CN109276915A - Separator - Google Patents
Separator Download PDFInfo
- Publication number
- CN109276915A CN109276915A CN201710599108.0A CN201710599108A CN109276915A CN 109276915 A CN109276915 A CN 109276915A CN 201710599108 A CN201710599108 A CN 201710599108A CN 109276915 A CN109276915 A CN 109276915A
- Authority
- CN
- China
- Prior art keywords
- liquid
- separator
- gas
- tank body
- branch pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- 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
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0202—Separation of non-miscible liquids by ab- or adsorption
-
- 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
- C10G33/06—Dewatering or demulsification of hydrocarbon oils with mechanical means, e.g. by filtration
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Mechanical Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
The present invention provides a kind of separators, including tank body, gas-liquid separator, liquid distributor and baffle, wherein, the lower end of the gas-liquid separator is connected with outlet tube, the lower end of the outlet tube is connected to the liquid distributor, the outlet tube and the liquid distributor are located in the tank body, and the baffle is fixed in the tank body, are located at below the liquid distributor；The liquid distributor includes the branch pipe of multiple connections, and the lower part of each branch pipe is flowed out suitable for liquid；The baffle includes arc surface, and the circular arc is recessed downwards.Separator provided by the invention can be relieved the unstable situation of the intracorporal liquid fluctuating of tank caused by the liquid of gas-liquid separator outflow and flow field.
Description
Technical field
The present invention relates to oil-gas mining technical field, in particular to a kind of separator.
Background technique
In oilfield development process, oil well liquid-producing is the mixture of crude oil, natural gas and water, in order to obtain pure original
Oil, it is necessary to separate oil well liquid-producing.Three phases separator is an important equipment in the production of oil field, oil well can be produced
Crude oil, natural gas and water in liquid separate.
A kind of prior art provides a kind of three phases separator, which includes that tank body is gentle
Liquid/gas separator, rectification element, coalescing internal and mist eliminator, the liquid isolated from the outlet tube of gas-liquid separator are fallen directly into
Into tank body.
In the implementation of the present invention, the inventors discovered that in the prior art the prior art has at least the following problems:
When the three phases separator provided using the prior art, due to the liquid velocity that is flowed out from gas-liquid separator compared with
Greatly, when falling into the intracorporal liquid of tank, it will cause the intracorporal liquid fluctuating of tank, flow field is unstable, to influence subsequent process
The effect that middle oil is separated with water.
Summary of the invention
In view of this, the present invention provides a kind of separator, can be relieved in tank body caused by the liquid of gas-liquid separator outflow
The unstable situation of liquid fluctuating and flow field.
Specifically, including technical solution below:
The present invention provides a kind of separators, including tank body, gas-liquid separator, liquid distributor and baffle, wherein
The lower end of the gas-liquid separator is connected with outlet tube, and the lower end of the outlet tube is connected to the liquid distributor,
The outlet tube and the liquid distributor are located in the tank body, and the baffle is fixed in the tank body, are located at the cloth liquid
Below device；
The liquid distributor includes the branch pipe of multiple connections, and the lower part of each branch pipe is flowed out suitable for liquid；
The baffle includes arc surface, and the circular arc is recessed downwards.
Selectively, each branch pipe is vertical with the outlet tube, and the first end of the multiple branch pipe links together
And be connected to the lower end of the outlet tube, the lower part of each branch pipe is provided with fluid hole.
Selectively, multiple fluid holes are provided on the lower part tube wall of each branch pipe, from the of each branch pipe
One end is gradually increased to second end, the size of fluid hole.
Selectively, each branch pipe is vertical with the outlet tube, and the first end of the multiple branch pipe links together
And be connected to the lower end of the outlet tube, it offers on the lower part tube wall of each branch pipe and to extend from first end to second end
Gap.
Selectively, the gas-liquid separator is cyclone gas-liquid separator.
Selectively, the separator further includes cylinder, and the upper end of the tank body is provided with the first aperture, and the cylinder is logical
First aperture is crossed to be connected to the tank interior；The first gas outlet and air inlet are provided on the barrel of the cylinder；Institute
It states and is provided with mist eliminator in cylinder；
The second gas outlet is provided on the gas-liquid separator；
Second gas outlet of the gas-liquid separator is connected to the air inlet of the cylinder；
Gas is suitable for entering in the cylinder by the air inlet, after the mist eliminator, through first outlet
The cylinder is discharged in mouth.
