CN2936379Y - Air floating flushing type active sand continuous automatic filter - Google Patents
Air floating flushing type active sand continuous automatic filter Download PDFInfo
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- CN2936379Y CN2936379Y CN 200520079441 CN200520079441U CN2936379Y CN 2936379 Y CN2936379 Y CN 2936379Y CN 200520079441 CN200520079441 CN 200520079441 CN 200520079441 U CN200520079441 U CN 200520079441U CN 2936379 Y CN2936379 Y CN 2936379Y
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- gas
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- rectifier
- liquid
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Abstract
The utility model relates to a gas-liquid separator, which can be used for gas liquid separation in fields of petroleum, chemical engineering, oil refining, thermal energy engineering and environmental protection engineering. The utility model comprises a cylinder, a spiral-flow pre-elution device, a dished rotation device, a gas evolution plate, a droplets coalescence device, a rectifier, a demister and a filtering element of a filter. The utility model can provide separated flow field with clear function and greatly improve the gas liquid separation efficiency through the mutual position relationship of the parts in the gravity action.
Description
Technical field the utility model relates to a kind of gas-liquid separation equipment, is used for the field of oil, chemical industry, oil refining, heat energy and environment-friendly engineering gas-liquid separation.
In the background technology prior art, gas-liquid separator mainly is that two-phase separates the dependence gravitational settling to gas-liquid.But because the function of device structure element is indeterminate, cause the separative efficiency of equipment low, it is higher mainly to show as in the gas after the separation liquid carry over, and taking tolerance in the liquid after the separation can not meet the demands.Chinese patent 01260635.9 discloses a kind of gas-liquid separation device with energy-dissipating structure, this device is coming a kind of element for energy dissipation that has dumped packing has been installed on the liquid pipeline, although improved the flow pattern of coming liquid, long-term operation, random packing forms obstruction easily, makes the equipment can't operate as normal.
The summary of the invention the purpose of this utility model is to provide a kind of new and effective gas-liquid separation equipment, is intended to overcome the shortcoming of above-mentioned prior art, not only can provide function clearly demarcated separating flowing field, and can improve the removal efficiency of drop in the gas greatly.
Also be illustrated more clearly in the utility model in conjunction with the accompanying drawings by following description, but it does not limit the utility model, all should be considered as in scope of the present utility model based on above-mentioned any improvement, scheme of the present utility model and scope should limit with claims.
Realize that technical solution adopted in the utility model one is:
Adopt horizontal cylindrical structure, in cylinder, be provided with eddy flow pre-degasser, dish-shaped steering gear, gas successively and separate out plate, droplet coalescer, rectifier, demister, and on housing, be provided with mixture intake adapter, liquid outlet adapter, on mist eliminator, be provided with gas vent and take over.The eddy flow pre-degasser is connected with housing, air communicating pipe, and the umbrella shape catheter by being located at eddy flow pre-degasser bottom and conduit feed in the housing gas and separate out the plate top, is provided with dish-shaped steering gear in the catheter outlet.In housing, be provided with droplet coalescer, it be arranged on the perpendicular plane of housing axis on, droplet coalescer adopts and can carry out effectively coalescent structure to liquid in the gas.Rectifier be arranged on housing shaft on vertical plane, airflow pattern is put in order and is adjusted.Demister is arranged on the hull outside top, and is connected with enclosure interior, is provided with gas vent at its top and takes over.Be provided with liquid outlet at housing bottom and take over, liquid outlet adapter place is provided with anti-whirlpool element.The eddy flow pre-degasser is mainly by radially baffle plate, umbrella shape catheter, silk screen are formed.Gas is separated out plate and is made up of the plate that multilayer and housing horizontal axis form an angle, and is fixed with many current stabilization blend stops onboard, and the current stabilization blend stop can be made with angle steel, round steel, steel pipe or other material.Demister is made up of umbrella crown, silk screen, filter core.
Realize that the technical solution of the utility model two is:
Adopt the upright shell structure, mixture enters enclosure interior with tangential direction, is provided with multilayer deflection plate, rectifier, demister and minim pipette successively in enclosure interior.Be provided with liquid outlet in lower housing portion and take over, liquid outlet adapter place is provided with anti-whirlpool element.Demister is located at case top, and is connected with housing, is provided with gas vent and takes over above demister.Rectifier is arranged in the housing mixture intake and takes over the top, and makes its runner direction and housing axis perpendicular.
Structural detail and combining form that the utility model adopts have overcome the deficiencies in the prior art, have improved the separative efficiency of equipment to a greater extent.
Utilize description of drawings case study on implementation of the present utility model below the description of drawings.
