CN2500366Y - Oil gas separator for thickened oil and special thickened oil - Google Patents
Oil gas separator for thickened oil and special thickened oil Download PDFInfo
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- CN2500366Y CN2500366Y CN 01261038 CN01261038U CN2500366Y CN 2500366 Y CN2500366 Y CN 2500366Y CN 01261038 CN01261038 CN 01261038 CN 01261038 U CN01261038 U CN 01261038U CN 2500366 Y CN2500366 Y CN 2500366Y
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Abstract
The utility model pertains to crude oil separation equipment of oilfield and relates to a gas-oil separator for thick oil, super thick oil and the accompanying gas thereof. The tube body is equipped with a gas-separating bag and a liquid-eliminating bag thereon and is equipped with a mechanical defoaming device, a wave resistance foam-breaking screen, an anti-foam web, and a snake type plate rectifier defogger therein. The utility model can solve the problem about long bubble season cracking time, poor oil-gas separation effect caused by slow lifting speed of bubble in thick oil and super thick oil, in the separation course of thick oil and super thick oil with gas content of 20-70Nm <3>/t. The utility model adopts oil-gas separation in the gas-separating bag, utilizes the serrated foam-forming plate and the foam-breaking web on the defoaming plate to break the foam surrounded by liquid film in the tube body and eliminates the liquid drop carried by gas in the liquid eliminating bag. The utility model has good oil-gas separation effect in the treatment of the thick oil and super thick oil with greater gas content. And after separation, the liquid content of the gas <= 0.05g/Nm<3> and emersion rate of the bubble with the grain diameter >= 150Mu m in thick oil and super thick oil >= 98.5 percent.
Description
Technical field
The utility model belongs to the crude oil separation equipment, relate to a kind of viscous crude and special viscous crude [according to the regulation of People's Republic of China's China National Petroleum industry standard " heavy oil gathering and steam injection systematic design discipline " SY0027-94, temperature is in the time of 50 ℃, dynamic viscosity is greater than 0.4Pa.S, and temperature when being 20 ℃ density greater than 0.9161g/cm
3Crude oil be viscous crude; Temperature is in the time of 50 ℃, and dynamic viscosity is greater than 10Pa.S, and temperature when being 20 ℃ density greater than 1.0g/cm
3Crude oil be special viscous crude] with the gs-oil separator of its associated gas.
Background technology
Domestic widely used lightweight and matter crude oil (50 ℃ of viscosity＜0.4Pa.S, 20 ℃ of density＜0.9161g/cm of being used for
3) gs-oil separator, its structural design meets " gs-oil separator standard " SY/T0515-1997, has vertical, horizontal and spherical three kinds from the appearance, uses maximum still vertical and horizontal gs-oil separators.Because domestic onshore oil field (promotion oil field, the Liaohe River, triumph Gudao oilfield, Karamay oilfield, Jing Lou oil field, Henan etc.) viscous crude air content is lower, oil-gas ratio generally is lower than 5Nm
3/ t adopts the steam soak method to recover the oil mostly, so the problem of viscous crude Oil-gas Separation difficulty shows not too outstandingly, makes each research and design unit do lessly in the research work aspect the viscous crude degassing.Recently come, (oil-gas ratio is at 20-70Nm along with air content is big
3/ t) marine viscous crude (as the SZ36-1 and the QHD32-6 oil-field thick-oil in Bohai Sea Gulf) and land viscous crude (Xinjiang system in Tahe Oilfield viscous crude) drops into exploitation gradually, the problem of viscous crude degassing difficulty just shows very outstandingly, as SZ36-1 oil field land terminal, purification viscous crude after its dehydration is when decompression enters storage tank stores, the oil mass that stores only be 2/3rds of a tank volume, overflows but its tank deck overfall has foam (bubble population that is surrounded by the viscous crude liquid film); The Xinjiang system in Tahe Oilfield uses common lightweight and middle matter crude oil vapor separator to carry out the special viscous crude degassing, contains a large amount of foams in the gas that separator is deviate from, and contains a large amount of bubbles in the crude oil after the separation, and oil gas separation is very poor.This shows the Oil-gas Separation problem of viscous crude and special viscous crude, can not rely on the gs-oil separator that is used for handling lightweight and matter crude oil to solve.