Selectively, weir plate is provided in the tank body, the tank body is divided into only on the weir plate by the weir plate
Two liquid storage areas of Fang Liantong.
Selectively, the separator further includes coalescing-plate, the top inner wall of the upper end of the coalescing-plate and the tank body
Connection, the lower end of the coalescing-plate far from the bottom of the tank body, the coalescing-plate be located at the weir plate and the outlet tube it
Between.
Selectively, the intracorporal liquid of the cylinder is suitable for entering the storage for being provided with the baffle by first aperture
Liquid zone.
Selectively, it is equipped with along the vertical direction in the liquid storage area for being provided with the baffle, the barrel of the tank body multiple
Fluid hole.
Selectively, in the liquid storage for being not provided with the baffle, the bottom of the tank body is provided with the second aperture.
Selectively, vortex shield is provided with above second aperture.
Selectively, in the liquid storage area for being provided with the baffle, the bottom of the tank body is provided with third aperture.
Technical solution provided in an embodiment of the present invention the utility model has the advantages that
Separator provided by the invention makes to flow out from outlet tube by the way that the liquid distributor being connected to outlet tube lower end is arranged
Liquid disperse and flow out in the same direction, the liquid of outflow, which is fallen on, can reduce liquid splash on baffle, so alleviate splashing
Caused by liquid the case where liquid fluctuating；The baffle below outlet tube, which is arranged in, can reduce the flow velocity of liquid, further alleviate
The unstable situation of liquid fluctuating caused by the intracorporal liquid of tank and flow field is flowed to, and then improves the oil and moisture in subsequent liquid
From effect.
Detailed description of the invention
To describe the technical solutions in the embodiments of the present invention more clearly, make required in being described below to embodiment
Attached drawing is briefly described, it should be apparent that, drawings in the following description are only some embodiments of the invention, for
For those of ordinary skill in the art, without creative efforts, it can also be obtained according to these attached drawings other
Attached drawing.
Fig. 1 is a kind of schematic diagram of separator in one embodiment of the invention；
Fig. 2 is a kind of schematic diagram of liquid distributor in one embodiment of the invention；
Fig. 3 is a kind of schematic diagram of liquid distributor in one embodiment of the invention；
Fig. 4 is a kind of schematic diagram of liquid distributor in one embodiment of the invention.
Appended drawing reference in figure is respectively as follows:
1, tank body；
2, inlet；
3, gas-liquid separator；
4, coalescing-plate；
5, cylinder；
6, mist eliminator；
7, the first gas outlet；
8, the first liquid storage area；
9, plug；
10, weir plate；
11, plug；
12, the second liquid storage area；
13, plug；
14, support column；
15, baffle；
16, liquid distributor；
17, the first vortex shield；
18, the second vortex shield；
19, pipeline；
20, the first aperture；
21, the second gas outlet；
22, air inlet；
23, branch pipe；
24, fluid hole；
25, connecting tube.
Specific embodiment
To keep technical solution of the present invention and advantage clearer, below in conjunction with attached drawing to embodiment of the present invention make into
One step it is described in detail.
One embodiment of the invention provides a kind of separator, as shown in Figure 1, including tank body 1, gas-liquid separator 3, cloth liquid
Device 16 and baffle 15, wherein
The lower end of gas-liquid separator 3 is connected with outlet tube 20, and the lower end of outlet tube 20 is connected to liquid distributor 16, outlet tube
20 and liquid distributor 16 be located inside tank body 1, baffle 15 is fixed in tank body 1, is located at the lower section of liquid distributor 16；
Liquid distributor 16 includes the branch pipe of multiple connections, and the lower part of each branch pipe is flowed out suitable for liquid；
Baffle 15 includes arc surface, and arc surface edge is high and center is low.
The working principle for producing device with regard to core provided in this embodiment below, which is given, to be described:
When in use, oil well liquid-producing being injected to gas-liquid separator 3, oil well liquid-producing is carried out gas-liquid separation by gas-liquid separator 3,
Liquid flows out into liquid distributor 16 by outlet tube 20, passes through under multiple branch pipes into the liquid in liquid distributor 16
Portion's outflow is fallen on the arc surface of baffle 15, and is flowed in tank body by the edge of baffle 15.
