等距离安装有多个螺旋喷嘴,塔体外由上向下依次设有检查孔、三级喷淋装置、二级喷淋装置和一级喷淋装置,塔体内且位于三个支架下方分别设有三级旋流板、二级旋流板和一级旋流板,塔体外右侧表面且位于一级旋流板下方安装烟气进气管,此脱硫除尘塔外壳为钢制,塔体内上部布置有除雾器。塔体下部共有三级喷淋、除尘装置和旋流板组成。塔体底部与循环水池连通,这样可以有效的降低运行成本,且结构相对简单,此装置操作简单,实用性强。The characteristics of this embodiment are that the tower body is installed in the circulating water pool, the upper end of the tower body is equipped with an exhaust tube, the upper end of the tower body is installed with a demister, and the tower body is installed with three brackets equidistantly below the demister, each There are multiple spiral nozzles installed equidistantly on the bracket. Inspection holes, third-level spraying devices, second-level spraying devices and first-level spraying devices are arranged on the tower body from top to bottom. The tower body is located under the three brackets respectively. There are three-stage swirl plates, two-stage swirl plates and first-stage swirl plates. The flue gas inlet pipe is installed on the right side surface of the tower outside and below the first-stage swirl plates. The shell of the desulfurization and dust removal tower is made of steel. The upper part is arranged with a demister. The lower part of the tower consists of three stages of spraying, dust removal device and swirl plate. The bottom of the tower body is connected with the circulating water pool, which can effectively reduce the operating cost, and the structure is relatively simple. The device is easy to operate and has strong practicability.
在本实施方案中,烟气在引风机作用下,经烟气入口进入塔体,先与塔底的循环水冲击混合,质量较大的灰尘及颗粒在重力和离心力的作用下进入循环池底部进行沉淀。含有细小颗粒或灰尘的液气混合物,继续沿塔体向上流动,进入一级旋流板,经旋流板后,在离心力的作用下,部分灰尘颗粒被甩到塔体壁上。脱掉灰尘的烟气继续上行,上行过程中与喷淋装置上的螺旋喷嘴喷出的雾状液体混合,混合后的液气混合物仍旧上行,在上行过程中液气混合物中的液体颗粒不断聚集,形成大的液滴,在重力作用下掉落下来。其它的则进入二级旋流板,经离心分离后,与二级喷淋装置喷出的雾状液体混合,混合后进入三级旋流板,再次进行离心分离。分离后的气体在上行过程中,与三级喷淋装置喷出的雾状液体混合。在经过较长距离的行进时,将近85%的液体会在重力作用下,分离出来。液气混合物中仍有15%的细小液滴未被分离出来,最后经过上部设置的除雾器,液滴经过除雾器的格栅板被吸附变成液体。气体则通过除雾器进入排气筒排入大气。In this embodiment, under the action of the induced draft fan, the flue gas enters the tower body through the flue gas inlet, and first impacts and mixes with the circulating water at the bottom of the tower, and the dust and particles with a large mass enter the bottom of the circulating pool under the action of gravity and centrifugal force Precipitate. The liquid-gas mixture containing fine particles or dust continues to flow upward along the tower body and enters the first-stage swirl plate. After passing through the swirl plate, part of the dust particles are thrown to the wall of the tower body under the action of centrifugal force. The flue gas that has been removed from the dust continues to go upwards. During the upward process, it is mixed with the mist liquid sprayed from the spiral nozzle on the spray device. The mixed liquid-gas mixture is still upward, and the liquid particles in the liquid-gas mixture continue to gather during the upward process. , forming large droplets that fall under the force of gravity. Others enter the secondary swirl plate, and after centrifugation, they are mixed with the mist liquid sprayed from the secondary spraying device, and then enter the third-stage swirl plate for centrifugal separation again. The separated gas is mixed with the mist liquid sprayed by the three-stage spraying device during the upward process. Nearly 85% of the liquid will separate under the force of gravity when traveling over a longer distance. There are still 15% of the fine droplets in the liquid-gas mixture that have not been separated, and finally pass through the demister installed on the upper part, and the droplets are absorbed into liquid after passing through the grid plate of the demister. The gas enters the exhaust pipe through the demister and is discharged into the atmosphere.
上述技术方案仅体现了本实用新型技术方案的优选技术方案,本技术领域的技术人员对其中某些部分所可能做出的一些变动均体现了本实用新型的原理,属于本实用新型的保护范围之内。The above-mentioned technical solutions only embody the preferred technical solutions of the technical solutions of the present utility model, and some changes that may be made by those skilled in the art to some parts thereof reflect the principles of the present utility model and belong to the protection scope of the present utility model within.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201621057068.4U CN206064045U (en) | 2016-09-18 | 2016-09-18 | A kind of desulfurized dust collection column |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201621057068.4U CN206064045U (en) | 2016-09-18 | 2016-09-18 | A kind of desulfurized dust collection column |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107261808A (en) * | 2017-08-03 | 2017-10-20 | 北京威肯众合环保科技有限公司 | A kind of double ultra-clean desulfurized dust collection columns of spray of the double turbulent flows of single cycle |
| CN110882618A (en) * | 2018-09-10 | 2020-03-17 | 黄骅市鑫通机械设备有限公司 | Double-tower desulfurization dust-removing equipment |
| CN116585806A (en) * | 2023-07-06 | 2023-08-15 | 北京莱比特环保科技有限公司 | Spin centrifugation deodorization tower |
| CN118807386A (en) * | 2024-07-22 | 2024-10-22 | 青岛海纳化工环保设备有限公司 | New integrated spray dehydration equipment |
-
2016
- 2016-09-18 CN CN201621057068.4U patent/CN206064045U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107261808A (en) * | 2017-08-03 | 2017-10-20 | 北京威肯众合环保科技有限公司 | A kind of double ultra-clean desulfurized dust collection columns of spray of the double turbulent flows of single cycle |
| CN110882618A (en) * | 2018-09-10 | 2020-03-17 | 黄骅市鑫通机械设备有限公司 | Double-tower desulfurization dust-removing equipment |
| CN116585806A (en) * | 2023-07-06 | 2023-08-15 | 北京莱比特环保科技有限公司 | Spin centrifugation deodorization tower |
| CN118807386A (en) * | 2024-07-22 | 2024-10-22 | 青岛海纳化工环保设备有限公司 | New integrated spray dehydration equipment |
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Address after: 061000 Houdianzi Village, Huanghua City, Cangzhou City, Hebei Province Patentee after: Huanghua Xintong Environmental Protection Technology Co.,Ltd. Address before: 061000 Houdianzi Village, Huanghua City, Cangzhou City, Hebei Province Patentee before: HUANGHUA XINTONG MECHANICAL EQUIPMENT CO.,LTD. |
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Granted publication date: 20170405 |