CN204051077U - A kind of aqueous phase UNICOM balanced type three phases separator - Google Patents
A kind of aqueous phase UNICOM balanced type three phases separator Download PDFInfo
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- CN204051077U CN204051077U CN201420440144.4U CN201420440144U CN204051077U CN 204051077 U CN204051077 U CN 204051077U CN 201420440144 U CN201420440144 U CN 201420440144U CN 204051077 U CN204051077 U CN 204051077U
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- crude oil
- housing
- aqueous phase
- balanced type
- unicom
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Abstract
The utility model discloses a kind of aqueous phase UNICOM balanced type three phases separator.A kind of aqueous phase UNICOM balanced type three phases separator, it comprise housing and on water, gas, oil export, crude oil entrance is placed on the left end socket of described housing, is provided with crude oil inlet baffle in the housing at this crude oil entrance rear; The rear of this crude oil inlet baffle is provided with coalescent pack device, and be provided with crude oil overflow weir and profit dividing plate in the housing at this coalescent pack device rear successively, oil export is between crude oil overflow weir and profit dividing plate; Be located at delivery port in crude oil overflow weir front end shell with the water inlet be located at after profit dividing plate in end housing by communicating pipe UNICOM, the other end of this water inlet is connected with balance pipe.The utility model, by the hydroecium UNICOM after the hydroecium before weir plate and profit dividing plate, utilizes difference in specific gravity to reach liquid level equilibrium, more efficiently, accurately, reliably can complete water-oil separating.
Description
Technical field
The utility model relates to a kind of separator for former oil and gas, more particularly, relates to one and carries out pretreated aqueous phase UNICOM balanced type three phases separator device to crude oil.
Background technology
The three phases separator of common single weir plate form, after oil gas water mixed liquid enters separator, gas is discharged from gas vent after collision is separated and fine droplet is removed in sedimentation separation by demist resolution element, small drop constantly collides with each other coalescent, form larger drop, collect in the liquid phase region of the bottom of container, oil water mixture scatters to dirty along impingement baffle, enter separator liquid collection section, Oil-water separation is carried out by difference in specific gravity, when after stop time enough, just obvious oil-water interfaces are defined, the oil reservoir that proportion is lighter flows into gathering room naturally from weir plate top, finally discharge from oil export, water is then deposited on hydroecium, finally discharge from water out.But when profit proportion is close especially, oil-water interfaces are not just clearly, and as selected this form, certainty of measurement will decline, and quite high to the required precision of Liquid level instrument, causes cost to increase.
Summary of the invention
The utility model provides a kind of aqueous phase UNICOM balanced type three phases separator, more efficiently, accurately, reliably can complete water-oil separating.
The purpose of this utility model is achieved by following technical solution:
A kind of aqueous phase UNICOM balanced type three phases separator, it comprise housing and on water, gas, oil export, crude oil entrance is placed on the left end socket of described housing, is provided with crude oil inlet baffle in the housing at this crude oil entrance rear; The rear of this crude oil inlet baffle is provided with coalescent pack device, and be provided with crude oil overflow weir and profit dividing plate in the housing at this coalescent pack device rear successively, oil export is between crude oil overflow weir and profit dividing plate; Be located at delivery port in crude oil overflow weir front end shell with the water inlet be located at after profit dividing plate in end housing by communicating pipe UNICOM, the other end of this water inlet is connected with balance pipe.
Water out and oil export are all equipped with vortex broken device.
Described vortex broken device is the plate structure of cross welding.
Described housing sidewall is provided with liquid level gauge mouth, thermometer mouth and temperature transmitter mouth; Case top is provided with gauge port, pressure transmitter mouth and relief valve port.
The left and right end socket at described housing two ends is provided with manhole, and this left and right end socket internal side wall is provided with cat ladder.
Separator is supported by the saddle that two are located at housing bottom.
