CN106761657A - A kind of multistage natural gas gas-liquid separation device and method under water - Google Patents
A kind of multistage natural gas gas-liquid separation device and method under water Download PDFInfo
- Publication number
- CN106761657A CN106761657A CN201710137273.4A CN201710137273A CN106761657A CN 106761657 A CN106761657 A CN 106761657A CN 201710137273 A CN201710137273 A CN 201710137273A CN 106761657 A CN106761657 A CN 106761657A
- Authority
- CN
- China
- Prior art keywords
- separation device
- core pipe
- eddy flow
- gas
- discharge opeing
- 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
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 70
- 238000000926 separation method Methods 0.000 title claims abstract description 63
- 239000007788 liquid Substances 0.000 title claims abstract description 49
- 239000003345 natural gas Substances 0.000 title claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 32
- 238000000034 method Methods 0.000 title claims abstract description 8
- 238000004581 coalescence Methods 0.000 claims abstract description 34
- 239000007789 gas Substances 0.000 claims abstract description 26
- 230000007246 mechanism Effects 0.000 claims abstract description 18
- 239000003595 mist Substances 0.000 claims abstract description 11
- 239000007791 liquid phase Substances 0.000 claims description 17
- 230000005484 gravity Effects 0.000 claims description 9
- 239000003949 liquefied natural gas Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003112 inhibitor Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/34—Arrangements for separating materials produced by the well
- E21B43/36—Underwater separating arrangements
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
The invention discloses a kind of multistage natural gas gas-liquid separation device and method under water, it includes the first stage separation device, second-stage separation device and the third level separator that are sequentially connected in series from the bottom to top：First stage separation device includes horizontally disposed tank body, is arranged at the air flap near tank body air inlet, the spiral case separative element for being arranged at the coalescence silk screen at air flap rear and being arranged at tank body gas outlet；Second-stage separation device includes the eddy flow core pipe being connected with tank body gas outlet, the multiple eddy flow mechanisms being arranged inside eddy flow core pipe and the first discharge opeing sleeve pipe being set in outside eddy flow core pipe；The first discharge opeing latasuture is offered on the eddy flow core pipe bottom tube wall on rear side of eddy flow mechanism each described；Third level separator include with the eddy flow core pipe coalescence core pipe that be connected of outlet, be arranged at catching mist silk screen and be set in the second discharge opeing of the outside sleeve pipe for coalescing core pipe inside coalescence core pipe；Multiple second discharge opeing latasutures are also opened up on the bottom tube wall of coalescence core pipe.
Description
Technical field
The present invention relates to a kind of natural gas gas-liquid separation equipment and method, more particularly to a kind of multistage natural gas gas-liquid under water
Separator and method.
Background technology
With advances in technology and international community is to the demand of natural gas energy resource, the construction of natural gas fields by land under water,
By shallow water to deep water.The construction of natural gas fields is generally accompanied by NGL and water, and NGL and water are in natural gas
Can cause to flow security risk, the particularly conveying of long range tieback or standpipe tieback deep water platform in course of conveying.For producing
The less gas field of water, can be by injecting the hydrate inhibitors such as ethylene glycol under water, and being then delivered to platform carries out natural gas gas
Liquid separating treatment；For High water cut gas field, not only hydrate inhibitor demand is big, costly, but also can greatly increase conveying
Pressure, causes pressure to produce to the flow production in gas field, and shut-in pressure is high or even cannot the adverse effect such as flow production.Therefore, for
High water cut gas field needs to be separated under water.Gas production and the gas liquid ratio meeting during Development and Production of deep water natural gas field
Constantly fluctuation, and degree of fluctuation is than larger, and conventional separator is difficult in the whole life cycle of natural gas field exploitation
It is attained by efficiently separating.
Currently, some separators are separated suitable for containing large amount of liquid, will there is separative efficiency in the case where liquid phase is fewer
Low problem；Some problems are efficiently separated suitable for low operating mode containing liquid, and often there is liquid phase in the case where liquid phase is relatively more breaks
It is broken, entrainment the problems such as, so as to cause separative efficiency low.
