CN102423551A - Efficient gas-liquid separator - Google Patents
Efficient gas-liquid separator Download PDFInfo
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- CN102423551A CN102423551A CN2011102331683A CN201110233168A CN102423551A CN 102423551 A CN102423551 A CN 102423551A CN 2011102331683 A CN2011102331683 A CN 2011102331683A CN 201110233168 A CN201110233168 A CN 201110233168A CN 102423551 A CN102423551 A CN 102423551A
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- Separating Particles In Gases By Inertia (AREA)
Abstract
The invention discloses an efficient gas-liquid separator which comprises a shell. The shell is internally divided into a gas collection area, a flow distribution area, a precipitation area, a liquid collection area and a sewage discharge area, wherein a liquid baffle is arranged between the gas collection area and the flow distribution area; a sewage discharge plate is arranged between the liquid collection area and the sewage discharge area; a mist catcher is arranged at the top of the gas collection area; a gas outlet is arranged on the mist catcher; a flow distributor is arranged in the flow distribution area and communicated with a gas-liquid inlet; a multi-layer traverse baffle is arranged at the upper part of the precipitation area; a liquid level control valve is arranged at the lower part of the precipitation area; a liquid outlet is arranged on the liquid collection area; a heating pipe is arranged in the liquid collection area; a hot water inlet/outlet is arranged on the heating pipe; a sewage discharge port is arranged at the bottom of the sewage discharge area; a safety valve is arranged on the gas collection area; a barometer is arranged on the gas collection area; a liquid level meter is arranged on the liquid collection area; the mist catcher is a silk screen type mist catcher; and the silk screen type mist catcher is formed by weaving stainless steel wires and overlapping into a screen pad. Through the invention, a good phase-equilibrium separation and mechanical separation environment is created for gas-liquid separation, and efficient separation is realized.
Description
Technical field
The present invention is a kind of gas-liquid separator, particularly a kind of high efficient gas and liquid separator.
Background technology
In oilfield surface engineering, for satisfying oil gas well gauging of products, the needs that mining site processing, storage and pipeline (or other mode of movements) are carried must separate established gas-liquid two-phase, and two are separated carries out in gas-liquid separator usually.When the gas-liquid separator that uses on the oil field at present existed to come liquid measure to change, adaptive capacity was poor, and buffer capacity is low; It is difficult to install, check, maintain; Be not easy to process shortcomings such as skid-mounted unit, exist to separate in addition not thorough, problem such as separating effect is undesirable, energy consumption is big, efficient is low.
Summary of the invention
The objective of the invention is to invent a kind of high efficient gas and liquid separator with good balance each other separation and mechanical separation environment in order to overcome the halfway defective of the low separation of existing gas-liquid separator adaptive capacity difference buffer capacity.
The objective of the invention is to be to realize: said high efficient gas and liquid separator by following technical scheme; Comprise a housing; From top to bottom be divided into gas collection district, shunting zone, decanting zone, liquid collecting zone and blowdown district in the housing; Be provided with liquid barrier between gas collection district and shunting zone, liquid collecting zone and blowdown interval are provided with the blowdown plate; The top in gas collection district is provided with mist eliminator, and mist eliminator is provided with gas vent; Be provided with current divider in the shunting zone, current divider is communicated with the gas-liquid import; The top of decanting zone is provided with the multilayer deflection plate, and the bottom of decanting zone is provided with fluid level control valve; Liquid collecting zone is provided with liquid outlet, is provided with heating tube in the liquid collecting zone, and heating tube is provided with the hot water entrance; The bottom in blowdown district is provided with sewage draining exit.
Said gas collection district is provided with safety valve.
Said gas collection district is provided with barometer; Liquid collecting zone is provided with liquid level gauge.
Said mist eliminator is the screen type mist eliminator, and the screen type mist eliminator is made up of braiding of the stainless steel wire of diameter 0.05mm～0.5mm and the gauze pad that builds up thick 100mm～150mm.
