CN204745938U - Composite set is filtered in horizontal coalescence - Google Patents
Composite set is filtered in horizontal coalescence Download PDFInfo
- Publication number
- CN204745938U CN204745938U CN201520240002.8U CN201520240002U CN204745938U CN 204745938 U CN204745938 U CN 204745938U CN 201520240002 U CN201520240002 U CN 201520240002U CN 204745938 U CN204745938 U CN 204745938U
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- filter
- coalescer
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- chamber
- coalescence
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Abstract
The utility model discloses a composite set is filtered in horizontal coalescence, including the base, set up the coalescence filter equipment on the base, coalescence filter equipment include with the base fixed together the coalescer, fix and pass through the filter of pipeline intercommunication in the coalescer top and with the coalescer, coalescer right side head leaves has the medium export, leave at the filter top has the medium inlet, medium inlet, filter, coalescer and medium export intercommunication in proper order constitute and filter the coalescence passageway.
Description
Technical field
The utility model relates to liquid insults filtering technique apparatus field, especially relates to a kind of horizontal coalescence filtration combination unit.
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), all there is parameter index in various degree to the clean level of gas, need to carry out filtration, purification to gas, thus reaching quality requirement required in production, life, widely used separator in the market, has plenty of single-stage isolated by filtration, can only filtering solid contaminants or liquid impurity, the less effective of isolated by filtration; In order to reach good isolation of purified effect, sometimes needing multiple combinationally using, causing occupation area of equipment large, later maintenance point and potential safety hazard many; Although what have is that the effect of multi-stage separation still for the separation containing the solid, liquid impurity in assorted gas is undesirable, this multistage filtering separator is when carrying out isolated by filtration to the good gas of cleanliness factor simultaneously, remain and processed by the multistage filtering separation of multiple devices, waste cost resource and social resources greatly.
Utility model content
In order to solve the defect of above-mentioned filter, the utility model proposes a kind of horizontal coalescence filtration combination unit.
Its technical scheme is, a kind of horizontal coalescence filtration combination unit, comprise base, be arranged on the coalescence filtration device on base, described coalescence filtration device comprise be fixed together with base coalescer, to be fixed on above coalescer and with the filter of coalescer by pipeline communication, on the right side of coalescer, end socket has media outlet, and filter top has medium inlet, and medium inlet, filter, coalescer and media outlet are communicated with formation successively and filter coalescent passage.
Filter comprises housing, and enclosure interior is divided into the filter chamber be communicated with medium inlet and the plenum chamber be communicated with coalescer by sealing plate, and filter chamber's internal fixtion has filter core, and filter core is fixed on sealing plate and outlet is communicated with plenum chamber.
Coalescer comprises shell, and the output cavity that in shell, space is separated into the current stabilization chamber be communicated with filter, the coalescent chamber be communicated with current stabilization chamber and is communicated with coalescent chamber, is communicated with media outlet outside output cavity.
In coalescent chamber, be provided with Coalescence filter core and be separated filter core, Coalescence filter core is communicated with current stabilization chamber, is separated filter core and is communicated with output cavity, medium in current stabilization chamber through Coalescence filter core be separated filter core and enter output cavity.
Below coalescer, be also provided with hydrops tank, hydrops pot bottom is connected with blow-off pipe.
The medium carrying dust and spray film flows to inner surface by the outer surface of filter core and carries out filtration and coalescent, through the plenum chamber of the medium access arrangement of filter core process, the filter chamber of medium no matter on the left of equipment or the plenum chamber on the right side of equipment, all there is larger process space, medium is stopped fully at device interior, obtains best isolated by filtration effect.The pipeline that medium after metre filter is connected with coalescer by filter enters coalescer inside, equipment is divided into current stabilization chamber, coalescent chamber and output cavity by supporting clapboard by coalescer, medium is pooled to current stabilization chamber and enters Coalescence filter core inside, and flow to Coalescence filter core outside, through filtration, breakdown of emulsion, coalescent, sedimentation Four processes, by the liquid breakdown of emulsion of emulsification, then the droplet after breakdown of emulsion is agglomerated into large water drop, be deposited to housing bottom, discharged by sewage draining exit.The be not able to do in time droplet of sedimentation of part is separated filter core with flow direction, and be separated filter core and have good hydrophobicity performance, droplet is tackled completely effectively outside filter core, is again agglomerated into large water drop sedimentation thus guarantees effectively to remove moisture content.The moisture being deposited to housing bottom flows into the hydrops tank bottom coalescer, is shown, can be discharged by sewage draining exit by moisture content termly by liquid level gauge.Clean medium flows out from coalescer outlet.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of embodiment of the present utility model;
In figure, arrow line represents media flow direction.
Detailed description of the invention
Below in conjunction with specific embodiment, the utility model is described further.
As shown in Figure 1, a kind of detailed description of the invention of the present utility model.A kind of horizontal coalescence filtration combination unit, comprise base 1, be arranged on the coalescence filtration device 2 on base, described coalescence filtration device comprise be fixed together with base coalescer 3, to be fixed on above coalescer and with the filter 4 of coalescer by pipeline communication, on the right side of coalescer, end socket has media outlet 5, filter top has medium inlet 6, and medium inlet, filter, coalescer and media outlet are communicated with formation successively and filter coalescent passage.