Compare with general lightweight and middle matter crude oil, viscous crude and special viscous crude have the density height from physical property, the viscosity height, asphalt colloid content height, freezing point is low, the characteristics that light ends content is low, if associated gas content is bigger in this situation viscous crude and special viscous crude, after gas floats on the magma face with the form of bubble in viscous crude and special viscous crude, owing to contain more asphalitine and colloid (its content reaches 20-50%) in the liquid film of encirclement gas, and the existence of the surface reactive materials such as naphthenic soap of alkanoic acid in viscous crude and the special viscous crude and metal ion reaction generation, make air bubble liquid-membrane intensity more greatly and very stable, thereby the time that bubble is broken naturally prolongs significantly, during speed that the speed that produces bubble when the viscous crude that enters separator and special viscous crude is broken greater than bubble, a large amount of bubble populations will be assembled on the viscous crude liquid level in separator, can be full of whole gas-phase space when serious, thereby destroy the normal operating conditions of separator, making its macro manifestations is to contain big quantity of fluid in the exit gas, contains a large amount of bubbles in outlet viscous crude and the special viscous crude.
Summary of the invention
The purpose of this utility model is to provide that a kind of to be used to handle air content be 20-70Nm
3When the viscous crude of/t and special viscous crude, can destroy bubble effectively, shorten the bubble required time that breaks, thereby make the interface that has metastable viscous crude and special viscous crude one foam one gas continuous phase in the gs-oil separator, contain the gs-oil separator that big quantity of fluid, outlet viscous crude and special viscous crude contain a large amount of bubbles to eliminate the gs-oil separator exit gas.
The purpose of this utility model is achieved in that a kind of viscous crude and special viscous crude gs-oil separator, comprises that cylindrical shell is provided with oil, gas-liquid mixture import, gas outlet, the outlet of fluid body, sewage draining exit and safety valve, liquid level gauge, liquor-level regulator, manhole; The cylindrical shell outer bottom is provided with saddle, it is characterized in that cylindrical shell is provided with a branch gas bag and one and removes the liquid bag, is provided with mechanical defoaming device, wave-proof foam-distinction otter board, demister, snake type plate rectifying defogger in the cylindrical shell.
The several piece that comprises mechanical defoaming device tilt symmetrically arranged froth breaking plate and vertically disposed broken indulging in serfing the Net.
The base plate of froth breaking plate is provided with several apertures, and every of the froth breaking plate is drawn the bubble plate to be provided with sawtooth.
Divide gas bag to be provided with viscous crude and the import of special viscous crude gas-liquid mixture, divide in the gas bag to be provided with high-penetration type mesh mist eliminator; Remove in the liquid bag and be provided with the standard type mesh mist eliminator, remove liquid bag top and be provided with the gas outlet.
Be provided with the catheter that divides gas bag to be communicated with in the cylindrical shell, be arranged on fluid proportion plate, dividing plate on the froth breaking plate.
Divide gas bag and remove the liquid bag to communicate by pipeline, connecting line is provided with valve, Pressure gauge.
The utility model adopts deviates from free gas (gas phase is continuous) outside the cylindrical shell of Horizontal Cylindrical Tank, destroy the bubble that is surrounded by liquid film in the cylindrical shell of Horizontal Cylindrical Tank, so function division is clear and definite; In the cylindrical shell of Horizontal Cylindrical Tank, utilize simultaneously the zigzag on the froth breaking plate to draw bubble plate and the broken destruction bubble of indulging in serfing the Net, therefore can shorten the bubble required time that breaks; Also be provided with wave-proof foam-distinction otter board in the cylindrical shell of this external Horizontal Cylindrical Tank, demister and snakelike plate rectification demister, therefore can form metastable liquid, foam and gas continuous phase interface in the cylindrical shell of Horizontal Cylindrical Tank, the utility model gs-oil separator has good oil gas separation when handling bigger viscous crude of air content and special viscous crude.
Description of drawings
Fig. 1 is the utility model structural representation;
Fig. 2 is the front view of froth breaking plate structure schematic diagram of the present utility model;
Fig. 3 is the vertical view of froth breaking plate structure schematic diagram of the present utility model;
Fig. 4 is an A-A cutaway view among Fig. 2;
Fig. 5 is an I portion enlarged drawing among Fig. 3.