Separator provided in this embodiment is made by the way that the liquid distributor 16 being connected to 20 lower end of outlet tube is arranged from liquid out
The liquid that pipe 20 flows out disperses and flows out in the same direction, and the liquid of outflow, which is fallen on, can reduce liquid splash on baffle 15, in turn
The case where alleviating liquid fluctuating caused by the liquid to splash；The baffle 15 below outlet tube 20, which is arranged in, can reduce liquid
Flow velocity is further alleviated and flows to the unstable situation of liquid fluctuating caused by the intracorporal liquid of tank and flow field.Due in liquid
The density of oil is less than the density of water, and the two is separated according to density contrast, when liquid fluctuating, can aggravate the mixing of oil and water,
It is unfavorable for the two separation.It is intracorporal to can be relieved tank caused by the liquid of gas-liquid separator outflow for separator provided in this embodiment
The unstable situation of liquid fluctuating and flow field, and then improve oil and water separating effect in subsequent liquid.
In the present embodiment, in order to become apparent from the effect of baffle 15, the general area that baffle 15 is arranged is larger, makes from cloth
The liquid of liquid device outflow can be entirely fallen in the recess of baffle 15.As shown in Figure 1, baffle 15 can be fixed by support column 14
In 1 bottom of tank body.
In the present embodiment, the length of outlet tube 20 can make liquid distributor 16 close to the bottom of tank body 1, in this way, in tank body 1
There are liquid when a certain amount of liquid, flowed in tank body 1 from baffle 15 to be introduced into the already existing liquid of tank body 1, thus
The liquid flowed out from baffle 15 is washed in existing liquid in uphill process, and the efficiency of water-oil separating can be improved.
As a kind of embodiment of liquid distributor 16, the first end of multiple branch pipes of liquid distributor 16 link together and
It is connected to the lower end of outlet tube 20, the lower part of each branch pipe is provided with fluid hole.Each branch pipe is vertical with outlet tube 20, Mei Gezhi
Fluid hole is provided on pipe.In this way, be dispersed into multiple branch pipes from the liquid that outlet tube 20 flows out, and from multiple branch pipe lower parts
Fluid hole outflow flows into the flow direction of the liquid in branch pipe from outlet tube 20 since each branch pipe is vertical with outlet tube 20
It changes, momentum reduces, and flow velocity becomes smaller, so that the flow velocity when liquid flows out branch pipe is relative to directly from the liquid of outlet tube 20
The flow velocity of body is smaller, and flows out in the same direction from the liquid that branch pipe flows out, so as to reduce fall on baffle 15 after liquid
Splashing amount.As a kind of improvement of the embodiment, multiple fluid holes are provided on the tube wall of each branch pipe lower part, from the of branch pipe
To second end, the size of the fluid hole on the branch pipe is gradually increased for one end.Since the first end of branch pipe is connected to outlet tube 20, then
The fluid in branch pipe is flowed into preferentially from the fluid hole outflow of the first end close to branch pipe, i.e., fluid is in the first end close to branch pipe
The flow velocity of fluid hole is greater than the flow velocity of the fluid hole far from first end.From the first end of branch pipe to second end, the size of fluid hole
It is gradually increased, it is ensured that the uniform flow of the liquid flowed out from each fluid hole is further reduced liquid after falling on baffle 15
Splashing amount optimizes the cloth liquid effect of liquid distributor 16.
As the first example of the embodiment, as shown in Fig. 2, liquid distributor 16 may include four branch pipes 23, four
The first end of branch pipe 23 connects and organizes across pipe, two of them branch pipe 23 point-blank, perpendicular to another two branch pipe
Straight line where 23.From the first end of each branch pipe 23 to second end, the size of fluid hole 24 is gradually increased.But the present invention is unlimited
In this, in other embodiments, the branch pipe for forming liquid distributor 16 can also be other quantity, for example, liquid distributor 16 may include
The first end connection of three branch pipes, three branch pipes forms the angle between two branch pipes adjacent in T-type pipe or three branch pipes
It is identical.
As second of example of the embodiment, as shown in figure 3, liquid distributor 16 may include 10 branch pipes 23 and connection
Pipe 25, wherein the first end of 5 branch pipes 23 is connected to the side of connecting tube 25, in addition 5 branch pipes 23 and connecting tube 25 is another
Side connection, the upper end of connecting tube 25 are connected to the lower end of outlet tube 20, and outlet tube 20 is perpendicular to 10 branch pipes 23.It needs to illustrate
, Fig. 3 with the quantity of branch pipe 23 be 10 be illustrated, in other embodiments, branch pipe 23 can also for other number
Amount.