Good effect of the present invention is following: reach the effect of further separation to the oil of decanting zone through the effect of multilayer deflection plate owing to descend slowly and lightly, and the gas after separating intercepts and captures the more oil droplet of small particle diameter through mist eliminator, so realized the purpose of high efficiency separation gas-liquid mixture; The present invention is through pressure, liquid level control, and the employing safety prevention measure, has created good balancing each other for gas-liquid separation and has separated and the mechanical separation environment, has realized the efficient of separation.
Description of drawings
Accompanying drawing 1 is a structural representation of the present invention;
Accompanying drawing 2 is a schematic top plan view of the present invention;
Among the figure: 1 housing, 2 gas collection districts, 3 shunting zones
5 liquid collecting zones, 6 blowdown districts, 4 decanting zones
7 liquid barriers, 8 blowdown plates, 9 mist eliminators
The 12 gas-liquid imports of 10 gas vents, 11 current dividers
13 deflection plates, 14 fluid level control valves, 15 liquid outlets
16 heating tubes, 17 hot water entrances, 18 sewage draining exits
19 safety valves, 20 barometers, 21 liquid level gauges
22 gauze pads
The specific embodiment
Shown in Figure 2 like Fig. 1; Said high efficient gas and liquid separator comprises a housing 1, from top to bottom is divided into gas collection district 2, shunting zone 3, decanting zone 4, liquid collecting zone 5 and blowdown district 6 in the housing 1; 3 of gas collection district 2 and shunting zones are provided with liquid barrier 7, and 6 in liquid collecting zone 5 and blowdown district are provided with blowdown plate 8; The top in gas collection district 2 is provided with mist eliminator 9, and mist eliminator 9 is provided with gas vent 10; Be provided with current divider 11 in the shunting zone 3, current divider 11 is communicated with gas-liquid import 12; The top of decanting zone 4 is provided with multilayer deflection plate 13, and the bottom of decanting zone 4 is provided with fluid level control valve 14; Liquid collecting zone 5 is provided with liquid outlet 15, is provided with heating tube 16 in the liquid collecting zone 5, and heating tube 16 is provided with hot water entrance 17; The bottom in blowdown district 6 is provided with sewage draining exit 18.
Said gas collection district 2 is provided with safety valve 19.
Said gas collection district 2 is provided with barometer 20; Liquid collecting zone 5 is provided with liquid level gauge 21.
Said mist eliminator 9 is the screen type mist eliminator, and the screen type mist eliminator is woven and built up gauze pad 22 by stainless steel wire to be formed.
Said gauze pad 22 is woven and is built up the thickness of 100mm～150mm by the stainless steel wire of diameter 0.05mm～0.5mm.
During use, gas-liquid mixture gets into current divider through the gas-liquid import, and current divider separates gas-liquid mixture, and the oil after the separation will descend slowly and lightly downwards, and the gas collection that will make progress of the gas after separating; Descend slowly and lightly the oil that gets off through the effect of multilayer deflection plate, the bubble in the oil is separated out, reach the effect of further separation, the oil after further separating falls into liquid collecting zone; Gas after the separation is intercepted and captured the more oil droplet of small particle diameter through mist eliminator.
The above; It only is preferred embodiment of the present invention; Be not that the present invention is done any pro forma restriction, every foundation technical spirit of the present invention all still belongs in the scope of technical scheme of the present invention any simple modification, equivalent variations and modification that above embodiment did.
Claims (5)
1. high efficient gas and liquid separator, it is characterized in that: it comprises a housing, from top to bottom is divided into gas collection district, shunting zone, decanting zone, liquid collecting zone and blowdown district in the housing, is provided with liquid barrier between gas collection district and shunting zone, liquid collecting zone and blowdown interval are provided with the blowdown plate; The top in gas collection district is provided with mist eliminator, and mist eliminator is provided with gas vent; Be provided with current divider in the shunting zone, current divider is communicated with the gas-liquid import; The top of decanting zone is provided with the multilayer deflection plate, and the bottom of decanting zone is provided with fluid level control valve; Liquid collecting zone is provided with liquid outlet, is provided with heating tube in the liquid collecting zone, and heating tube is provided with the hot water entrance; The bottom in blowdown district is provided with sewage draining exit.
2. high efficient gas and liquid separator according to claim 1 is characterized in that: said gas collection district is provided with safety valve.
