CN201711047U - Spray catcher used for separator - Google Patents
Spray catcher used for separator Download PDFInfo
- Publication number
- CN201711047U CN201711047U CN2010202619070U CN201020261907U CN201711047U CN 201711047 U CN201711047 U CN 201711047U CN 2010202619070 U CN2010202619070 U CN 2010202619070U CN 201020261907 U CN201020261907 U CN 201020261907U CN 201711047 U CN201711047 U CN 201711047U
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- China
- Prior art keywords
- separator
- gas
- catcher used
- spray catcher
- folded plate
- Prior art date
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- Expired - Fee Related
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- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model belongs to the technical field of gas purifying equipment and discloses a spray catcher used for a separator. The main technical characteristics of the spray catcher used for the separator are as follows: the spray catcher used for the separator includes a shell provided with an air inlet and an air outlet; a louver folded plate fixed on a locating tube is arranged in the shell; and a fin is arranged on the louver folded plate. The spray catcher used for the separator provided by the utility model secretly carries air flows with drops to realize gas-liquid separation under the effect of the louver folded plate, which has large gas circulation surface, and is hard to be blocked; moreover, the spray catching efficiency is not influenced by the velocity of the gas; a manhole or a container flange is not needed to be reserved; the equipment has a simple structure and a low cost, and can be free from maintenance. The moving direction of the drops separated is vertical to the air flow; the fin leads the drops from being influenced by the air flow, and prevents the phenomena like gas-liquid carrying and cracking, etc, from happening.
Description
Technical field
The utility model belongs to the gas-purification equipment technical field, relates in particular to a kind of separator mist eliminator.
Background technology
Mist eliminator is a vitals of filter separator and whirlwind, cyclone separator, in the gas transmission and distribution engineering, be mainly used in and catch the free drop of carrying secretly in the gas, it is mainly used in and separates the drop of diameter greater than 3 μ m～5 μ m, realizes the secondary separation of gas.The wire-mesh mist extractor of current use is mainly by silk screen, and compositions such as framework and sump pit are a kind of gas-liquid separation devices efficiently.But its shortcoming be processed gas flow velocity to wire-mesh mist extractor to catch the mist effectiveness affects very big; gas flow rate is big; drop produced carry secretly, fragmentation; make and catch mist efficient and reduce greatly; when in the processed gas when entrained solids particle or stickum, easily stick to silk screen surface or inner, make constriction in flow area; system pressure drop increases, and produces vicious circle.Need periodic maintenance, on equipment, need leave manhole or container and adopt vessel flange to connect the equipment cost height.
The utility model content
Technical problem to be solved in the utility model with regard to provide a kind of simple in structure, gas communication face big, be difficult for stopping up, catching the separator mist eliminator that mist efficient is not influenced by gas flow rate.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is: comprise the housing that has air inlet, gas outlet, be provided with the blinds flap that is fixed on the positioning pipe in the described housing.
Its additional technical feature is: described blinds flap is provided with fin keel.
Separator mist eliminator provided by the utility model compared with prior art, is provided with the blinds flap that is fixed on the positioning pipe in the housing.During use, the air-flow that is entrained with drop enters blinds folded plate type mist eliminator housing by air inlet, is discharged by the gas outlet through the blinds flap.In housing, be entrained with the air-flow of drop owing to be subjected to the restriction of blinds flap, move along the direction dioptric type of blinds flap, drop can be trapped on the blinds flap when bumping against the blinds flap, simultaneously, be subjected to the influence of air-flow again, rest in the groove of fin keel and blinds flap, and constantly accumulate and increase, when reaching one, volume regularly falls by gravity own, flow into downspout, finally enter fluid collection chamber, and realize gas-liquid separator.Gas enters blinds folded plate type mist eliminator, and the number of times that the direction of gas flow changes is many more, and the efficient of drop separation is high more.Compare with wire-mesh mist extractor, blinds folded plate type mist eliminator gas communication face is big, is difficult for stopping up, and catches mist efficient and not influenced by gas flow rate, need not leave manhole or vessel flange, and device structure is simple, and cost is low, and equipment is non-maintaining.The direction of motion of the drop that is separated is vertical with air-flow, because the effect of fin keel is arranged, drop is not subjected to the influence of air-flow, enters mozzle, does not produce phenomenons such as entrained liquid, fragmentation.The gas treatment amount is big, and system pressure drop is little applied widely, and vertical and horizontal filtering separation device all can adopt
Description of drawings
Accompanying drawing is the structural representation of the utility model separator with mist eliminator.
The specific embodiment
Below in conjunction with the drawings and specific embodiments structure and the operation principle of the utility model separator with mist eliminator is described in further details.
As shown in the figure, the utility model separator comprises housing 1 with mist eliminator, and housing 1 has air inlet 2, gas outlet 3, is provided with positioning pipe 4 in the housing 1, is fixed with blinds flap 5 on the positioning pipe 4, and blinds flap 5 is provided with fin keel 6.