The specific embodiment
Consult shown in Figure 1ly, viscous crude and special viscous crude gs-oil separator mainly are by minute gas bag 1, remove liquid bag 2, cylindrical shell 3, oil, gas-liquid mixture import 4, high-penetration type mesh mist eliminator 5, standard type mesh mist eliminator 6, gas outlet 7, viscous crude and special viscous crude liquid outlet 8, relief valve connection 9, sewage draining exit 10, on the liquid level gauge, lower interface 11, float liquor-level regulator interface 12, manhole 13, froth breaking plate 14, catheter 15, fluid proportion plate 16, break and indulge in serfing the Net 17, wave-proof foam-distinction otter board 18, demister 19, snake type plate rectifying defogger 20, dividing plate 21, saddle 22, valve 23, Pressure gauge 24 grades constitute.The cylindrical shell 3 of its horizontal cylindrical pressure vessel is provided with a branch gas bag 1 and one and removes liquid bag 2, communicate by pipeline, and two bag bottoms all communicates with cylindrical shell 3; Divide gas bag 1 to be provided with viscous crude and special viscous crude gas-liquid mixture import 4, divide in the gas bag 1 to be provided with high-penetration type mesh mist eliminator 5, finish with gas and being separated in the branch gas bag 1 of viscous crude and special viscous crude that the continuous phase form exists; Remove in the liquid bag 2 and be provided with standard type mesh mist eliminator 6, remove liquid bag 2 tops and be provided with gas outlet 7, in removing liquid bag 2, remove the drop that gas carries; The cylindrical shell 3 of horizontal cylindrical pressure vessel is provided with viscous crude and special viscous crude liquid outlet 8, relief valve connection 9, sewage draining exit 10, the upper and lower interface 11 of liquid level gauge, float liquor-level regulator interface 12, manhole 13; In the cylindrical shell 3 of horizontal cylindrical pressure vessel left ends be provided with mechanical defoaming device, with the catheter 15 that divides gas bag 1 to be communicated with, be arranged on fluid proportion plate 16 on the froth breaking plate 14, break and indulge in serfing the Net 17, the bottom is provided with wave-proof foam-distinction otter board 18, dividing plate 21, top is provided with demister 19, snake type plate rectifying defogger 20, is used for separating of bubble and viscous crude and special viscous crude; Cylindrical shell 3 outer bottoms are provided with container saddle 22; The connecting line that divides gas bag 1 and remove liquid bag 2 is provided with valve 23, Pressure gauge 24.
Consult Fig. 2, Fig. 3, Fig. 4, shown in Figure 5 simultaneously, mechanical defoaming device of the present utility model is arranged on left ends in the cylindrical shell 3 of horizontal cylindrical pressure vessel, comprises that the froth breaking plate 14 of eight inclination symmetric arrangement and some are vertically disposed brokenly to indulge in serfing the Net 17; Froth breaking plate 14 draws bubble plate 141, base plate 142 to constitute by sawtooth pattern, and base plate 142 is provided with φ 10 apertures 143 of some, and every is drawn bubble plate 141 to be provided with sawtooth 144.
Said structure makes function division of the present utility model clear and definite: a branch gas bag 1 and one are installed on the cylindrical shell 3 of a horizontal cylindrical pressure vessel remove liquid bag 2, viscous crude and special viscous crude are mixed angry mixture and are at first entered branch gas bag 1 with it, rely on centrifugal force and Gravity Separation to go out the gas that exists with continuous phase; In the cylindrical shell 3 of horizontal cylindrical pressure vessel, destroy bubble that is surrounded by liquid film and the bubble of deviating from remaining particle diameter in the liquid 〉=150 μ m by froth breaking plate 14; In removing liquid bag 2, remove the drop that gas carries.
The course of work of the present utility model: the mixture of viscous crude and special viscous crude and its associated gas enters branch gas bag 1, rely on gravity and centrifugal force to isolate the gas that exists with the continuous phase form, isolated gas is through high-penetration type mesh mist eliminator 5, enter except that liquid bag 2 through connecting pipeline again, in removing liquid bag 2 with horizontal cylindrical pressure vessel cylindrical shell 3 in the gas deviate from converge and enter standard type mesh mist eliminator 6, remove the liquid that carries in the gas after gas outlet 7 outflow separators; The mechanical defoaming device that divides the left end in catheter 15 and fluid proportion plate 16 enter the cylindrical shell 3 of horizontal cylindrical pressure vessel of isolated liquid and foam in the gas bag 1.