The content of the invention
Regarding to the issue above, natural gas can be realized in different operating modes containing liquid it is an object of the invention to provide a kind of
The gas of multistage natural under water gas-liquid separation device and method that gas liquid high-efficiency is separate.
To achieve the above object, the present invention uses following technical scheme：A kind of multistage natural gas gas-liquid separation device under water,
Characterized in that, it includes that the first stage separation device, second-stage separation device and the third level that are sequentially connected in series from the bottom to top separate
Device：The first stage separation device includes horizontally disposed tank body, is arranged at the air flap near the tank body air inlet,
The spiral case separative element for being arranged at the coalescence silk screen at the air flap rear and being arranged at the tank body gas outlet；It is described
Second-stage separation device includes the eddy flow core pipe being connected with the tank body gas outlet, is arranged at the multiple inside the eddy flow core pipe
Eddy flow mechanism and the first discharge opeing sleeve pipe being set in outside the eddy flow core pipe；On rear side of eddy flow mechanism each described
The first discharge opeing latasuture is offered on the eddy flow core pipe bottom tube wall；The third level separator includes and the eddy flow core
The coalescence core pipe of pipe outlet connection, is arranged at catching mist silk screen and be set in the coalescence core pipe inside the coalescence core pipe
Outside second discharge opeing sleeve pipe；Multiple second discharge opeing latasutures are also opened up on the bottom tube wall of the coalescence core pipe.
The bottom of the tank body, the first discharge opeing sleeve pipe and the second discharge opeing sleeve pipe is provided with draining pipe.
The coalescence silk screen is arranged in the tank body upper inside walls at the air flap rear, and the coalescence
Silk screen bottom does not contact with the tank base.
Multiple eddy flow mechanisms arrange in the inside of the eddy flow core pipe along the axis spaced series of the eddy flow core pipe.
Multiple second-stage separation devices in parallel above the first stage separation device, each second level separates
Third level separator described in device correspondence series connection one, in each second-stage separation device and each third level separator
Porch set control valve.
The tank body uses pressure container cylinder.
The eddy flow mechanism include deflection cone and along the deflection cone middle part of sliding channel circumferencial direction it is uniform make vane piece.
Present invention also offers a kind of separation method based on multistage natural gas gas-liquid separation device under water, including following step
Suddenly：
1) gas field natural gas containing liquid first passes around first stage separation device and carries out gas-liquid separation under water；Natural gas containing liquid enters
Tank body, the most of liquid containing liquid natural gas condenses into drop after inlet baffle is encountered and is separated under gravity,
Then by coalescence silk screen, liquid in air-flow is agglomerated into big drop to air-flow in silk screen is coalesced, under gravity directly from
Coalesced filament is dripped on the net, and air-flow goes successively to spiral case separative element, and under the influence of centrifugal force, Partial Liquid Phase is separated,
The liquid phase isolated in first stage separation device is discharged through draining pipe；
2) through step 1) air-flow after treatment enters second-stage separation device, and air-flow is along the flowing of eddy flow core pipe successively by one
The eddy flow mechanism of the series connection of fixed number amount, vane piece is made, droplet is thrown to eddy flow core pipe side wall under the influence of centrifugal force, and
The first discharge opeing sleeve pipe is discharged to along the first discharge opeing latasuture in the side wall of eddy flow core pipe, the liquid phase for separating is arranged through draining pipe
Go out；
3) through step 2) treatment after air-flow enter third level separator, air-flow along coalescence core pipe flowing through catching mist silk
Net, the liquid phase in air-flow encounter catch mist silk screen after can constantly coalesce, droplet constantly gathers into big drop, and big drop is in gravity
Dripped under effect, the second discharge opeing sleeve pipe be discharged to then along the second discharge opeing latasuture, the liquid phase for separating is discharged through draining pipe,
Natural gas after being separated through three-level discharges transfer through the outlet of coalescence core pipe.