When the utility model separator was worked with mist eliminator, the air-flow that is entrained with drop entered blinds folded plate type mist eliminator housing 1 by air inlet 2, was discharged by gas outlet 3 through blinds flap 5.In housing 1, be entrained with the air-flow of drop owing to be subjected to the restriction of blinds flap 5, move along the direction dioptric type of blinds flap 5, drop can be trapped on the blinds flap 5 when bumping against blinds flap 5, simultaneously, be subjected to the influence of air-flow again, rest in the groove of fin keel 6 and blinds flap 5, and constantly accumulate and increase, when reaching one, volume regularly falls by gravity own, flow into downspout, finally enter fluid collection chamber, and realize gas-liquid separator.
Claims (2)
1. the separator mist eliminator comprises the housing that has air inlet, gas outlet, it is characterized in that: be provided with the blinds flap that is fixed on the positioning pipe in the described housing.
2. separator mist eliminator according to claim 1 is characterized in that: described blinds flap is provided with fin keel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202619070U CN201711047U (en) | 2010-07-19 | 2010-07-19 | Spray catcher used for separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202619070U CN201711047U (en) | 2010-07-19 | 2010-07-19 | Spray catcher used for separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201711047U true CN201711047U (en) | 2011-01-19 |
Family
ID=43457042
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202619070U Expired - Fee Related CN201711047U (en) | 2010-07-19 | 2010-07-19 | Spray catcher used for separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201711047U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102258917A (en) * | 2011-06-23 | 2011-11-30 | 哈尔滨汽轮机厂辅机工程有限公司 | Steam-water separation device for million-nuclear-power MSR (missile site radar) |
| CN104645724A (en) * | 2015-01-29 | 2015-05-27 | 东南大学 | Plate-type demister for improving demisting efficiency of small-particle-size droplets |
| WO2015143348A1 (en) | 2014-03-21 | 2015-09-24 | Veotec Americas LLC | Air intake separator systems and methods |
| WO2015196997A1 (en) * | 2014-06-25 | 2015-12-30 | 普尔利斯（中国）环保分离设备制造有限公司 | Vane-type separator with two pockets for removing liquid from gas |
| CN109499242A (en) * | 2018-11-29 | 2019-03-22 | 无锡佳龙换热器股份有限公司 | A kind of water separation device |
| CN110433636A (en) * | 2019-07-22 | 2019-11-12 | 山东聊城鲁西化工第六化肥有限公司 | A kind of chlorosulfonic acid production exhaust treatment system and processing method |
| CN115090037A (en) * | 2022-06-28 | 2022-09-23 | 长城海工装备(江苏)有限公司 | High-precision gas-liquid separation device |
-
2010
- 2010-07-19 CN CN2010202619070U patent/CN201711047U/en not_active Expired - Fee Related
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102258917A (en) * | 2011-06-23 | 2011-11-30 | 哈尔滨汽轮机厂辅机工程有限公司 | Steam-water separation device for million-nuclear-power MSR (missile site radar) |
| WO2015143348A1 (en) | 2014-03-21 | 2015-09-24 | Veotec Americas LLC | Air intake separator systems and methods |
| US10179305B2 (en) | 2014-03-21 | 2019-01-15 | Veotec Americas LLC | Air intake separator systems and methods |
| US11148087B2 (en) | 2014-03-21 | 2021-10-19 | Veotec Americas LLC | Air intake separator systems and methods |
| WO2015196997A1 (en) * | 2014-06-25 | 2015-12-30 | 普尔利斯（中国）环保分离设备制造有限公司 | Vane-type separator with two pockets for removing liquid from gas |
| CN104645724A (en) * | 2015-01-29 | 2015-05-27 | 东南大学 | Plate-type demister for improving demisting efficiency of small-particle-size droplets |
| CN104645724B (en) * | 2015-01-29 | 2016-01-27 | 东南大学 | A kind of board-like demister for improving small particle diameter droplet demisting efficiency |
| CN109499242A (en) * | 2018-11-29 | 2019-03-22 | 无锡佳龙换热器股份有限公司 | A kind of water separation device |
| CN110433636A (en) * | 2019-07-22 | 2019-11-12 | 山东聊城鲁西化工第六化肥有限公司 | A kind of chlorosulfonic acid production exhaust treatment system and processing method |
| CN110433636B (en) * | 2019-07-22 | 2021-07-30 | 山东聊城鲁西化工第六化肥有限公司 | Chlorosulfonic acid production tail gas treatment system and method |
| CN115090037A (en) * | 2022-06-28 | 2022-09-23 | 长城海工装备(江苏)有限公司 | High-precision gas-liquid separation device |
| CN115090037B (en) * | 2022-06-28 | 2024-03-26 | 长城海工装备(江苏)有限公司 | High-precision gas-liquid separation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110119 Termination date: 20140719 |
|
| EXPY | Termination of patent right or utility model |