CN107189810A - A kind of novel combination type three phases separator based on solar energy utilization technique - Google Patents
A kind of novel combination type three phases separator based on solar energy utilization technique Download PDFInfo
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- CN107189810A CN107189810A CN201710574317.XA CN201710574317A CN107189810A CN 107189810 A CN107189810 A CN 107189810A CN 201710574317 A CN201710574317 A CN 201710574317A CN 107189810 A CN107189810 A CN 107189810A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
- C10G31/10—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for with the aid of centrifugal force
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/042—Breaking emulsions by changing the temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/045—Breaking emulsions with coalescers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/12—Auxiliary equipment particularly adapted for use with liquid-separating apparatus, e.g. control circuits
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0042—Degasification of liquids modifying the liquid flow
- B01D19/0052—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
- B01D19/0057—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused the centrifugal movement being caused by a vortex, e.g. using a cyclone, or by a tangential inlet
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G33/00—Dewatering or demulsification of hydrocarbon oils
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Cyclones (AREA)
Abstract
A kind of novel combination type three phases separator based on solar energy utilization technique belongs to separator field, including entrance preseparator (7), solar energy heating-heat-exchanger rig, tank device, the initial gross separation of gas-liquid-solid three-phase is carried out using entrance preseparator (7), improve gas-liquid separation efficiency, and oil mixing with water is mutually free of sandstone impurity, the problem of avoiding blocking, extends the usage cycles of three phases separator；Water-oil emulsion is heated by solar energy heat collection exchanger, at utmost changes the viscosity of water-oil phase, accelerates water-oil separating, realizes that solar energy highly effective is utilized, reduces the heating energy consumption of traditional oils mixing wastewater with air phase；Efficiently separating for oil gas water three phase is realized using the synergy of entrance preseparator (7), solar energy heating-heat-exchanger rig, tank device three.
Description
Technical field
The present invention relates to a kind of separator, and in particular to a kind of novel combination type oil gas based on solar energy utilization technique
Water three-phase separator.
Background technology
The conventional oil gas well anhydrous productive life is very short, as current domestic main force's oil gas field subsequently enters the middle and later periods rank of exploitation
Section, water filling drives by force technology progressively in each oil field large-scale promotion application, and achieves huge economic and social benefit, the skill
The extensive use of art, while recovery ratio is improved, also increases, moisture content is constantly raised with landing ground Produced Liquid amount.Largely
High water cut produced fluid oil supply field surface production bring a series of problems, such as increase gathering line load, crude oil dehydration
System is constantly remodeled and expand.Wherein, prominent is crude oil dehydration, and many oil fields use two sections or three sections, or even the use four having
Duan Liucheng is dehydrated.Not only flow is complicated for traditional dewatering process, and engineering construction investment is high, and power consumption is big, simultaneously because
This multistage process automation level is low, and the also safety in production to oil field brings problem.Therefore each oil field is saved to reduce cost
About energy consumption, improves competitiveness, and crude oil dehydration energy-efficient to development of new, degassing equipment is adopted new technology, and new technology is increasingly weighed
Depending on getting up.The use of three phase separator is the demand that oil field enters tail period, and it is used as a kind of simple in construction, treatment effeciency
Higher equipment and be widely used.
Three phases separator is by development for many years, and its performance constantly improve, separative efficiency is improved constantly, in oil field
Widely applied in development process, but be in particular in the following aspects there is also some problems simultaneously:Operation energy consumption
Height, conventional oil, gas and water three phase separator are heated to be into before separator, using the heating of mixed liquor heater and separator import
Locate coil pipe heating, both heaters all have that heating cycle is complicated, silt is more, easily block, it is easy to wear situations such as, and heat and set
The standby thermal efficiency is low, is easily damaged, the shortcomings of firing equipment maintenance is difficult；Low separation efficiency, oil field mining liquid is constantly being produced
During, its component and content are all being continually changing, and the fluctuation of oil gas water flow can influence equipment to divide gas-liquid and profit
From effect, and then separator separating property is caused to decline；Accommodation is narrow, anti-fluctuation ability, the oil gas water three of current application
Phase separator is all designed according to the concrete condition at scene, is merely able to meet the oil and gas and water under the conditions of this from if in other oil fields
Using, it is likely that the problem of inferior separating effect occurs.