The present invention uses above technical scheme, and it has the following advantages that：1st, the present invention by the first separator, second point
It is sequentially connected in series from top to bottom from device and the 3rd separator, it is not at the same level suitable for the different operating modes of natural gas containing liquid, Neng Gouzhen
Gas liquid high-efficiency is separated can be realized to different operating modes containing liquid.2nd, in second-stage separation device, multiple eddy flow mechanisms exist the present invention
Successively along the axis direction interval setting of eddy flow core pipe in eddy flow core pipe, natural gas containing liquid can be realized in second-stage separation device
It is middle through multiple gas-liquid centrifugation, put forward the gas-liquid separation efficiency of containing large amount of liquid natural gas.3rd, the present invention passes through first stage separation device
Top multiple second-stage separation device in parallel, one third level separator of each second-stage separation device series connection, in the second fraction
Control valve is set from the porch of device and third level separator, can be controlled according to the gas production in gas field in running order
Second-stage separation device and third level separator number, ensure that the efficient of in each separator gas-liquid separation
Property simultaneously put forward containing large amount of liquid natural gas processing amount.4th, tank body of the invention uses pressure container cylinder, ensure that the pressure-bearing of tank body
Ability, it is ensured that the safe handling of whole device.
Brief description of the drawings
Fig. 1 is overall structure diagram of the invention；
Fig. 2 is the structural representation of eddy flow mechanism of the invention.
Specific embodiment
The present invention is described in detail with reference to the accompanying drawings and examples.
As shown in figure 1, according to the gas gas-liquid separation device of multistage natural under water proposed by the present invention, it is separated including the first order
Device 1, second-stage separation device 2 and third level separator 3, first stage separation device 1, second-stage separation device 2 and the 3rd
Level separator 3 is sequentially connected in series from top to bottom.
Wherein, first stage separation device 1 includes tank body 11, air flap 12, coalescence silk screen 13 and spiral case separative element 14,
Tank body 11 is horizontally disposed with, and its one end top has air inlet, and other end top has gas outlet, and air flap 12 is arranged on tank body
In 11 and near the air inlet of tank body 11.Coalescence silk screen 13 is arranged in the upper inside walls of tank body 11 at the rear of air flap 12
On, and coalescence the bottom of silk screen 13 do not contacted with tank body 11.Spiral case separative element 14 is also arranged in tank body 11 and positioned at tank body 11
Gas outlet at, the bottom of tank body 11 connection discharge opeing common excretory duct 4.
Second-stage separation device 2 includes eddy flow core pipe 21, eddy flow mechanism 22 and discharge opeing sleeve pipe 23, the entrance of eddy flow core pipe 21
Connect the gas outlet of tank body 11, the inside of eddy flow core pipe 21 along eddy flow core pipe 21 axis spaced series multiple eddy flow mechanisms
22, offer discharge opeing latasuture 211 on the bottom tube wall of eddy flow core pipe 21 positioned at each rear side of eddy flow mechanism 22.Discharge opeing sleeve pipe
23 outsides for being set in eddy flow core pipe 21, the bottom of discharge opeing sleeve pipe 23 is provided with for connecting discharge opeing sleeve pipe 23 and discharge opeing common excretory duct
4 the first draining pipe 24.
Third level separator 3 includes coalescence core pipe 31, catches mist silk screen 32 and discharge opeing sleeve pipe 33, coalesces the entrance of core pipe 31
Outlet with eddy flow core pipe 21 is connected, and coalesces outlet and the external connection of core pipe 31.Set in the inside of coalescence core pipe 31 and catch mist
Silk screen 32, multiple discharge opeing latasutures 311 are opened up on the bottom tube wall of coalescence core pipe 31.Discharge opeing sleeve pipe 33 is set in coalescence core pipe 31
Outside, the bottom of discharge opeing sleeve pipe 33 is provided with the second draining pipe 34 for connecting discharge opeing sleeve pipe 33 and discharge opeing common excretory duct 4.
It is possible to further in the top of first stage separation device 1 multiple second-stage separation device 2 in parallel, each second level
Correspondence one third level separator 3 of series connection of separator 2, in each second-stage separation device 2 and each third level separator 3
Porch set control valve 5.