Fig. 1 is a structural representation of the present utility model, and illustration is as follows:
1 gas is separated out plate 2 dish-shaped steering gear 3 mixture intakes and is taken over 4 eddy flow pre-degassers, 5 communicating pipe, 6 droplet coalescer, 7 rectifiers, 8 gas vents and take over the anti-whirlpool of 9 demisters 10 element 11 liquid outlets and take over 12 housings
Fig. 2 is the structural representation of another exemplifying embodiment of the utility model, and illustration is as follows:
3 mixture intakes are taken over 7 rectifiers, 8 gas vents and are taken over the anti-whirlpool of 9 demisters 10 element 11 liquid outlets and take over 12 housings, 13 liquid collecting zones, 14 liquid barriers, 15 multilayer deflection plates, 16 minim pipettes
Fig. 3 is the structural representation of eddy flow pre-degasser, and illustration is as follows:
4-1 eddy flow pre-degasser housing 4-2 escape pipe 4-3 droplet coalescence filler 4-4 baffle circle 4-5 circular hole 4-6 umbrella shape catheter 4-7 conduit
Fig. 4 is the structural representation that gas is separated out plate, and illustration is as follows:
1-1 hang plate 1-2 current stabilization blend stop 1-3 liquid barrier
Fig. 5 is the rectifier structure schematic diagram, and illustration is as follows:
7 rectifier 7-1 air distribution plate 7-2 flow-stopping plate 7-3 liquid barrier 7-4 apertures
Fig. 6 is the structural representation of rectifier element, and illustration is as follows:
7-4-1 horizontal component 7-4-2 groove 7-4-3 spacing body 7-4-4 connector 7-4-5 sloping portion
Fig. 7 is the structural representation of demister, and illustration is as follows:
9-1 through hole 9-2 baffle plate 9-3 umbrella crown 9-4 silk screen 9-5 demister housing 9-6 filter core
The specific embodiment is referring to Fig. 1, Fig. 3, its structure is horizontal cylindrical structure, gas-liquid mixture is by entrance sleeve 3 and tangentially enters in the eddy flow pre-degasser 4 that is arranged on housing top, gas and liquid are separated under centrifugal action, and a part of gas causes demister 9 through top escape pipe 4-2 communicating pipe 5.Liquid flows to the dish-shaped steering gear 2 relative with conduit 4-7 with the mixture of remaining gas by umbrella shape catheter 4-6 conduit 4-7, absorb the energy of gas-liquid mixture and transformation takes place to flow in this dish-shaped steering gear, flow direction gas after turning to is separated out plate 1, because mixture and gas are separated out the plate contact area and increased suddenly, the bubble in the liquid is separated out in a large number and is dropped down then into lower housing portion liquid collecting zone 13.Gas then flows to demister 9 through droplet coalescer 6 rectifiers 7 that are arranged in housing top successively, and takes over 8 outflow equipment through the gas vent that is arranged on the demister 9.Liquid is taken over 11 outflow equipment through anti-whirlpool element 10, liquid outlet.
Referring to Fig. 2, Fig. 7, its structure is the upright shell structure, gas-liquid mixture enters in the housing 12 by taking over 3 with the tangent mixture intake of housing, under centrifugal action, gas-liquid produces separates, liquid drops down into housing bottom liquid collecting zone 13 through liquid barrier 14, and through anti-whirlpool element 10, liquid outlet is taken over 11 outflow equipment.Multilayer deflection plate 15, the rectifier 7 of gas through being arranged on entrance sleeve 3 tops carries out droplet collision and enters demister 9 after coalescent, remove trickle droplet after gas vent is taken over 8 outflow equipment through silk screen (9-4), filter core (9-6) in demister 9, the liquid of removing in gas flows into liquid collecting zone 13 through minim pipette 16.