Viscous crude and special viscous crude and foam enter the froth breaking plate 14 of mechanical defoaming device from the top, one deck froth breaking plate 14 and the broken of some indulged in serfing the Net 17 under the aperture 143 of liquid on the base plate 142 of froth breaking plate 14 flowed to, foam climbs over sawtooth pattern and draws the sawtooth 144 at bubble plate 141 tops to flow to next piece sawtooth pattern to draw bubble plate 141, sharp edge when drawing bubble plate 141 to utilize foam to climb over sawtooth pattern destroys bubble, make the gas that is surrounded by oil film enter the cylindrical shell 3 internal upper part gas-phase spaces of horizontal cylindrical pressure vessel, liquid and a small amount of residual bubble enter the cylindrical shell 3 interior liquid phase spaces, bottom of horizontal cylindrical pressure vessel; Liquid further destroys a small amount of residual bubbles that carry in the liquid through two wave-proof foam-distinction otter boards 18 again, and viscous crude and special viscous crude climb over dividing plate 21 and enter surge chamber and export 8 effluent oil gas separating devices through viscous crude and special viscous crude; The gas of deviating from the cylindrical shell 3 enters snake type plate rectifying defogger 20 through demister 19 and deviates from drop, enters then except that liquid bag 2, and the gas of deviating from minute gas bag 1 converges after the standard type mesh mist eliminator removes effluent oil gas separating device behind the liquid.
Air content is 20-70Nm
3The viscous crude of/t and special viscous crude after the utility model is handled, isolated gas liquid content≤0.05g/Nm
3, bubble extrusion rate 〉=98.5% of particle diameter in isolated viscous crude and the special viscous crude 〉=150 μ m.
Claims (6)
1, a kind of viscous crude and special viscous crude gs-oil separator comprise that cylindrical shell is provided with oil, gas-liquid mixture import, gas outlet, the outlet of fluid body, sewage draining exit and safety valve, liquid level gauge, liquor-level regulator, manhole; The cylindrical shell outer bottom is provided with saddle, it is characterized in that cylindrical shell (3) is provided with a branch gas bag (1) and one and removes liquid bag (2), be provided with mechanical defoaming device, wave-proof foam-distinction otter board (18), demister (19), snake type plate rectifying defogger (20) in the cylindrical shell (3).
2, viscous crude according to claim 1 and special viscous crude gs-oil separator is characterized in that mechanical defoaming device comprises several piece tilt symmetrically arranged froth breaking plate (14) and vertically disposed broken indulge in serfing the Net (17).
3, viscous crude according to claim 2 and special viscous crude gs-oil separator is characterized in that the base plate (142) of froth breaking plate (14) is provided with several apertures (143), and every of froth breaking plate (14) is drawn bubble plate (141) to be provided with sawtooth (144).
4, viscous crude according to claim 1 and special viscous crude gs-oil separator is characterized in that branch gas bag (1) is provided with viscous crude and special viscous crude gas-liquid mixture import (4), divide in the gas bag (1) to be provided with high-penetration type mesh mist eliminator (5); Remove in the liquid bag (2) and be provided with standard type mesh mist eliminator (6), remove liquid bag (2) top and be provided with gas outlet (7).
5, viscous crude according to claim 1 and special viscous crude gs-oil separator is characterized in that being provided with in the cylindrical shell (3) and divide the gas bag catheter that (1) is communicated with (15), are arranged on fluid proportion plate (16), dividing plate (21) on the froth breaking plate (14).
6, according to claim 1 or 4 described viscous crude and special viscous crude gs-oil separator, it is characterized in that branch gas bag (1) and remove liquid bag (2) communicating by pipeline, connecting line is provided with valve (23), Pressure gauge (24).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01261038 CN2500366Y (en) | 2001-09-07 | 2001-09-07 | Oil gas separator for thickened oil and special thickened oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01261038 CN2500366Y (en) | 2001-09-07 | 2001-09-07 | Oil gas separator for thickened oil and special thickened oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2500366Y true CN2500366Y (en) | 2002-07-17 |