Filter comprises housing 41, and enclosure interior is divided into the filter chamber 43 be communicated with medium inlet and the plenum chamber 44 be communicated with coalescer by sealing plate 42, and filter chamber's internal fixtion has filter core 45, and filter core is fixed on sealing plate and outlet is communicated with plenum chamber.
Coalescer comprises shell 31, and the output cavity 34 that in shell, space is separated into the current stabilization chamber 32 be communicated with filter, the coalescent chamber 33 be communicated with current stabilization chamber and is communicated with coalescent chamber, is communicated with media outlet outside output cavity.
In coalescent chamber, be provided with Coalescence filter core 35 and be separated filter core 36, Coalescence filter core is communicated with current stabilization chamber, is separated filter core and is communicated with output cavity, medium in current stabilization chamber through Coalescence filter core be separated filter core and enter output cavity.
Below coalescer, be also provided with hydrops tank 37, hydrops pot bottom is connected with blow-off pipe 38.
The medium carrying dust and spray film flows to inner surface by the outer surface of filter core and carries out filtration and coalescent, through the plenum chamber of the medium access arrangement of filter core process, the filter chamber of medium no matter on the left of equipment or the plenum chamber on the right side of equipment, all there is larger process space, medium is stopped fully at device interior, obtains best isolated by filtration effect.The pipeline that medium after metre filter is connected with coalescer by filter enters coalescer inside, equipment is divided into current stabilization chamber, coalescent chamber and output cavity by supporting clapboard by coalescer, medium is pooled to current stabilization chamber and enters Coalescence filter core inside, and flow to Coalescence filter core outside, through filtration, breakdown of emulsion, coalescent, sedimentation Four processes, by the liquid breakdown of emulsion of emulsification, then the droplet after breakdown of emulsion is agglomerated into large water drop, be deposited to housing bottom, discharged by sewage draining exit.The be not able to do in time droplet of sedimentation of part is separated filter core with flow direction, and be separated filter core and have good hydrophobicity performance, droplet is tackled completely effectively outside filter core, is again agglomerated into large water drop sedimentation thus guarantees effectively to remove moisture content.The moisture being deposited to housing bottom flows into the hydrops tank bottom coalescer, is shown, can be discharged by sewage draining exit by moisture content termly by liquid level gauge.Clean medium flows out from coalescer outlet.
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. a horizontal coalescence filtration combination unit, comprise base (1), be arranged on the coalescence filtration device (2) on base, it is characterized in that, described coalescence filtration device comprise be fixed together with base coalescer (3), to be fixed on above coalescer and with the filter (4) of coalescer by pipeline communication, on the right side of coalescer, end socket has media outlet (5), filter top has medium inlet (6), and medium inlet, filter, coalescer and media outlet are communicated with formation successively and filter coalescent passage.
2. horizontal coalescence filtration combination unit according to claim 1, it is characterized in that, filter comprises housing (41), enclosure interior is divided into the filter chamber (43) be communicated with medium inlet and the plenum chamber (44) be communicated with coalescer by sealing plate (42), filter chamber's internal fixtion has filter core (45), and filter core is fixed on sealing plate and outlet is communicated with plenum chamber.
3. horizontal coalescence filtration combination unit according to claim 2, it is characterized in that, coalescer comprises shell (31), in shell, space is separated into the current stabilization chamber (32) be communicated with filter, the coalescent chamber (33) be communicated with current stabilization chamber and the output cavity (34) be communicated with coalescent chamber, is communicated with media outlet outside output cavity.
4. horizontal coalescence filtration combination unit according to claim 3, it is characterized in that, in coalescent chamber, be provided with Coalescence filter core (35) and be separated filter core (36), Coalescence filter core is communicated with current stabilization chamber, be separated filter core and be communicated with output cavity, medium in current stabilization chamber through Coalescence filter core be separated filter core and enter output cavity.
5. horizontal coalescence filtration combination unit according to claim 1, is characterized in that, is also provided with hydrops tank (37) below coalescer, and hydrops pot bottom is connected with blow-off pipe (38).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520240002.8U CN204745938U (en) | 2015-04-20 | 2015-04-20 | Composite set is filtered in horizontal coalescence |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520240002.8U CN204745938U (en) | 2015-04-20 | 2015-04-20 | Composite set is filtered in horizontal coalescence |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204745938U true CN204745938U (en) | 2015-11-11 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520240002.8U Expired - Fee Related CN204745938U (en) | 2015-04-20 | 2015-04-20 | Composite set is filtered in horizontal coalescence |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204745938U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110499197A (en) * | 2019-08-15 | 2019-11-26 | 魏砚广 | A kind of horizontal filter separator |
| CN110723832A (en) * | 2019-11-20 | 2020-01-24 | 黑珀（上海）工业技术有限公司 | High-efficient oily waste water minimizing processing system |
-
2015
- 2015-04-20 CN CN201520240002.8U patent/CN204745938U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110499197A (en) * | 2019-08-15 | 2019-11-26 | 魏砚广 | A kind of horizontal filter separator |
| CN110723832A (en) * | 2019-11-20 | 2020-01-24 | 黑珀（上海）工业技术有限公司 | High-efficient oily waste water minimizing processing system |
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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: 20151111 Termination date: 20180420 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |