CN204672028U - Vertical gas dehydration coalescer - Google Patents
Vertical gas dehydration coalescer Download PDFInfo
- Publication number
- CN204672028U CN204672028U CN201520241470.7U CN201520241470U CN204672028U CN 204672028 U CN204672028 U CN 204672028U CN 201520241470 U CN201520241470 U CN 201520241470U CN 204672028 U CN204672028 U CN 204672028U
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- CN
- China
- Prior art keywords
- assembly
- housing
- coalescent
- gas
- foam removal
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The utility model discloses a kind of vertical gas dehydration coalescer, comprise housing, open the medium inlet on the downside of housing, open media outlet on the upside of housing, foam removal assembly and coalescent assembly is also fixed with in housing, foam removal assembly is fixed on the downside of coalescent assembly, and medium inlet, foam removal assembly, coalescent assembly and media outlet are communicated with formation scrubbing passage successively.In the technical program, this equipment carries out two-layer dehydration to medium.Gas is from lower end access arrangement, first the mist carried secretly in Despumation device removing gas, device bottom is deposited to by the mist under stopping, enter coalescent assembly again through the gas of demister and carry out deep layer dehydration, enter with the inside of liquid gas from Coalescence filter core, through filter core, entrained liquid is caught by filter core and is agglomerated into large drop, is flowed to below coalescent assembly and is discharged.
Description
Technical field
The utility model belongs to gas filtration purification techniques apparatus field, especially relates to a kind of vertical gas dehydration coalescer.
Background technology
In oil, natural gas, petrochemical industry, chemical industry, Coal Chemical Industry, electric power every field and production, life, relate to the air inlet requirement before device, pipeline pure qi (oxygen), need to carry out filtration, purification to oil gas, thus reach quality requirement required in production, life, but existing equipment is generally horizontal type structure, floor space is large, and due to pressure medium large, speed is fast, causes the problems such as poor filtration effect.
Utility model content
In order to solve the defect of above-mentioned purifier, the utility model proposes a kind of vertical gas dehydration coalescer.
Its technical scheme is a kind of vertical gas dehydration coalescer, comprise housing, open the medium inlet on the downside of housing, open media outlet on the upside of housing, foam removal assembly and coalescent assembly is also fixed with in housing, foam removal assembly is fixed on the downside of coalescent assembly, and medium inlet, foam removal assembly, coalescent assembly and media outlet are communicated with formation scrubbing passage successively.In the technical program, this equipment carries out two-layer dehydration to medium.Gas is from lower end access arrangement, first the mist carried secretly in Despumation device removing gas, device bottom is deposited to by the mist under stopping, enter coalescent assembly again through the gas of demister and carry out deep layer dehydration, enter with the inside of liquid gas from Coalescence filter core, through filter core, entrained liquid is caught by filter core and is agglomerated into large drop, is flowed to below coalescent assembly and is discharged.
Described foam removal assembly comprises screen pack and is arranged on the upper and lower both sides of screen pack and the fixed head be fixed on housing.In the technical program, adopt the mist carried secretly in the filter screen of mesh-like removing gas, mist is attached on the silk thread of silk screen coalescent to discharging together by silk screen obstruction, improves foam removal efficiency, and silk screen processing simultaneously is simply convenient to change and is repaired.
The Coalescence filter core that described coalescent assembly comprises the seal diaphragm together with being set to housing and is fixed on seal diaphragm, shell intracorporeal space is separated into upper and lower two chambers by seal diaphragm, and Coalescence filter core is arranged in upper chamber and its entrance is communicated with lower chambers through seal diaphragm.In the technical program, seal diaphragm prevents filtering coalescent gas without Coalescence filter core and is mixed into media outlet, and filter core filters coalescent to the further removal of impurities of the gas medium after foam removal, is discharged by coalescent large drop, improves filter efficiency.
Sewage draining exit is provided with on the downside of upper chamber and lower chambers.In the technical program, the dirt drop that foam removal assembly and coalescent assembly filtering are converged discharges housing by scrubbing mouth, ensure that the long term life of equipment.
Also content gauge is provided with above sewage draining exit.In this technology, the liquid level of content gauge monitoring soiling solution, blowing time of making rational planning for, improves service life of equipment further.
Accompanying drawing explanation
Fig. 1 is the main TV structure schematic diagram of a kind of embodiment of the present utility model;
Detailed description of the invention
Below in conjunction with specific embodiment, the utility model is described further.
Composition graphs 1, a kind of embodiment of the present utility model.
A kind of vertical gas dehydration coalescer, comprise housing 1, open the medium inlet 11 on the downside of housing, open media outlet 12 on the upside of housing, foam removal assembly 2 and coalescent assembly 3 is also fixed with in housing, foam removal assembly is fixed on the downside of coalescent assembly, and medium inlet, foam removal assembly, coalescent assembly and media outlet are communicated with formation scrubbing passage successively.In the present embodiment, described foam removal assembly comprises with screen pack 21 and is arranged on the upper and lower both sides of screen pack and is fixed in the fixed head 22 on housing.The Coalescence filter core 31 that described coalescent assembly comprises the seal diaphragm 32 together with being set to housing and is fixed on seal diaphragm, shell intracorporeal space is separated into upper and lower two chambers by seal diaphragm, and Coalescence filter core is arranged in upper chamber and its entrance is communicated with lower chambers through seal diaphragm.Sewage draining exit 4 is provided with on the downside of upper chamber and lower chambers.Content gauge 5 is also provided with above sewage draining exit.
This equipment is mainly used for each compressor station of gas gathering and transportation system and oil gas field treatment plant, object be remove in gas with drop, remove precision can reach 0.1 μm and more than, clearance can reach 99.9%.
This equipment is mainly through two-layer dehydration.Gas, from lower end access arrangement, first removes the mist carried secretly in gas through silk screen foam removal assembly, deposited to device bottom by the mist under stopping, the content gauge of bottom demonstrates the capacity of liquid, facilitates the timely sewage draining exit discharge opeing from device bottom; Enter coalescent assembly again through the gas of demister and carry out deep layer dehydration, band liquid gas enters from the inside of Coalescence filter core, and through filter core, entrained liquid is caught by filter core and is agglomerated into large drop, is finally discharged by the sewage draining exit of epicoele.This equipment major advantage is that vertical equipment floor space is little; Two-layer filtration, better effects if, economical and practical.
In sum, not whole intension of the present utility model: after this, all to have within do by utility model subject spirit any amendment, replacement until improve the projects such as upgrading, include within protection domain of the present utility model.
Claims (5)
1. vertical gas dehydration coalescer, comprise housing (1), open the medium inlet (11) on the downside of housing, open media outlet (12) on the upside of housing, it is characterized in that, foam removal assembly (2) and coalescent assembly (3) is also fixed with in housing, foam removal assembly is fixed on the downside of coalescent assembly, and medium inlet, foam removal assembly, coalescent assembly and media outlet are communicated with formation scrubbing passage successively.
2. vertical gas dehydration coalescer according to claim 1, it is characterized in that, described foam removal assembly comprises with screen pack (21) and is arranged on the upper and lower both sides of screen pack and is fixed in the fixed head (22) on housing.
3. vertical gas dehydration coalescer according to claim 1, it is characterized in that, the Coalescence filter core (31) that described coalescent assembly comprises the seal diaphragm (32) together with being set to housing and is fixed on seal diaphragm, shell intracorporeal space is separated into upper and lower two chambers by seal diaphragm, and Coalescence filter core is arranged in upper chamber and its entrance is communicated with lower chambers through seal diaphragm.
4. vertical gas dehydration coalescer according to claim 3, is characterized in that, be provided with sewage draining exit (4) on the downside of upper chamber and lower chambers.
5. vertical gas dehydration coalescer according to claim 4, is characterized in that, be also provided with content gauge (5) above sewage draining exit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520241470.7U CN204672028U (en) | 2015-04-20 | 2015-04-20 | Vertical gas dehydration coalescer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520241470.7U CN204672028U (en) | 2015-04-20 | 2015-04-20 | Vertical gas dehydration coalescer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204672028U true CN204672028U (en) | 2015-09-30 |
Family
ID=54171753
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520241470.7U Expired - Fee Related CN204672028U (en) | 2015-04-20 | 2015-04-20 | Vertical gas dehydration coalescer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204672028U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108939717A (en) * | 2018-08-31 | 2018-12-07 | 江山市双氧水有限公司 | Oxidized tail gas efficiently removes liquid/gas separator in a kind of dilute product process units of hydrogen peroxide |
-
2015
- 2015-04-20 CN CN201520241470.7U patent/CN204672028U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108939717A (en) * | 2018-08-31 | 2018-12-07 | 江山市双氧水有限公司 | Oxidized tail gas efficiently removes liquid/gas separator in a kind of dilute product process units of hydrogen peroxide |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Guo Haibo Inventor after: Zhang Yan Inventor before: Zhang Yan |
|
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: No. 1, No. 27, Zhixin Road, Haidian District, Beijing, 367 Patentee after: BEIJING CENTURY ENERGY TECHNOLOGY CORPORATION Address before: 100011 Beijing City, Xicheng District Street No. 26 Desheng Property Building No. 1 918 Patentee before: SANCHUAN CENTURY ENERGY EQUIPMENT CO., LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150930 Termination date: 20190420 |