The content of the invention
The technical problems to be solved by the invention are：Overcome the deficiencies in the prior art there is provided one kind based on solar heat profit
With the novel combination type three phases separator of technology.
The technical scheme adopted by the invention to solve the technical problem is that：It is a kind of based on the new of solar energy utilization technique
Combined type oil gas water three-phase separator includes entrance preseparator, solar energy heating-heat-exchanger rig, tank device.
The entrance preseparator is installed on enclosure interior one end, including sediment ejection opening, Produced Liquid entrance, solid impurity are collected
Room, profit return passage, liquid distribution mouth, cyclone separator inlet, collection chamber, gas vent, cyclone separator single tube, entrance
Preseparator cylinder, reflux hole, cyclone separator single tube are arranged circumferentially along entrance preseparator cylinder, optimally, outside
8 are arranged circumferentially, inner circumferential is evenly arranged 3；Sediment ejection opening is installed on solid impurity collecting chamber bottom, reflux hole peace
Loaded on solid impurity collecting chamber top, Produced Liquid entrance is connected with cyclone separator inlet, and gas vent is connected with collection chamber,
Liquid distribution mouthful is installed on profit return passage；Solid impurity collecting chamber, profit return passage, cyclone separator inlet and collection chamber
Entrance preseparator inner barrel is sequentially placed into from bottom to top.
Solar energy heating-the heat-exchanger rig include solar thermal collector, attemperater, heat exchange feedwater piping, circulating pump,
Exchanged heat water return pipeline and heat exchange unit, and solar thermal collector is connected by pipeline with attemperater, attemperater, circulating pump and is changed
Hot cell is sequentially connected by the feedwater piping that exchanges heat, and heat exchange unit is connected with solar thermal collector by the water return pipeline that exchanges heat, this
When, solar energy heating-heat-exchanger rig formation closed-loop path.
The tank device includes housing, gas multi-purpose station pipeline, grating type stabilier, corrugated plating coalescer, grease chamber, fuel-displaced
Mouth, delivery port, hydroecium, two grades of mist eliminators, intermediate gas pipeline and one-level mist eliminator, gas vent, one-level mist eliminator, middle gas
Body pipeline, two grades of mist eliminators, gas multi-purpose station pipelines are in turn connected to form gas piping, are set between liquid distribution mouthful and heat exchange unit
There is grating type stabilier, heat exchange unit rear is sequentially provided with corrugated plating coalescer, grease chamber, hydroecium, and grease chamber bottom is provided with oil-out,
Hydroecium bottom is provided with delivery port.
The heat exchange unit includes heat exchanger plates beam, heat exchange fin, and heat exchanger plates beam is placed in housing at profit emulsus layer, according to
Its outward appearance of oil droplet floating track shape in a rectangular trapezoid；Heat exchange fin is brazed in heat exchanger plates beam outer wall, and profile is in corrugated plate shape, and
Circular hole is opened up at its Wave crest and wave trough, while augmentation of heat transfer, makes full use of shallow pool principle to accelerate water-oil separating.
The height of the grating type stabilier is the 3/4 of body height.
The corrugated plating coalescer is in round pie, and diameter is identical with housing inner diameter, and shell is also trapped while oil-water separation
The drop of body inner space, corrugated plating is staggeredly superimposed successively, and opens up at Wave crest and wave trough circular hole.
Compared with prior art, the present invention is had an advantageous effect in that：
(1) entrance preseparator is placed in enclosure interior by the present invention, and using many cut-in type cyclone separator single tubes simultaneously
Join the form of encapsulation, increase treating capacity and improve gas-liquid separation efficiency, while using cyclonic separation that sandstone in liquid etc. is solid
Body impurity is separated before downstream separation technique is entered, and oil mixing with water is mutually free of sandstone impurity, it is to avoid the problem of blocking, is prolonged
The usage cycles of three phases separator have been grown, the operating mode of Produced Liquid instability of flow is can adapt to, range of operation is wide.