Further, it is the underwater pressure-bearing ability of guarantee tank body 11, tank body 11 is pressure container cylinder.
Further, as shown in Fig. 2 eddy flow mechanism 22 includes deflection cone a and the middle part of sliding channel circumferencial direction along deflection cone a
Uniform makes vane piece b.
Based on the multistage natural gas gas-liquid separation device provided in above-described embodiment, present invention also offers a kind of many under water
Level natural gas gas-liquid separating method, comprises the following steps：
1) gas field natural gas containing liquid first passes around first stage separation device 1 and carries out gas-liquid separation under water；Natural gas containing liquid enters
Enter tank body 11, the most of liquid containing liquid natural gas condenses into drop after inlet baffle 12 is encountered and separated under gravity
Get off, then by coalescence silk screen 13, the liquid in air-flow is agglomerated into big drop to air-flow in silk screen 13 is coalesced, in Action of Gravity Field
Lower directly to be dripped from coalescence silk screen 13, air-flow goes successively to spiral case separative element 14, under the influence of centrifugal force, Partial Liquid Phase
Separated, the liquid phase isolated in first stage separation device 1 is discharged to discharge opeing common excretory duct 4；
2) through step 1) air-flow after treatment enters second-stage separation device 2, and air-flow passes through after flowing elder generation along eddy flow core pipe 21
The eddy flow mechanism 22 of a number of series connection is crossed, droplet is thrown to eddy flow core pipe under the influence of centrifugal force vane piece a is made
21 side walls, and discharge opeing sleeve pipe 23 is discharged to along the discharge opeing latasuture 211 in the side wall of eddy flow core pipe 21, the liquid phase for separating is through
One draining pipe 24 is discharged to discharge opeing common excretory duct 4；
3) through step 2) air-flow after treatment enters third level separator 3, and air-flow is along the coalescence flowing of core pipe 31 by catching
Mist silk screen 32, the liquid phase in air-flow encounter catch mist silk screen 32 after can constantly coalesce, droplet constantly gathers into big drop, big liquid
Drop is dripped under gravity, discharge opeing sleeve pipe 33 is discharged to then along discharge opeing latasuture 311, through the row of being pooled to of the second draining pipe 34
Liquid common excretory duct 4, the natural gas after being separated through three-level discharges transfer through the outlet of coalescence core pipe 31.
The present invention is only illustrated with above-described embodiment, and the structure of each part, set location and its connection all can be have
Changed.On the basis of technical solution of the present invention, all improvement carried out to individual part according to the principle of the invention or equivalent
Conversion, should not exclude outside protection scope of the present invention.
Claims (8)
1. one kind multistage natural gas gas-liquid separation device under water, it is characterised in that it includes be sequentially connected in series from the bottom to top first
Level separator, second-stage separation device and third level separator：
The first stage separation device includes horizontally disposed tank body, is arranged at the air flap near the tank body air inlet,
The spiral case separative element for being arranged at the coalescence silk screen at the air flap rear and being arranged at the tank body gas outlet；
The second-stage separation device includes the eddy flow core pipe being connected with the tank body gas outlet, is arranged in the eddy flow core pipe
Multiple eddy flow mechanisms in portion and the first discharge opeing sleeve pipe being set in outside the eddy flow core pipe；Positioned at eddy flow machine each described
The first discharge opeing latasuture is offered on the eddy flow core pipe bottom tube wall on rear side of structure；
The third level separator includes the coalescence core pipe being connected with eddy flow core pipe outlet, is arranged at the coalescence core pipe
It is internal to catch mist silk screen and be set in the second discharge opeing of outside sleeve pipe of the coalescence core pipe；In the lower tube of the coalescence core pipe
Also multiple second discharge opeing latasutures are opened up on wall.
2. multistage natural gas gas-liquid separation device under water as claimed in claim 1 a kind of, it is characterised in that：The tank body,
The bottom of one discharge opeing sleeve pipe and the second discharge opeing sleeve pipe is provided with draining pipe.