As the third example of the embodiment, as shown in figure 4, liquid distributor 16 includes 5 branch pipes, 23,5 branch pipes
23 first end is connected to the side of connecting tube 25, and the upper end of connecting tube 25 is connected to the lower end of outlet tube 20, and outlet tube 20 hangs down
Directly in 5 branch pipes 23.It is illustrated it should be noted that Fig. 4 is 5 with the quantity of branch pipe 23, in other embodiments,
Branch pipe 23 can also be other quantity.
As the another embodiment of liquid distributor 16, multiple branch pipes of liquid distributor 16 are vertical with outlet tube 20, more
The upper end of a branch pipe is connected to the lower end of outlet tube 20, is offered on the lower part tube wall of each branch pipe and is prolonged from first end to second end
The gap stretched.It is same that the liquid that outlet tube 20 flows out enters the gap of dispersion and the lower part tube wall along each branch pipe in multiple branch pipes
Direction outflow, so as to reduce fall on baffle 15 after liquid splashing amount.Wherein, in the embodiment, liquid distributor 16 can be wrapped
Four branch pipes are included, four branch pipe compositions are cross, or including 3 branch pipes, three branch pipes form T-type, or including multiple flat
Capable branch pipe.
In the present embodiment, as shown in Figure 1, being provided with inlet 2 on the side wall of gas-liquid separator 3, top is provided with
Two gas outlets 21.The preferable cyclone gas-liquid separator of gas-liquid separation effect can be selected in gas-liquid separator 3.Cyclone gas-liquid separator is
Gas-liquid is set to realize that a kind of separator separated, gas-liquid mixture enter cyclone gas-liquid from 2 tangential inlet of inlet by centrifugal force
The eddy flow that generates after separator generates the centrifugal force for being much larger than gravity, since gas and fluid density difference are larger, it is suffered from
Mental and physical efforts difference is larger, so that liquid is radially pushed to outside, and is discharged by outlet tube 20, gas motion to center, from top
The second gas outlet 21 discharge.Other kinds of gas-liquid separator can also be used in other embodiments of the invention.
In the present embodiment, as shown in Figure 1, separator may also include cylinder 5, the upper end of tank body 1 is provided with the first aperture
20, cylinder 5 inside the first aperture 20 and tank body 1 by being connected to；The first gas outlet 7 and air inlet are provided on the barrel of cylinder 5
22；Mist eliminator 6 is provided in cylinder 5；
Second gas outlet 21 of gas-liquid separator 3 is connected to the air inlet 22 of cylinder 5；
Gas is suitable for entering in cylinder 5 by air inlet 22, and after mist eliminator 6, cylinder is discharged through the first gas outlet 7
5。
As shown in Figure 1, the second gas outlet 21 of gas-liquid separator 3 is connected to the air inlet 22 of cylinder 5 by pipeline 19.
Therefore mist eliminator 6 can separate the liquid carried in the gas entered in cylinder 5.Divide from gas-liquid separator 3
It separates out after the gas come enters cylinder 5 by pipeline 19, gas passes through mist eliminator 6, and mist eliminator 6 is by the drop separation in gas
Out, isolated drop flows down and agglomerates to form larger drop, overcome Surface Tension of Liquid Drops and uprising gas to its buoyancy and
It falls and passes through the first aperture and flow in tank body 1.
Folded plate type, screen type, material filling type and the diversified forms such as centrifugal can be selected in mist eliminator 6.It is with screen type mist eliminator
Example is illustrated, and when the silk screen in the gas of carrying of liquids and screen type mist eliminator bumps against, gas wears net and mistake, is carried in gas
Droplet collision to silk screen after, flow down and agglomerate to form larger drop, its surface tension and gas are overcome when drop is larger
It falls after buoyancy.
In the present embodiment, as shown in Figure 1, being provided with weir plate 10 in tank body 1, tank body 1 is divided into only on weir by weir plate 10
The first liquid storage area 8 and the second liquid storage area 12 being connected to above plate 10.The lower end of weir plate 10 is connected with the bottom of tank body 1, weir plate 10
Opposite two sides two sides opposite with tank body 1 connect, the upper end of weir plate 10 is not contacted with the top of tank body 1, thus weir plate
Tank body 1 is divided into the first liquid storage area 8 and the second liquid storage area 12 being only connected to above weir plate 10 by 10.