(2) present invention sets the heat exchange unit based on solar energy utilization technique in housing, can be directly to profit breast
Shape liquid is heated, and at utmost changes the viscosity of water-oil phase, accelerates water-oil separating, and origin of heat is in solar energy, by too
Positive energy thermal-arrest-heat-exchanger rig realizes that solar energy highly effective is utilized, and under the intelligent control of related intelligence control system, realizes and add
Synthetic operation between hot stove and solar energy heating-heat-exchanger rig, substantially reduces the heating energy consumption of traditional oils mixing wastewater with air phase.
(3) present invention can carry out the same of water-oil separating using diameter with housing inner diameter identical corrugated plating coalescer
When, the condensation drop floated in three phases separator internal liquid level upper air is trapped using the knock-on effect of drop, it is real
Now efficiently separate.
Brief description of the drawings
Fig. 1 is that a kind of overall appearance of the novel combination type three phases separator based on solar energy utilization technique is shown
It is intended to
Fig. 2 is that a kind of internal structure of the novel combination type three phases separator based on solar energy utilization technique is shown
It is intended to
Fig. 3 is entrance preseparator front view
Fig. 4 is entrance preseparator sectional view
Fig. 5 is C-C cross-sectional views in Fig. 4
Fig. 6 is solar energy heating-isometric test chart of heat-exchanger rig heat exchange unit
Fig. 7 is solar energy heating-heat-exchanger rig heat exchange unit top view
Fig. 8 is the partial enlarged drawing of I in Fig. 7
Fig. 9 is E-E cross-sectional views in Fig. 7
Figure 10 is the partial enlarged drawing of II in Fig. 9
Wherein, 1, solar thermal collector, 2, attemperater, 3, heat exchange feedwater piping, 4, circulating pump, 5, housing, 6, gas
Multi-purpose station pipeline, 7, entrance preseparator, 8, sediment ejection opening, 9, grating type stabilier, 10, heat exchange water return pipeline, 11, heat exchange unit,
12nd, corrugated plating coalescer, 13, grease chamber, 14, oil-out, 15, delivery port, 16, hydroecium, 17, two grades of mist eliminators, 18, intermediate gas
Pipeline, 19, one-level mist eliminator, 20, Produced Liquid entrance, 21, solid impurity collecting chamber, 22, profit return passage, 23, liquid distribution
Mouthful, 24, cyclone separator inlet, 25, collection chamber, 26, gas vent, 27, cyclone separator single tube, 28, entrance pre-separation
Device cylinder, 29, reflux hole, 30, heat exchanger plates beam, 31, heat exchange fin.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.Based on this
Embodiment in invention, it is all other that those of ordinary skill in the art are obtained on the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Fig. 1~10 are highly preferred embodiment of the present invention, and 1~10 the present invention will be further described below in conjunction with the accompanying drawings.
Referring to the drawings 1~10：A kind of novel combination type three phases separator based on solar energy utilization technique, bag
Entrance preseparator 7, solar energy heating-heat-exchanger rig, tank device are included, entrance preseparator 7 is installed on the inside of housing 5 one
End, including sediment ejection opening 8, Produced Liquid entrance 20, solid impurity collecting chamber 21, profit return passage 22, liquid distribution mouth 23, eddy flow point
From device inlet 24, collection chamber 25, gas vent 26, cyclone separator single tube 27, entrance preseparator cylinder 28, reflux hole
29, cyclone separator single tube 27 is arranged circumferentially along entrance preseparator cylinder 28, and optimally, external circumferential is evenly arranged 8
Root, inner circumferential is evenly arranged 3, and sediment ejection opening 8 is installed on the bottom of solid impurity collecting chamber 21, and it is miscellaneous that reflux hole 29 is installed on solid
The top of matter collecting chamber 21, Produced Liquid entrance 20 is connected with cyclone separator inlet 24, and gas vent 26 is connected with collection chamber 25,
Liquid distribution mouthful 23 is installed on profit return passage 22, solid impurity collecting chamber 21, profit return passage 22, cyclone separator inlet
24 and collection chamber 25 be sequentially placed into from bottom to top inside entrance preseparator cylinder 28.