3. high efficient gas and liquid separator according to claim 1 is characterized in that: said gas collection district is provided with barometer; Liquid collecting zone is provided with liquid level gauge.
4. high efficient gas and liquid separator according to claim 1 is characterized in that: said mist eliminator is the screen type mist eliminator, and the screen type mist eliminator is woven and built up gauze pad by stainless steel wire to be formed.
5. high efficient gas and liquid separator according to claim 4 is characterized in that: said gauze pad is woven and is built up the thickness of 100mm～150mm by the stainless steel wire of diameter 0.05mm～0.5mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011102331683A CN102423551A (en) | 2011-08-15 | 2011-08-15 | Efficient gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011102331683A CN102423551A (en) | 2011-08-15 | 2011-08-15 | Efficient gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102423551A true CN102423551A (en) | 2012-04-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011102331683A Pending CN102423551A (en) | 2011-08-15 | 2011-08-15 | Efficient gas-liquid separator |
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| CN (1) | CN102423551A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103421564A (en) * | 2012-05-18 | 2013-12-04 | 北京三聚环保新材料股份有限公司 | Natural gas desulfuration and liquid-removing device and desulfuration technology thereof |
| CN103657314A (en) * | 2013-11-30 | 2014-03-26 | 成都科盛石油科技有限公司 | Gas-liquid separation device provided with spiral pipe |
| CN103657313A (en) * | 2013-11-30 | 2014-03-26 | 成都科盛石油科技有限公司 | Gas-liquid separator |
| CN104096407A (en) * | 2014-07-25 | 2014-10-15 | 攀钢集团矿业有限公司 | Liquid drainage system comprising vacuum filter |
| CN106621474A (en) * | 2016-12-12 | 2017-05-10 | 胜利油田森诺胜利工程有限公司 | Technology for removing combustible gas and hydrogen sulfide from geothermal water |
| CN115337740A (en) * | 2022-08-16 | 2022-11-15 | 武汉国力通能源环保股份有限公司 | Gas-liquid separation method with large variation of treatment gas amount |
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| US5698014A (en) * | 1996-02-23 | 1997-12-16 | Atlantic Richfield Company | Liquid carryover control for spiral gas liquid separator |
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| CN1966122A (en) * | 2005-11-18 | 2007-05-23 | 中国科学院力学研究所 | Device for separating incompatible gas-liquid two phase and liquid-liquid two phase |
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2011
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| US5698014A (en) * | 1996-02-23 | 1997-12-16 | Atlantic Richfield Company | Liquid carryover control for spiral gas liquid separator |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103421564A (en) * | 2012-05-18 | 2013-12-04 | 北京三聚环保新材料股份有限公司 | Natural gas desulfuration and liquid-removing device and desulfuration technology thereof |
| CN103421564B (en) * | 2012-05-18 | 2015-10-14 | 北京三聚环保新材料股份有限公司 | A kind of natural qi exhaustion liquid desulfurizer and sulfur removal technology thereof |
| CN103657314A (en) * | 2013-11-30 | 2014-03-26 | 成都科盛石油科技有限公司 | Gas-liquid separation device provided with spiral pipe |
| CN103657313A (en) * | 2013-11-30 | 2014-03-26 | 成都科盛石油科技有限公司 | Gas-liquid separator |
| CN104096407A (en) * | 2014-07-25 | 2014-10-15 | 攀钢集团矿业有限公司 | Liquid drainage system comprising vacuum filter |
| CN104096407B (en) * | 2014-07-25 | 2016-03-23 | 攀钢集团矿业有限公司 | A kind of drainage system comprising vacuum filter |
| CN106621474A (en) * | 2016-12-12 | 2017-05-10 | 胜利油田森诺胜利工程有限公司 | Technology for removing combustible gas and hydrogen sulfide from geothermal water |
| CN115337740A (en) * | 2022-08-16 | 2022-11-15 | 武汉国力通能源环保股份有限公司 | Gas-liquid separation method with large variation of treatment gas amount |
| CN115337740B (en) * | 2022-08-16 | 2024-01-12 | 武汉国力通能源环保股份有限公司 | Gas-liquid separation method with large change of treatment gas quantity |
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Application publication date: 20120425 |