CN107803089A - a demister - Google Patents
a demister Download PDFInfo
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- CN107803089A CN107803089A CN201711249369.6A CN201711249369A CN107803089A CN 107803089 A CN107803089 A CN 107803089A CN 201711249369 A CN201711249369 A CN 201711249369A CN 107803089 A CN107803089 A CN 107803089A
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- Prior art keywords
- defoaming
- demister
- stage
- cylinder
- ring cone
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 abstract description 7
- 239000013530 defoamer Substances 0.000 description 8
- 239000003595 mist Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000443 aerosol Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种除沫装置,尤其涉及一种用于分离气体与其所夹带雾沫的除沫器。The invention relates to a demister device, in particular to a demister used for separating gas from the entrained mist.
背景技术Background technique
在化工工业中,很多塔类设备顶部均设有除沫装置,以降低气体中雾沫的夹带量。现阶段主要的除沫设备有惯性除沫器、旋流板除沫器、丝网除沫器等,目的是从气体介质中分离悬浮的液体颗粒。但这些除沫装置大部分是单层除沫,依靠一次除沫过程除去气体中夹带的雾沫,其结构单一,除沫效率不高。In the chemical industry, a demister is installed on the top of many towers to reduce the entrainment of mist in the gas. At present, the main demisters include inertial demisters, swirl plate demisters, wire mesh demisters, etc. The purpose is to separate suspended liquid particles from the gas medium. However, most of these defoaming devices are single-layer defoaming devices, which rely on one defoaming process to remove the mist entrained in the gas. The structure is simple and the defoaming efficiency is not high.
发明内容Contents of the invention
本发明提供了一种除沫器,采用两级除沫装置实现气体介质的连续两次除沫过程,有效提高除沫效率;其中丝网除沫结构简单轻巧,除沫效果好;环锥板同时起到集液及扰流作用,进一步提高分离效果。The invention provides a demister, which uses a two-stage demister device to realize two consecutive defoaming processes of the gas medium, effectively improving the defoaming efficiency; wherein the wire mesh defoaming structure is simple and light, and the defoaming effect is good; the ring cone plate At the same time, it plays the role of collecting liquid and disturbing flow, further improving the separation effect.
为了达到上述目的,本发明采用以下技术方案实现:In order to achieve the above object, the present invention adopts the following technical solutions to realize:
一种除沫器,设置在塔体顶部气体出口处;包括一级除沫装置和二级除沫装置;所述一级除沫装置由一级除沫筒和一级环锥板组成,所述二级除沫装置由二级除沫筒和二级环锥板组成;二级除沫筒设置在气体出口下方的塔体内,二级除沫筒的下方设二级环锥板;一级除沫筒设置在二级除沫筒的外侧,其底部延伸到二级环锥板的下方,一级除沫筒的下方设一级环锥板;一级除沫筒与一级环锥板之间、二级除沫筒与二级环锥板之间留有环形间隙;一级环锥板、二级环锥板的主体均为中间高四周低的圆锥形结构,一级环锥板、二级环锥板的外圆周还设有存水槽,其中一级环锥板存水槽还连接有降液管。A demister, which is arranged at the gas outlet at the top of the tower body; includes a primary demister and a secondary demister; the primary demister is composed of a primary demister and a primary ring cone plate, the The secondary defoaming device is composed of a secondary defoamer and a secondary ring cone; The defoaming cylinder is set outside the secondary defoaming cylinder, and its bottom extends to the bottom of the secondary ring cone plate, and the primary ring cone plate is set under the primary defoaming cylinder; the primary defoaming cylinder and the primary ring cone plate There is an annular gap between the secondary demister and the secondary ring cone plate; the main bodies of the primary ring cone plate and the secondary ring cone plate are all conical structures with a high middle and low surroundings, and the primary ring cone plate 1. A water storage tank is also provided on the outer circumference of the secondary ring cone plate, wherein the water storage tank of the primary ring cone plate is also connected with a downcomer.
所述一级除沫筒、二级除沫筒均由圆形筒体和丝网组成,圆形筒体上均匀开设多个通孔,丝网围设在圆形筒体的外侧。The first-stage defoamer and the second-stage defoamer are both composed of a circular cylinder and a wire mesh. A plurality of through holes are evenly opened on the circular cylinder, and the wire mesh is arranged around the outside of the circular cylinder.
所述一级环锥板锥形结构的锥底圆与一级除沫筒圆形筒体在一级环锥板上的投影重合,二级环锥板锥形结构的锥底圆与二级除沫筒圆形筒体在二级环锥板上的投影重合。The cone bottom circle of the conical structure of the first-stage ring cone-plate coincides with the projection of the first-stage demister cylinder on the first-stage ring cone-plate, and the cone-bottom circle of the second-stage ring cone-plate conical structure coincides with the second-stage The projections of the demister cylinder body on the secondary ring cone plate are coincident.