Solar energy heating-heat-exchanger rig include solar thermal collector 1, attemperater 2, heat exchange feedwater piping 3, circulating pump 4,
Exchanged heat water return pipeline 10 and heat exchange unit 11, and solar thermal collector 1 is connected by pipeline with attemperater 2, attemperater 2, is followed
Ring pump 4 and heat exchange unit 11 are sequentially connected by the feedwater piping 3 that exchanges heat, and heat exchange unit 11 passes through heat exchange with solar thermal collector 1
Water return pipeline 10 is connected, now, solar energy heating-heat-exchanger rig formation closed-loop path.
Tank device include housing 5, gas multi-purpose station pipeline 6, grating type stabilier 9, corrugated plating coalescer 12, grease chamber 13,
Oil-out 14, delivery port 15, hydroecium 16, two grades of mist eliminators 17, intermediate gas pipeline 18 and one-level mist eliminator 19, gas vent
26th, one-level mist eliminator 19, intermediate gas pipeline 18, two grades of mist eliminators 17, gas multi-purpose station pipelines 6 are in turn connected to form flue
Road, is provided with grating type stabilier 9, the rear of heat exchange unit 11 is sequentially provided with ripple between liquid distribution mouthful 23 and heat exchange unit 11
Plate coalescer 12, grease chamber 13, hydroecium 16, the bottom of grease chamber 13 are provided with oil-out 14, and the bottom of hydroecium 16 is provided with delivery port 15.
Heat exchange unit 11 includes heat exchanger plates beam 30, heat exchange fin 31, and heat exchanger plates beam 30 is placed in profit emulsus layer in housing 5
Place, according to its outward appearance of oil droplet floating track shape in a rectangular trapezoid；Heat exchange fin 31 is brazed in the outer wall of heat exchanger plates beam 30, and profile is in ripple
Card shape, and circular hole is opened up at its Wave crest and wave trough, while augmentation of heat transfer, make full use of shallow pool principle to accelerate profit point
From.
The height of grating type stabilier 9 is the 3/4 of body height.
Corrugated plating coalescer 12 is in round pie, and diameter is identical with the internal diameter of housing 5, and housing is also trapped while oil-water separation
The drop of 5 inner spaces, corrugated plating is staggeredly superimposed successively, and opens up at Wave crest and wave trough circular hole.
Operation principle：According to specific operating condition, the oil gas water three phase mixing of heated stove heat to certain temperature is adopted
Go out liquid and cyclone separator inlet 24 is entered by Produced Liquid entrance 20, eddy flow point is utilized subsequently into cyclone separator single tube 27
Gas-liquid-solid separation is carried out to oil gas water three phase mixing Produced Liquid from effect, wherein the gas separated passes through cyclone separator list
The exhaust outlet of pipe 27 enters collection chamber 25, and then by the further gas-liquid separation of one-level mist eliminator 19, now clean gas enters
Enter intermediate gas pipeline 18；The liquid-solid mixture separated enters solid impurity by the lower part outlet of cyclone separator single tube 27
Collecting chamber 21, the solid impurity separated periodically is discharged through sediment ejection opening 8, and liquid enters profit return passage by reflux hole 29
22, then enter downstream separation space by liquid distribution mouthful 23, the current stabilization effect through grating type stabilier 9, flow pattern is stable
Oil water mixture flows through heat exchange unit 11, is further heated to the optimum temperature of water-oil separating, and the profit through further heating is mixed
Compound flows through corrugated plating coalescer 12, completes water-oil separating using its efficient coalescence effect, the oil phase separated enters grease chamber
13 are discharged through oil-out 14, into crude oil gathering system, and the aqueous phase separated is discharged into hydroecium 16 through delivery port 15, are entered
Sewage disposal system.The component evaporated in oil water separation process floats in the internal liquid level upper air of housing 5 and condenses into liquid
Drop, these drops are trapped when passing through corrugated plating coalescer 12 using the knock-on effect of drop, and realization is efficiently separated.