3. multistage natural gas gas-liquid separation device under water as claimed in claim 1 a kind of, it is characterised in that：The coalescence silk screen
It is arranged in the tank body upper inside walls at the air flap rear, and the coalesced filament net bottom end and the tank body bottom
Portion does not contact.
4. multistage natural gas gas-liquid separation device under water as claimed in claim 1 a kind of, it is characterised in that：Multiple eddy flows
Mechanism arranges in the inside of the eddy flow core pipe along the axis spaced series of the eddy flow core pipe.
5. a kind of multistage natural gas gas-liquid separation device under water as claimed in claim 1 or 2 or 3 or 4, it is characterised in that：
First stage separation device top multiple second-stage separation devices in parallel, each second-stage separation device correspondence is gone here and there
Third level separator described in connection one, sets in the porch of each second-stage separation device and each third level separator
Put control valve.
6. a kind of multistage natural gas gas-liquid separation device under water as described in claim 1 or 2 or 3, it is characterised in that：The tank
Body uses pressure container cylinder.
7. a kind of multistage natural gas gas-liquid separation device under water as described in claim 1 or 4, it is characterised in that：The eddy flow
Mechanism include deflection cone and along the deflection cone middle part of sliding channel circumferencial direction it is uniform make vane piece.
8. a kind of gas gas-liquid separating method of multistage natural under water based on claim 2 to 7 any one described device, including it is following
Step：
1) gas field natural gas containing liquid first passes around first stage separation device and carries out gas-liquid separation under water；Natural gas containing liquid enters tank
Body, the most of liquid containing liquid natural gas condenses into drop after inlet baffle is encountered and is separated under gravity, so
By coalescence silk screen, liquid in air-flow is agglomerated into big drop to air-flow in silk screen is coalesced afterwards, under gravity directly from poly-
Dripped on knot silk screen, air-flow goes successively to spiral case separative element, and under the influence of centrifugal force, Partial Liquid Phase is separated,
The liquid phase isolated in first stage separation device is discharged through draining pipe；
2) through step 1) air-flow after treatment enters second-stage separation device, and air-flow is along the flowing of eddy flow core pipe successively by a fixed number
The eddy flow mechanism of the series connection of amount, vane piece is made, droplet is thrown to eddy flow core pipe side wall under the influence of centrifugal force, and along
The first discharge opeing latasuture in the side wall of eddy flow core pipe is discharged to the first discharge opeing sleeve pipe, and the liquid phase for separating is discharged through draining pipe；
3) through step 2) air-flow after treatment enters third level separator, air-flow along coalescence core pipe flowing by catching mist silk screen,
Liquid phase in air-flow encounter catch mist silk screen after can constantly coalesce, droplet constantly gathers into big drop, and big drop is made in gravity
Dripped under, the second discharge opeing sleeve pipe is discharged to then along the second discharge opeing latasuture, the liquid phase for separating is discharged through draining pipe, warp
Natural gas after three-level is separated discharges transfer through the outlet of coalescence core pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710137273.4A CN106761657A (en) | 2017-03-09 | 2017-03-09 | A kind of multistage natural gas gas-liquid separation device and method under water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710137273.4A CN106761657A (en) | 2017-03-09 | 2017-03-09 | A kind of multistage natural gas gas-liquid separation device and method under water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106761657A true CN106761657A (en) | 2017-05-31 |
Family
ID=58961928
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710137273.4A Pending CN106761657A (en) | 2017-03-09 | 2017-03-09 | A kind of multistage natural gas gas-liquid separation device and method under water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106761657A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2515202A (en) * | 1944-11-06 | 1950-07-18 | Heyward J Dyer | Gas and liquid separator |