The utility model is on the basis of conventional oil gas-water separator, grease chamber and hydroecium are transformed, single weir plank frame of the three phase separator of common single weir plate form is changed into two grease chambeies structure, doing so avoids the control at oil/water interface, and only have control that is gas/oil, gas/water termination, make measurement more accurate.Especially when profit proportion is close especially, oil-water interfaces are not just clearly, as selected single weir plate form, will be quite high to the required precision of Liquid level instrument, and cause cost to increase.The utility model, by the hydroecium UNICOM after the hydroecium before weir plate and profit dividing plate, utilizes difference in specific gravity to reach liquid level equilibrium, more efficiently, accurately, reliably can complete water-oil separating.To low, the bulky and power consumption of the current separator separation treatment efficiency of solution, there is greatly certain directive significance
In a word, the utility model structure is simple, easy to operate, function admirable, safe and reliable, cheap, operating cost is low, separative efficiency is high, and coalescent pack repeatedly Reusability capable of washing, the life-span is long.The Automatic continuous that this device can realize crude oil is separated, and is particularly suitable for ocean platform oil gas water treatment technology and uses.
Accompanying drawing explanation
Fig. 1 is profile of the present utility model;
Fig. 2 is side view of the present utility model.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is further described.
Structure of the present utility model is see Fig. 1,2, and it comprises: housing 10, left end socket 2-1, right end socket 2-2, crude oil entrance 4, water out 18, oil export 20, gas outlet 15; It also includes: crude oil inlet baffle 5, and coalescent pack device 6(is PEX coalescing-plate).Be provided with crude oil overflow weir 12 and profit dividing plate 14 in the housing 10 at this coalescent pack device 6 rear successively, oil export 20 is between crude oil overflow weir 12 and profit dividing plate 14; The water inlet 19 being located at the delivery port 23 in crude oil overflow weir 12 front end shell 10 and be located in the rear end housing 10 of profit dividing plate 14, by communicating pipe 22 UNICOM, the other end of this water inlet 19 is connected with balance pipe 26.
The housing 10 of separator is pressure vessel, and two ends are welded with left and right end socket 2-1,2-2.The crude oil entrance 4 that left end socket 2-1 top is provided with, the bottom of housing 10 is provided with water out 18 and oil export 20.
Described aqueous phase UNICOM balanced type three phases separator, carries out the separation of oil gas water as coalescent pack with PEX coalescing-plate.This separator also comprises: vortex broken device 17; Vortex broken device 17 is equipped with water out 18 and oil export 20, the plate that vortex broken device 17 welds for cross.Housing 10 sidewall be provided with first, second liquid level gauge mouth 11,13, thermometer mouth 24 and temperature transmitter mouth 25.Housing 10 top is provided with gauge port 7, pressure transmitter mouth 8, the gentle outlet 15 of relief valve port 9.Left end socket 2-1 is provided with manhole 3-1, and right end socket 2-2 is provided with manhole 3-2, and left and right end socket 2-1,2-2 internal side wall is provided with cat ladder 16.Separator is supported by the saddle 1 that two are located at housing bottom.
Oil gas water three phase mixed liquor enters internal tank through crude oil entrance 4, crude oil entrance rear end has crude oil inlet baffle 5 to make oil gas aqueous mixtures carry out pre-separation, enter three phases separator cohesion section, by difference in specific gravity with on coalescent pack device and PEX coalescing-plate 6, oil is carried out in cohesion, gas, water is separated, the oil droplet that proportion is lighter floats, and heavier falls under water, just defines obvious oil-water interfaces, the oil reservoir that proportion is lighter enters grease chamber through crude oil overflow weir 12, finally discharges from oil export 20; Water is then gathered in bottom housing 10 and connects through communicating pipe 22 from delivery port 23, and enter hydroecium by water inlet 19 and balance pipe 26, discharge through water out 18, balance pipe 26 plays the principle of linker, makes the liquid level before and after fuel tank reach self-balancing.Isolated gas, by demist resolution element, is discharged from gas vent 15 after sedimentation separation is separated removal fine droplet with collision.Can external Pressure gauge display pressure by gauge port 7, can external temperature meter displays temperature by thermometer mouth 24, directly observe liquid height in separator by first, second liquid level gauge mouth 11,13.Be provided with relief valve port 9 at separator top and can carry out overpressure protection by external safety valve.Add in operation rationally reliably the control instrument such as pressure transmitter 8, temperature transmitter 25 make whole system reach steady and continuous print oil and gas and water from process.