Downstream area after corrugated plating coalescer 12, i.e. grease chamber 13 and the gas-liquid two-phase in the overhead of hydroecium 16 enter by two grades of mist eliminators 17
The further gas-liquid separation of row, separates clean gas with flowing through the clean gas of intermediate gas pipeline 18 and together enters defeated outside gas
Pipeline 6, into gas handling system, so far realizes efficiently separating for oil gas water three phase.
The operation principle of solar energy heating-heat-exchanger rig：The water of certain temperature is heated to through conveying through solar thermal collector 1
The hot water that pipeline enters in attemperater 2, attemperater 2 is pumped to heat exchange feedwater piping 3 through circulating pump 4 and enters heat exchange unit
11, utilize the heat exchanger plates beam 30 and the high efficient heat exchanging efficiency of heat exchange fin 31 in heat exchange unit 11 and auxiliary water-oil separating performance pair
Oil water mixture carries out high efficient heat exchanging and water-oil separating, and the water for completing heat exchange effect returns to solar energy collection through the water return pipeline 10 that exchanges heat
In hot device 1, this process persistent loop can effectively reduce the operation energy consumption of three phases separator, realize green production.
It the foregoing is only presently preferred embodiments of the present invention and oneself, be not intended to limit the invention, all essences in the present invention
God is with principle, and any modification, equivalent substitution and improvements made etc. should be included in the scope of the protection.
Claims (7)
1. a kind of novel combination type three phases separator based on solar energy utilization technique, it is characterised in that：Including entering
Mouth preseparator (7), solar energy heating-heat-exchanger rig, tank device.
2. a kind of novel combination type oil gas water three phase separation based on solar energy utilization technique according to claim 1
Device, it is characterised in that：The entrance preseparator (7) is installed on the internal one end of housing (5), including sediment ejection opening (8), Produced Liquid enter
Mouthful (20), solid impurity collecting chamber (21), profit return passage (22), liquid distribution mouthful (23), cyclone separator inlet (24),
Collection chamber (25), gas vent (26), cyclone separator single tube (27), entrance preseparator cylinder (28), reflux hole (29), rotation
Stream separator single tube (27) is arranged circumferentially along entrance preseparator cylinder (28), and optimally, external circumferential is evenly arranged 8
Root, inner circumferential is evenly arranged 3；Sediment ejection opening (8) is installed on solid impurity collecting chamber (21) bottom, and reflux hole (29) are installed on
Solid impurity collecting chamber (21) top, Produced Liquid entrance (20) is connected with cyclone separator inlet (24), gas vent (26)
It is connected with collection chamber (25), liquid distribution mouthful (23) is installed on profit return passage (22)；Solid impurity collecting chamber (21), profit are returned
Flow chamber (22), cyclone separator inlet (24) and collection chamber (25) are sequentially placed into entrance preseparator cylinder (28) from bottom to top
It is internal.
3. a kind of novel combination type oil gas water three phase separation based on solar energy utilization technique according to claim 1
Device, it is characterised in that：Solar energy heating-the heat-exchanger rig includes solar thermal collector (1), attemperater (2), heat exchange feedwater
Pipeline (3), circulating pump (4), heat exchange water return pipeline (10) and heat exchange unit (11), solar thermal collector (1) is by pipeline with protecting
Reservoir (2) is connected, and attemperater (2), circulating pump (4) and heat exchange unit (11) are sequentially connected by the feedwater piping that exchanges heat (3),
Heat exchange unit (11) is connected with solar thermal collector (1) by the water return pipeline that exchanges heat (10), now, solar energy heating-heat exchange dress
Put to form closed-loop path.