As shown in Figure 1, liquid distributor 16 and baffle 15 are respectively positioned in the second liquid storage area 12, the liquid flowed out from outlet tube 20
Body enters in the second liquid storage area 12 after liquid distributor 16 and baffle 15.You Heshui since oil is different with water density, in liquid
It is layered, oil level is in the upper layer of water, and when the liquid in the second liquid storage area 12 reach a certain height, the oil on upper layer crosses weir plate
10 flow in the first liquid storage area 8, so that oil is separated.
In the present embodiment, the liquid in cylinder 5 is suitable for entering in the second liquid storage area 12 by the first aperture 20.Such as
Shown in Fig. 1, the first aperture 20 is located at the part at the top of the tank body 1 of 12 top of the second liquid storage area.Due to the liquid flowed out from cylinder 5
Body is the mixture of water and oil, needs to enter the interior oil that carries out of the second liquid storage area 12 and separates with water.
In the present embodiment, as shown in Figure 1, in the liquid storage area for being not provided with baffle 15, namely in the first liquid storage area 8,
The bottom of tank body 1 is provided with the second aperture (unused appended drawing reference is shown in figure, is located at plug 9 and the second vortex shield 17).This
Sample takes out plug 9 out of second aperture, and the oil in the first liquid storage area 8 can be flowed out by the second aperture, does not need to release oil
When, using plug 9 by the second plugging holes.
In the present embodiment, as shown in Figure 1, being provided with the second vortex shield 18 above the second aperture.When oil is from the second aperture
When interior outflow, the second aperture nearby can generate vortex, cause liquid fluctuating, and the second vortex shield 18 is vertical with vortex direction of rotation,
It can avoid or reduce the generation of vortex, reduce liquid fluctuating.
In the present embodiment, tank body 1 is provided with multiple fluid holes (figure along the vertical direction on the barrel of the second liquid storage area 12
In be not shown).Outlet tube is connected separately on the outside of each fluid hole.In this way, 1 different height of tank body can be taken out from multiple fluid holes
The liquid of liquid level, to detect the water content of different liquid level liquid.
In the present embodiment, as shown in Figure 1, in the liquid storage area for being provided with baffle 15, namely in the second liquid storage area 12, tank
The bottom of body 1 is provided with third aperture (unused appended drawing reference is shown in figure, is located at plug 11 and the first vortex shield 18).This
Sample takes out plug 11 from third aperture, and tank body 1 is discharged through third aperture in the low oil-containing water of lower part in the second liquid storage area 12.
In the present embodiment, as shown in Figure 1, being provided with the first vortex shield 17 above third aperture.When liquid is opened from third
When flowing out in hole, third aperture nearby can generate vortex, cause liquid fluctuating, and the first vortex shield 17 hangs down with vortex direction of rotation
Directly, the generation that can avoid or reduce vortex, reduces liquid fluctuating.
As shown in Figure 1, being provided with the 4th aperture on the bottom of tank body 1, (unused appended drawing reference is shown in figure below baffle 15
Out, it is located at plug 13).When containing silt from the liquid that outlet tube 20 flows out, can be deposited near the baffle 15 of tank body 1
Region.When region product sand is more, openable plug 13 is discharged.
In the present embodiment, as shown in Figure 1, separator further includes coalescing-plate 4, the upper end of coalescing-plate 4 and the top of tank body 1
Inner wall connection, the lower end of coalescing-plate 4 is far from the bottom of tank body 1, and coalescing-plate 4 is between weir plate 10 and outlet tube 20.
4 plate of coalescing-plate can promote the separation of oil and water, and corrugated plate type can be used in coalescing-plate 4, and surface has lipophilicity,
Drop in water can be adsorbed by coalescing-plate and be formed bigger oil droplet, thus the ascent rate rapid growth of oil droplet in water, when
When oil droplet is floated up to above the interface of water and oil, the separation with water can be realized.
In embodiment provided herein, it should be understood that term " first ", " second " etc. are only used for description mesh
, it is not understood to indicate or imply relative importance or implicitly indicates the quantity of indicated technical characteristic.
The above is merely for convenience of it will be understood by those skilled in the art that technical solution of the present invention, not to limit
The present invention.All within the spirits and principles of the present invention, any modification, equivalent replacement, improvement and so on should be included in this
Within the protection scope of invention.
Claims (14)
1. a kind of separator, which is characterized in that including tank body, gas-liquid separator, liquid distributor and baffle, wherein
The lower end of the gas-liquid separator is connected with outlet tube, and the lower end of the outlet tube is connected to the liquid distributor, described
Outlet tube and the liquid distributor are located in the tank body, and the baffle is fixed in the tank body, are located at the liquid distributor
Lower section；
The liquid distributor includes the branch pipe of multiple connections, and the lower part of each branch pipe is flowed out suitable for liquid；
The baffle includes arc surface, and the circular arc is recessed downwards.
2. separator according to claim 1, which is characterized in that each branch pipe is vertical with the outlet tube, described
The first end of multiple branch pipes links together and is connected to the lower end of the outlet tube, and the lower part of each branch pipe is provided with out
Fluid apertures.
3. separator according to claim 2, which is characterized in that be provided on the lower part tube wall of each branch pipe multiple
Fluid hole, from the first end of each branch pipe to second end, the size of fluid hole is gradually increased.
4. separator according to claim 1, which is characterized in that each branch pipe is vertical with the outlet tube, described
The first end of multiple branch pipes links together and is connected to the lower end of the outlet tube, opens on the lower part tube wall of each branch pipe
Equipped with the gap extended from first end to second end.
5. separator according to claim 1, which is characterized in that the gas-liquid separator is cyclone gas-liquid separator.
6. separator according to claim 1, which is characterized in that the separator further includes cylinder, the tank body it is upper
End is provided with the first aperture, and the cylinder is connected to by first aperture with the tank interior；On the barrel of the cylinder
It is provided with the first gas outlet and air inlet；Mist eliminator is provided in the cylinder；
The second gas outlet is provided on the gas-liquid separator；
Second gas outlet of the gas-liquid separator is connected to the air inlet of the cylinder；
Gas is suitable for entering in the cylinder by the air inlet, after the mist eliminator, arranges through first gas outlet
The cylinder out.
7. separator according to claim 6, which is characterized in that be provided with weir plate in the tank body, the weir plate is by institute
It states tank body and is divided into two liquid storage areas being only connected to above the weir plate.
8. separator according to claim 7, which is characterized in that the separator further includes coalescing-plate, the coalescing-plate
Upper end connect with the top inner wall of the tank body, the lower end of the coalescing-plate is far from the bottom of the tank body, the coalescing-plate
Between the weir plate and the outlet tube.
9. separator according to claim 7, which is characterized in that the intracorporal liquid of cylinder is suitable for opening by described first
Hole enters the liquid storage area for being provided with the baffle.
10. separator according to claim 7, which is characterized in that in the liquid storage area for being provided with the baffle, the tank body
Barrel on along the vertical direction be equipped with multiple fluid holes.
11. separator according to claim 7, which is characterized in that in the liquid storage for being not provided with the baffle, the tank
The bottom of body is provided with the second aperture.
12. separator according to claim 11, which is characterized in that be provided with vortex shield above second aperture.
13. separator according to claim 7, which is characterized in that in the liquid storage area for being provided with the baffle, the tank
The bottom of body is provided with third aperture.
14. separator according to claim 13, which is characterized in that be provided with vortex shield above the third aperture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710599108.0A CN109276915A (en) | 2017-07-21 | 2017-07-21 | Separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710599108.0A CN109276915A (en) | 2017-07-21 | 2017-07-21 | Separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109276915A true CN109276915A (en) | 2019-01-29 |
Family
ID=65185622
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710599108.0A Pending CN109276915A (en) | 2017-07-21 | 2017-07-21 | Separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109276915A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110483231A (en) * | 2019-08-21 | 2019-11-22 | 东营市科德化工有限公司 | A kind of energy-saving and environment-friendly isooctane purification tower |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2294100Y (en) * | 1997-06-02 | 1998-10-14 | 华东理工大学 | Disc like teethed hole type tube liquid distributor |
| CN201309911Y (en) * | 2008-12-08 | 2009-09-16 | 中国石油天然气股份有限公司 | Oil-water high-efficiency processor |
| CN102240526A (en) * | 2011-05-12 | 2011-11-16 | 中国石油天然气集团公司 | Gas lift type liquid distributor and reactor inner part |
| 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 |
| CN105176572A (en) * | 2015-10-09 | 2015-12-23 | 中国石油天然气股份有限公司 | Three-phase separator for foamed crude oil |
| 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 |
| CN205518723U (en) * | 2016-03-01 | 2016-08-31 | 湖北宏大玻璃制品股份有限公司 | Inside the drum goes out liquid formula glass cleaning machine |
| CN206107923U (en) * | 2016-09-05 | 2017-04-19 | 珠海经济特区美司达实业有限公司 | Emulsion pump unit with go out liquid buffering and locking function |
| CN206188744U (en) * | 2016-11-24 | 2017-05-24 | 胜利油田物华石油装备制造有限公司 | High -efficient electric dewaterer of horizontal flow |
| CN106925002A (en) * | 2017-04-24 | 2017-07-07 | 延长油田股份有限公司 | A kind of sludge drainage system with silt aggregation capability |
-
2017
- 2017-07-21 CN CN201710599108.0A patent/CN109276915A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2294100Y (en) * | 1997-06-02 | 1998-10-14 | 华东理工大学 | Disc like teethed hole type tube liquid distributor |
| CN201309911Y (en) * | 2008-12-08 | 2009-09-16 | 中国石油天然气股份有限公司 | Oil-water high-efficiency processor |
| CN102240526A (en) * | 2011-05-12 | 2011-11-16 | 中国石油天然气集团公司 | Gas lift type liquid distributor and reactor inner part |
| 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 |
| CN105176572A (en) * | 2015-10-09 | 2015-12-23 | 中国石油天然气股份有限公司 | Three-phase separator for foamed crude oil |
| 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 |
| CN205518723U (en) * | 2016-03-01 | 2016-08-31 | 湖北宏大玻璃制品股份有限公司 | Inside the drum goes out liquid formula glass cleaning machine |
| CN206107923U (en) * | 2016-09-05 | 2017-04-19 | 珠海经济特区美司达实业有限公司 | Emulsion pump unit with go out liquid buffering and locking function |
| CN206188744U (en) * | 2016-11-24 | 2017-05-24 | 胜利油田物华石油装备制造有限公司 | High -efficient electric dewaterer of horizontal flow |
| CN106925002A (en) * | 2017-04-24 | 2017-07-07 | 延长油田股份有限公司 | A kind of sludge drainage system with silt aggregation capability |
Non-Patent Citations (1)
| Title |
|---|
| 崔德文等: "《黄金矿实用手册》", 31 December 1990, 工人出版社 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110483231A (en) * | 2019-08-21 | 2019-11-22 | 东营市科德化工有限公司 | A kind of energy-saving and environment-friendly isooctane purification tower |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US8398756B2 (en) | Separator with liquid carry-over reduction assembly | |
| AU2009344910B2 (en) | Apparatus and method for separation of phases in a multiphase flow | |
| CN103566698B (en) | Gas-liquid-solid three-phase separator | |
| JPS61204017A (en) | Column for removing liquid from gas | |
| US20030154860A1 (en) | Separators for three-phase or two-phase fluid mixtures realized with a centrifugal device designed for the separation of the gas from the liquid mixture | |
| CN208130745U (en) | A kind of gas-liquid separator safety can | |
| CN204824746U (en) | Multi -functional oily deareator | |
| CN107899307A (en) | A kind of screw type gas-liquid separator | |
| CN105597378B (en) | A kind of gas-liquid light oil three-phase separating device | |
| US3722184A (en) | Apparatus for separating oil and gas from a foaming crude oil stream | |
| CN102641609A (en) | Elevation-type oil-gas-water three-phase separator with high water ratio | |
| CN105176572B (en) | A kind of frothy crude oil three phase separator | |
| CN109276915A (en) | Separator | |
| CN207598224U (en) | A kind of shale gas special horizontal gas-liquid sand three-phase separator measurement sled | |
| CN206652345U (en) | A kind of liquid foam coalescing separator | |
| CN206613222U (en) | A kind of three phase separator | |
| CN205699611U (en) | Ocean platform gravity type oil-gas-water separator | |
| CN209714376U (en) | A kind of oil field development tubular type degasser | |
| CN205699869U (en) | A kind of gs-oil separator | |
| CN204552725U (en) | The efficient oil, gas, water and sand four-phase separator of a kind of oil gas field | |
| CN2868379Y (en) | Mixed solvent phase splitter | |
| CN206244731U (en) | A kind of three phases separator | |
| US20210154601A1 (en) | Sand separator with gas vent | |
| CN104874206B (en) | Separator tube bank eddy flow inlet device | |
| CN108283841A (en) | A kind of spiral gas-liquid separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190129 |