| CN202238348U (en) * | 2011-04-13 | 2012-05-30 | 中国石油大学(华东) | A multi-tubular cyclone separator for natural gas purification |
| CN102732296A (en) * | 2012-07-26 | 2012-10-17 | 中国海洋石油总公司 | High water-content crude oil electrostatic dehydration device |
| CN202610203U (en) * | 2011-12-21 | 2012-12-19 | 中国石油大学(华东) | Combined type rotational flow coalescer for offshore platform natural gas purification |
| CN203530264U (en) * | 2013-09-24 | 2014-04-09 | 中国石油大学(华东) | Three-level natural gas separator |
| CN206545504U (en) * | 2017-03-09 | 2017-10-10 | 中国海洋石油总公司 | A kind of multistage natural gas gas-liquid separation device under water |
-
2017
- 2017-03-09 CN CN201710137273.4A patent/CN106761657A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2515202A (en) * | 1944-11-06 | 1950-07-18 | Heyward J Dyer | Gas and liquid separator |
| CN202238348U (en) * | 2011-04-13 | 2012-05-30 | 中国石油大学(华东) | A multi-tubular cyclone separator for natural gas purification |
| CN202610203U (en) * | 2011-12-21 | 2012-12-19 | 中国石油大学(华东) | Combined type rotational flow coalescer for offshore platform natural gas purification |
| CN102732296A (en) * | 2012-07-26 | 2012-10-17 | 中国海洋石油总公司 | High water-content crude oil electrostatic dehydration device |
| CN203530264U (en) * | 2013-09-24 | 2014-04-09 | 中国石油大学(华东) | Three-level natural gas separator |
| CN206545504U (en) * | 2017-03-09 | 2017-10-10 | 中国海洋石油总公司 | A kind of multistage natural gas gas-liquid separation device under water |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103566698B (en) | Gas-liquid-solid three-phase separator | |
| CN104773789B (en) | A kind of compact three-phase separation method and device | |
| CN202610203U (en) | Combined type rotational flow coalescer for offshore platform natural gas purification | |
| CN209261766U (en) | A kind of reciprocating compressor entrance gas-liquid separation device | |
| CN117298659B (en) | A pipe-in-pipe gas-liquid pre-separation device for treating oilfield gas-containing produced liquid | |
| CN206545504U (en) | A kind of multistage natural gas gas-liquid separation device under water | |
| CA2558060A1 (en) | Method and separator for cyclonic separation of a fluid mixture | |
| CN106352622A (en) | Oil separator and refrigeration system using it | |
| CN206715497U (en) | A kind of underwater combined type natural gas gas-liquid separation device | |
| CN206996182U (en) | A kind of gas-liquid separator of replaceable separating mechanism | |
| CN106731248A (en) | A kind of combined type natural gas gas-liquid separation device and method under water | |
| CN207498328U (en) | A kind of shale gas special horizontal gas-liquid sand three phase separator | |
| CN102926734A (en) | Multi-stage high-efficiency rotational flow self-cleaning separator and application method thereof | |
| CN107162106B (en) | A separation device for oil-water separation of oily sewage | |
| CN205269228U (en) | Tubular oil gas water three -phase separator | |
| RU87100U1 (en) | GAS-LIQUID SEPARATOR | |
| CN101979118B (en) | Multi-branch oil-gas-liquid phase separator | |
| CN109432827B (en) | Weak cyclone type oil-gas-water three-phase separation device and flow dividing method | |
| CN118745886A (en) | Pipeline oil, gas and water separation device | |
| CN217431118U (en) | Skid-mounted wellhead gas-liquid separation device | |
| CN103397873B (en) | Natural gas field well head gas purifier | |
| CN201823342U (en) | Oil-gas-liquid three-phase separator of manifold | |
| CN213132295U (en) | Steam-water separation device with horizontally-opposite inlet and outlet | |
| CN102008867B (en) | Multi-branch pipe gas-liquid separator | |
| CN112943213A (en) | Gas-liquid separation device for three-phase 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 | ||
| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: 100010 Beijing, Chaoyangmen, North Street, No. 25, No. Applicant after: CHINA NATIONAL OFFSHORE OIL Corp. Applicant after: CNOOC RESEARCH INSTITUTE Co.,Ltd. Address before: 100010 Beijing, Chaoyangmen, North Street, No. 25, No. Applicant before: CHINA NATIONAL OFFSHORE OIL Corp. Applicant before: CNOOC Research Institute |
|
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170531 |