4. a kind of novel combination type oil gas water three phase separation based on solar energy utilization technique according to claim 1
Device, it is characterised in that：The tank device includes housing (5), gas multi-purpose station pipeline (6), grating type stabilier (9), corrugated plating
Coalescer (12), grease chamber (13), oil-out (14), delivery port (15), hydroecium (16), two grades of mist eliminators (17), intermediate gas pipes
Road (18) and one-level mist eliminator (19), gas vent (26), one-level mist eliminator (19), intermediate gas pipeline (18), two grades catch mist
Device (17), gas multi-purpose station pipeline (6) are in turn connected to form gas piping, are set between liquid distribution mouthful (23) and heat exchange unit (11)
There is grating type stabilier (9), heat exchange unit (11) rear is sequentially provided with corrugated plating coalescer (12), grease chamber (13), hydroecium (16),
Grease chamber (13) bottom is provided with oil-out (14), and hydroecium (16) bottom is provided with delivery port (15).
5. a kind of novel combination type oil gas water three phase separation based on solar energy utilization technique according to claim 3
Device, it is characterised in that：The heat exchange unit (11) includes heat exchanger plates beam (30), heat exchange fin (31), and heat exchanger plates beam (30) is placed in
At the interior profit emulsus layer of housing (5), according to its outward appearance of oil droplet floating track shape in a rectangular trapezoid；Heat exchange fin (31), which is brazed in, to be changed
Hot plate beam (30) outer wall, profile is in corrugated plate shape, and opens up circular hole at its Wave crest and wave trough, while augmentation of heat transfer, fully
Accelerate water-oil separating using shallow pool principle.
6. a kind of novel combination type oil gas water three phase separation based on solar energy utilization technique according to claim 4
Device, it is characterised in that：The height of the grating type stabilier (9) is the 3/4 of housing (5) height.
7. a kind of novel combination type oil gas water three phase separation based on solar energy utilization technique according to claim 4
Device, it is characterised in that：The corrugated plating coalescer (12) is in round pie, and diameter is identical with housing (5) internal diameter, in oil-water separation
The drop of housing (5) inner space is also trapped simultaneously, and corrugated plating is staggeredly superimposed successively, and opens up at Wave crest and wave trough circular hole.
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| CN201710574317.XA CN107189810A (en) | 2017-07-14 | 2017-07-14 | A kind of novel combination type three phases separator based on solar energy utilization technique |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111686950A (en) * | 2020-06-11 | 2020-09-22 | 中科合成油技术有限公司 | Method and device for quickly separating oil from water at high temperature and high pressure |
| CN116988776A (en) * | 2023-09-27 | 2023-11-03 | 克拉玛依红山油田有限责任公司 | Photo-thermal liquid storage energy storage device |
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| CN2455329Y (en) * | 2000-11-23 | 2001-10-24 | 中国石化集团河南石油勘探局勘察设计研究院 | Three phase separator for oil, gas and water |
| CN203724817U (en) * | 2014-02-18 | 2014-07-23 | 中国石油大学(华东) | Three-phase separator applicable to gas-oil-water separation of onshore oil field |
| CN205077011U (en) * | 2015-10-09 | 2016-03-09 | 中国石油天然气股份有限公司 | Frothy crude oil three -phase separator |
| CN205743869U (en) * | 2015-12-16 | 2016-11-30 | 中石化石油工程技术服务有限公司 | Intelligent multistage three phase separator |
| CN206089246U (en) * | 2016-12-13 | 2017-04-12 | 山东普利龙压力容器有限公司 | Take profit gas three -phase separator and piece -rate system of circulation heating device |
| CN206916078U (en) * | 2017-07-14 | 2018-01-23 | 中国石油大学(华东) | A kind of novel combination type three phases separator based on solar energy utilization technique |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111686950A (en) * | 2020-06-11 | 2020-09-22 | 中科合成油技术有限公司 | Method and device for quickly separating oil from water at high temperature and high pressure |
| CN116988776A (en) * | 2023-09-27 | 2023-11-03 | 克拉玛依红山油田有限责任公司 | Photo-thermal liquid storage energy storage device |
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