Claims (6)
1. an aqueous phase UNICOM balanced type three phases separator, it comprise housing and on water, gas, oil export, it is characterized in that: crude oil entrance (4) is placed on the left end socket of described housing (10), in the housing (10) at this crude oil entrance (4) rear, be provided with crude oil inlet baffle (5); The rear of this crude oil inlet baffle (5) is provided with coalescent pack device (6), be provided with crude oil overflow weir (12) and profit dividing plate (14) in the housing (10) at this coalescent pack device (6) rear successively, oil export (20) is positioned between crude oil overflow weir (12) and profit dividing plate (14); Be located at delivery port (23) in crude oil overflow weir (12) front end shell (10) and be located at the water inlet (19) of profit dividing plate (14) afterwards in end housing (10) by communicating pipe (22) UNICOM, the other end of this water inlet (19) is connected with balance pipe (26).
2. a kind of aqueous phase UNICOM according to claim 1 balanced type three phases separator, is characterized in that: on water out (18) and oil export (20), vortex broken device (17) is all housed.
3. a kind of aqueous phase UNICOM according to claim 2 balanced type three phases separator, is characterized in that: the plate structure that described vortex broken device (17) welds for cross.
4. a kind of aqueous phase UNICOM according to claim 1 balanced type three phases separator, is characterized in that: described housing (10) sidewall is provided with liquid level gauge mouth, thermometer mouth and temperature transmitter mouth; Housing (10) top is provided with gauge port, pressure transmitter mouth and relief valve port.
5. a kind of aqueous phase UNICOM according to claim 1 balanced type three phases separator, is characterized in that: the left and right end socket at described housing (10) two ends is provided with manhole, and this left and right end socket (2-1,2-2) internal side wall is provided with cat ladder.
6. a kind of aqueous phase UNICOM according to claim 5 balanced type three phases separator, is characterized in that: separator is supported by the saddle (1) that two are located at housing (10) bottom.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420440144.4U CN204051077U (en) | 2014-08-06 | 2014-08-06 | A kind of aqueous phase UNICOM balanced type three phases separator |
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CN201420440144.4U CN204051077U (en) | 2014-08-06 | 2014-08-06 | A kind of aqueous phase UNICOM balanced type three phases separator |
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CN201420440144.4U Expired - Fee Related CN204051077U (en) | 2014-08-06 | 2014-08-06 | A kind of aqueous phase UNICOM balanced type three phases separator |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104629794A (en) * | 2015-02-09 | 2015-05-20 | 华东理工大学 | Oil-gas-washing-coupled oil-water initial separation method and device |
CN107510949A (en) * | 2017-09-26 | 2017-12-26 | 深圳市蓝石环保科技有限公司 | A kind of MVR vapo(u)rization systems |
-
2014
- 2014-08-06 CN CN201420440144.4U patent/CN204051077U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104629794A (en) * | 2015-02-09 | 2015-05-20 | 华东理工大学 | Oil-gas-washing-coupled oil-water initial separation method and device |
CN107510949A (en) * | 2017-09-26 | 2017-12-26 | 深圳市蓝石环保科技有限公司 | A kind of MVR vapo(u)rization systems |
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Legal Events
Date | Code | Title | Description |
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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: 20141231 Termination date: 20190806 |
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CF01 | Termination of patent right due to non-payment of annual fee |