所述一级环锥板的存水槽底部开设降液孔,降液管设于降液孔的下方,降液管为L形,其一端与降液孔连通,另一端延伸到除沫器外侧并靠近塔体内侧塔壁。The bottom of the water storage tank of the first-stage ring cone plate is provided with a downcomer hole, and the downcomer is arranged under the downcomer hole. The downcomer is L-shaped, one end of which communicates with the downcomer hole, and the other end extends to the outside of the demister And close to the tower wall inside the tower body.
与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:
1)两级除沫装置的圆形筒体外均围设有丝网,能够有效拦截气体中的大部分雾沫;1) The circular cylinder of the two-stage demisting device is surrounded by wire mesh, which can effectively intercept most of the mist in the gas;
2)经一级除沫装置除沫后,少部分雾沫未除净的气体进入二级除沫装置再次分离、除沫,大大提高除沫效率;2) After defoaming by the primary defoaming device, a small part of the unremoved gas enters the secondary defoaming device for separation and defoaming again, which greatly improves the defoaming efficiency;
3)环锥板一方面用于承载分离出的液体将其引导至存水槽,另一方面能够起到扰流作用,气体与之撞击后,能够强化气雾分离效果;3) On the one hand, the ring cone plate is used to carry the separated liquid and guide it to the water storage tank, and on the other hand, it can play a role in disrupting the flow. After the gas collides with it, it can strengthen the effect of aerosol separation;
4)结构简单轻巧,安装方便,对于大处理量气体除沫,单位处理量耗材少,降低综合成本。4) The structure is simple and light, and the installation is convenient. For the defoaming of large-capacity gas, the consumables per unit capacity are less, and the overall cost is reduced.
附图说明Description of drawings
图1是本发明所述一种除沫器的结构示意图。Fig. 1 is a schematic structural view of a demister according to the present invention.
图中:1.塔体 2.气体出口 3.一级除沫装置 4.二级除沫装置 5.圆形筒体6.丝网 7.一级环锥板 8.二级环锥板 9.存水槽 10.降液管In the figure: 1. Tower body 2. Gas outlet 3. Primary defoaming device 4. Secondary defoaming device 5. Circular cylinder 6. Wire mesh 7. Primary ring cone plate 8. Secondary ring cone plate 9 .water tank 10.downcomer
具体实施方式Detailed ways
下面结合附图对本发明的具体实施方式作进一步说明:The specific embodiment of the present invention will be further described below in conjunction with accompanying drawing:
如图1所示,本发明所述一种除沫器,设置在塔体1顶部气体出口2处;包括一级除沫装置3和二级除沫装置4;所述一级除沫装置3由一级除沫筒和一级环锥板7组成,所述二级除沫装置4由二级除沫筒和二级环锥板8组成;二级除沫筒设置在气体出口2下方的塔体1内,二级除沫筒的下方设二级环锥板8;一级除沫筒设置在二级除沫筒的外侧,其底部延伸到二级环锥板8的下方,一级除沫筒的下方设一级环锥板7;一级除沫筒与一级环锥板7之间、二级除沫筒与二级环锥板8之间留有环形间隙;一级环锥板7、二级环锥板8的主体均为中间高四周低的圆锥形结构,一级环锥板7、二级环锥板8的外圆周还设有存水槽9,其中一级环锥板7的存水槽9还连接有降液管10。As shown in Figure 1, a demister according to the present invention is arranged at the gas outlet 2 at the top of the tower body 1; includes a primary demister 3 and a secondary demister 4; the primary demister 3 It is composed of a primary defoaming cylinder and a primary ring cone plate 7, and the secondary defoaming device 4 is composed of a secondary defoaming cylinder and a secondary circular cone plate 8; the secondary defoaming cylinder is arranged below the gas outlet 2 In the tower body 1, a secondary ring cone plate 8 is arranged below the secondary demister; The first-level ring cone plate 7 is arranged below the defoamer; there is an annular gap between the first-level defoamer and the first-level ring cone 7, and between the second-level defoamer and the second-level ring cone 8; the first-level ring The main bodies of the cone plate 7 and the secondary ring cone plate 8 are conical structures that are high in the middle and low around. The water storage tank 9 of the cone plate 7 is also connected with a downcomer 10 .
所述一级除沫筒、二级除沫筒均由圆形筒体5和丝网6组成,圆形筒体5上均匀开设多个通孔,丝网6围设在圆形筒体5的外侧。The first-stage defoamer and the second-stage defoamer are both composed of a circular cylinder 5 and a wire mesh 6. A plurality of through holes are evenly opened on the circular cylinder 5, and the wire mesh 6 is surrounded by the circular cylinder 5. outside.
所述一级环锥板7锥形结构的锥底圆与一级除沫筒圆形筒体在一级环锥板7上的投影重合,二级环锥板8锥形结构的锥底圆与二级除沫筒圆形筒体在二级环锥板8上的投影重合。The cone-bottom circle of the conical structure of the first-stage ring cone plate 7 coincides with the projection of the first-stage defoaming cylinder cylinder body on the first-stage ring cone plate 7, and the cone-bottom circle of the second-stage ring cone plate 8 conical structure It coincides with the projection of the circular barrel of the secondary demisting cylinder on the secondary ring cone plate 8.