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ID=33669059
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01261038 Expired - Lifetime CN2500366Y (en) | 2001-09-07 | 2001-09-07 | Oil gas separator for thickened oil and special thickened oil |
Country Status (1)
| Country | Link |
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| CN (1) | CN2500366Y (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103157300A (en) * | 2011-12-14 | 2013-06-19 | 胜利油田胜利勘察设计研究院有限公司 | Thickened oil three-phase separator used for removing free water and combining thin oil |
| CN105498296A (en) * | 2016-01-07 | 2016-04-20 | 永胜机械工业（昆山）有限公司 | Defoaming tower |
| CN105521628A (en) * | 2016-01-07 | 2016-04-27 | 永胜机械工业（昆山）有限公司 | Removing tower used in polyvinyl chloride resin production |
| CN105597379A (en) * | 2016-01-14 | 2016-05-25 | 西安长庆科技工程有限责任公司 | Gas-liquid separator with defrothing structure |
| CN105909229A (en) * | 2016-05-06 | 2016-08-31 | 中国石油大学(北京) | Gas-liquid separator for oil field |
| CN106640029A (en) * | 2016-12-08 | 2017-05-10 | 中海艾普油气测试（天津）有限公司 | Thickened oil hydraulic power decomposition defoamer and control method |
| CN108057262A (en) * | 2017-12-21 | 2018-05-22 | 崔秀萍 | A kind of gasbag-type gas and oil separating plant and its method |
| CN108295513A (en) * | 2018-02-13 | 2018-07-20 | 中国石油天然气集团公司 | Weak eddy flow viscous crude defoams separator |
| CN108620274A (en) * | 2018-07-13 | 2018-10-09 | 广州市威迪尔实业有限公司 | A kind of the edge sealing oil fuel supply method and edge sealing oil box of anti-gel |
| CN108676933A (en) * | 2018-07-13 | 2018-10-19 | 广州市威迪尔实业有限公司 | A kind of edge sealing oil box |
| CN111456703A (en) * | 2020-04-10 | 2020-07-28 | 潘勇 | Oil separator |
| CN112147184A (en) * | 2020-11-24 | 2020-12-29 | 南京仪汇仪器设备有限公司 | Asphalt flash point detection device |
| WO2021088828A1 (en) * | 2019-11-04 | 2021-05-14 | 中国石油大学(华东) | Co 2 flooding produced fluid gas-liquid separation apparatus |
-
2001
- 2001-09-07 CN CN 01261038 patent/CN2500366Y/en not_active Expired - Lifetime
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103157300A (en) * | 2011-12-14 | 2013-06-19 | 胜利油田胜利勘察设计研究院有限公司 | Thickened oil three-phase separator used for removing free water and combining thin oil |
| CN105498296A (en) * | 2016-01-07 | 2016-04-20 | 永胜机械工业（昆山）有限公司 | Defoaming tower |
| CN105521628A (en) * | 2016-01-07 | 2016-04-27 | 永胜机械工业（昆山）有限公司 | Removing tower used in polyvinyl chloride resin production |
| CN105597379A (en) * | 2016-01-14 | 2016-05-25 | 西安长庆科技工程有限责任公司 | Gas-liquid separator with defrothing structure |
| CN105909229B (en) * | 2016-05-06 | 2018-12-21 | 中国石油大学(北京) | Oil field gas-liquid separator |
| CN105909229A (en) * | 2016-05-06 | 2016-08-31 | 中国石油大学(北京) | Gas-liquid separator for oil field |
| CN106640029A (en) * | 2016-12-08 | 2017-05-10 | 中海艾普油气测试（天津）有限公司 | Thickened oil hydraulic power decomposition defoamer and control method |
| CN106640029B (en) * | 2016-12-08 | 2019-05-21 | 中海艾普油气测试（天津）有限公司 | A kind of viscous crude hydraulic power resolving froth breaker and control method |
| CN108057262A (en) * | 2017-12-21 | 2018-05-22 | 崔秀萍 | A kind of gasbag-type gas and oil separating plant and its method |
| CN108295513A (en) * | 2018-02-13 | 2018-07-20 | 中国石油天然气集团公司 | Weak eddy flow viscous crude defoams separator |
| CN108620274A (en) * | 2018-07-13 | 2018-10-09 | 广州市威迪尔实业有限公司 | A kind of the edge sealing oil fuel supply method and edge sealing oil box of anti-gel |
| CN108676933A (en) * | 2018-07-13 | 2018-10-19 | 广州市威迪尔实业有限公司 | A kind of edge sealing oil box |
| WO2021088828A1 (en) * | 2019-11-04 | 2021-05-14 | 中国石油大学(华东) | Co 2 flooding produced fluid gas-liquid separation apparatus |
| CN111456703A (en) * | 2020-04-10 | 2020-07-28 | 潘勇 | Oil separator |
| CN111456703B (en) * | 2020-04-10 | 2022-03-18 | 万骏 | Oil separator |
| CN112147184A (en) * | 2020-11-24 | 2020-12-29 | 南京仪汇仪器设备有限公司 | Asphalt flash point detection device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: 100120, room 9, building 39, No. 403 middle third ring road, Haidian District, Beijing Patentee after: China Oil HBP Science & Technology Co.,Ltd. Address before: 100088 No. 39 middle third ring road, Haidian District, Beijing Patentee before: Huayou Huibopu Science and Technology Co., Ltd., Beijing |
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| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20110907 Granted publication date: 20020717 |