Claims (5)
1. gas-liquid two device for phase saparation, adopt horizontal or upright shell structure, being provided with eddy flow pre-degasser (4), dish type diverter (2), gas in housing successively separates out plate (1), multilayer deflection plate (15), droplet coalescer (6), rectifier (7), demister (9), liquid barrier (14), minim pipette (16) and is provided with on housing that mixture intake is taken over (3), anti-whirlpool element (10), liquid outlet is taken over (11), be provided with gas vent at demister (9) top and take over (8), it is characterized in that:
Eddy flow pre-degasser (4) is affixed with the housing external wall of upper portion, sidewall is provided with mixture intake and takes over (3), the top is by linking to each other with demister (9) communicating pipe (5), in eddy flow pre-degasser (4) top baffle circle (4-4) and angled with wall is set, baffle circle (4-4) is along boring a plurality of circular holes (4-5) near the wall place all around, baffle circle (4-4) top is provided with droplet coalescence filler (4-3) to catch drop, eddy flow pre-degasser top is provided with escape pipe (4-2), lower lumen is provided with umbrella shape catheter (4-6) and links to each other with conduit (4-7) and stretch in the housing (12), and with to be fixed in the dish-shaped steering gear (2) that gas separates out on the plate (1) relative;
Gas is separated out plate (1) and is placed in the housing (12), and forms an angle with axis, and gas is separated out plate and is made up of hang plate (1-1) and liquid barrier (1-3), is welded with current stabilization blend stop (1-2) thereon;
Rectifier (7) places in the housing (12), and is perpendicular with housing (12) axis, and in vertical structure, the runner of rectifier (7) and housing (12) axis are perpendicular;
Be connected with demister (9) at equipment upper end housing outer wall, it communicates by in through hole (9-1) and the housing, is provided with gas vent at its top and takes over (8);
Mixture intake is taken over (3) top and is provided with multilayer deflection plate (15) in the upright shell structure, and the bottom is provided with liquid barrier (14).
2. gas-liquid separation equipment according to claim 1, it is characterized in that: rectifier (7) is made up of the snakelike plate that multilayer is converted into definite shape, this plate is by horizontal component (7-4-1), form with the sloping portion (7-4-5) that forms an angle with horizontal component, a plurality of grooves (7-4-2) are arranged on horizontal component (7-4-1), fixedly connected with connector (7-4-4) by spacing body (7-4-3) between plate and the plate.
3. gas-liquid separation equipment according to claim 1, it is characterized in that: in the upright shell structure, at the upper and lower flow-stopping plate (7-2) that is equipped with of rectifier (7), make gas be baffling direction turnover rectifier (7), last flow-stopping plate gas outlet has a liquid barrier (7-3), rectifier (7) gas feed place has an air distribution plate (7-1), has uniform aperture (7-4) on it.
4. gas-liquid separation equipment according to claim 1 is characterized in that: rectifier (7) is provided with minim pipette (16), passes housing and inserts liquid collecting zone (13).
5. gas-liquid separation equipment according to claim 1, it is characterized in that: demister (9) mainly is made up of through hole (9-1), baffle plate (9-2), umbrella crown (9-3), silk screen (9-4), filter core (9-6) and demister housing (9-5), and filter core (9-6) is arranged between silk screen (9-4) and the top gas discharge connection (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520079441 CN2936379Y (en) | 2005-09-27 | 2005-09-27 | Air floating flushing type active sand continuous automatic filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520079441 CN2936379Y (en) | 2005-09-27 | 2005-09-27 | Air floating flushing type active sand continuous automatic filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2936379Y true CN2936379Y (en) | 2007-08-22 |
Family
ID=38360398
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520079441 Expired - Fee Related CN2936379Y (en) | 2005-09-27 | 2005-09-27 | Air floating flushing type active sand continuous automatic filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2936379Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102100988A (en) * | 2011-02-14 | 2011-06-22 | 中国石油集团工程设计有限责任公司 | Combined type natural gas-liquid separator |
| CN102423551A (en) * | 2011-08-15 | 2012-04-25 | 北京百恒达石油技术有限公司 | Efficient gas-liquid separator |
| CN102671470A (en) * | 2012-05-23 | 2012-09-19 | 浙江大学 | Efficient gas-liquid separator |
| CN108854159A (en) * | 2018-06-29 | 2018-11-23 | 上海米素环保科技有限公司 | A kind of butterfly acid hydrocarbon separator and manufacturing method |
-
2005
- 2005-09-27 CN CN 200520079441 patent/CN2936379Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102100988A (en) * | 2011-02-14 | 2011-06-22 | 中国石油集团工程设计有限责任公司 | Combined type natural gas-liquid separator |
| CN102423551A (en) * | 2011-08-15 | 2012-04-25 | 北京百恒达石油技术有限公司 | Efficient gas-liquid separator |
| CN102671470A (en) * | 2012-05-23 | 2012-09-19 | 浙江大学 | Efficient gas-liquid separator |
| CN108854159A (en) * | 2018-06-29 | 2018-11-23 | 上海米素环保科技有限公司 | A kind of butterfly acid hydrocarbon separator and manufacturing method |
| CN108854159B (en) * | 2018-06-29 | 2021-01-15 | 上海米素环保科技有限公司 | Butterfly acid hydrocarbon separator and manufacturing method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| DD01 | Delivery of document by public notice |
Addressee: Deng Zhian Document name: Notification to Pay the Fees |
|
| DD01 | Delivery of document by public notice |
Addressee: Yao Boyang Document name: Notification of Termination of Patent Right |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070822 Termination date: 20100927 |