所述一级环锥板7的存水槽9底部开设降液孔,降液管10设于降液孔的下方,降液管10为L形,其一端与降液孔连通,另一端延伸到除沫器外侧并靠近塔体1内侧塔壁。The bottom of the water storage tank 9 of the first-stage ring cone plate 7 is provided with a downcomer hole, and the downcomer 10 is arranged below the downcomer hole. The downcomer 10 is L-shaped, one end communicates with the downcomer hole, and the other end extends to The outside of the demister is close to the tower wall inside the tower body 1.
塔体1内的气体介质向顶部气体出口2移动过程中,先与一级除沫器3的一级环锥板7撞击,再通过丝网6和圆形筒体5上的通孔穿过一级除沫装置3,气体介质中的雾沫大部分被一级除沫器3的丝网6拦截下来,沿圆形筒体5流淌至下方的一级环锥板7上,完成第一次除沫过程;经一次除沫后的气体介质再与二级除沫器4的二级环锥板8撞击,再通过丝网6和圆形筒体5上的通孔穿过二级除沫装置4,气体介质中剩余的雾沫大部分被二级除沫器4的丝网6拦截下来,沿圆形筒体5流淌至下方的二级环锥板8上,完成第二次除沫过程;完成两次除沫过程的气体介质从气体出口2排出。During the movement of the gas medium in the tower body 1 to the top gas outlet 2, it first collides with the first-stage ring cone plate 7 of the first-stage demister 3, and then passes through the screen 6 and the through hole on the circular cylinder 5. The first-stage demister 3, most of the mist in the gas medium is intercepted by the wire mesh 6 of the first-stage demister 3, and flows along the circular cylinder 5 to the lower first-stage ring cone plate 7, completing the first stage. The first demister process; the gas medium after the first demister collides with the secondary ring cone plate 8 of the secondary demister 4, and then passes through the screen 6 and the through hole on the circular cylinder 5 to pass through the secondary demister The mist device 4, most of the remaining mist in the gas medium is intercepted by the wire mesh 6 of the secondary demister 4, flows along the circular cylinder 5 to the secondary ring cone plate 8 below, and completes the second demister Foaming process; the gas medium that has completed two defoaming processes is discharged from the gas outlet 2.
二级环锥板8上的雾沫流入对应的存水槽9中,再溢流至一级环锥板7的存水槽9中,通过降液管10引至塔体1内侧边缘顺塔壁流下。The mist on the secondary ring cone plate 8 flows into the corresponding water storage tank 9, and then overflows into the water storage tank 9 of the primary ring cone plate 7, and is led to the inner edge of the tower body 1 through the downcomer 10 and flows down the tower wall .
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,根据本发明的技术方案及其发明构思加以等同替换或改变,都应涵盖在本发明的保护范围之内。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto, any person familiar with the technical field within the technical scope disclosed in the present invention, according to the technical solution of the present invention Any equivalent replacement or change of the inventive concepts thereof shall fall within the protection scope of the present invention.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711249369.6A CN107803089A (en) | 2017-12-01 | 2017-12-01 | a demister |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711249369.6A CN107803089A (en) | 2017-12-01 | 2017-12-01 | a demister |
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| CN107803089A true CN107803089A (en) | 2018-03-16 |
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|---|---|---|---|
| CN201711249369.6A Pending CN107803089A (en) | 2017-12-01 | 2017-12-01 | a demister |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110391033A (en) * | 2019-07-09 | 2019-10-29 | 江苏中海华核环保有限公司 | A radioactive concentrate drying device with metering device |
| CN118874171A (en) * | 2024-08-12 | 2024-11-01 | 华能陇东能源有限责任公司正宁电厂 | Defoamer and absorption tower |
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| JP2009220092A (en) * | 2008-02-22 | 2009-10-01 | Anlet Co Ltd | Filter apparatus |
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2017
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Patent Citations (8)
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|---|---|---|---|---|
| US5112375A (en) * | 1991-04-18 | 1992-05-12 | Natco | Radial vane demisting system in a separator for removing entrained droplets from a gas stream |
| US20060201873A1 (en) * | 2005-03-14 | 2006-09-14 | Smith Kevin W | Concentric C-shaped filter and screen topology |
| CN201098647Y (en) * | 2007-07-16 | 2008-08-13 | 江苏纵横浓缩干燥设备有限公司 | Centrifugal gas-liquid separator |
| JP2009220092A (en) * | 2008-02-22 | 2009-10-01 | Anlet Co Ltd | Filter apparatus |
| US20120168361A1 (en) * | 2010-06-25 | 2012-07-05 | Abbas Motakef | Cyclone induced sweeping flow separator |
| CN205084534U (en) * | 2015-10-15 | 2016-03-16 | 北京国能中电节能环保技术有限责任公司 | Small -size tertiary defroster |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110391033A (en) * | 2019-07-09 | 2019-10-29 | 江苏中海华核环保有限公司 | A radioactive concentrate drying device with metering device |
| CN118874171A (en) * | 2024-08-12 | 2024-11-01 | 华能陇东能源有限责任公司正宁电厂 | Defoamer and absorption tower |
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Application publication date: 20180316 |