CN107620588A - The more tube group type gas-liquid continuous separation devices of intelligence - Google Patents
The more tube group type gas-liquid continuous separation devices of intelligence Download PDFInfo
- Publication number
- CN107620588A CN107620588A CN201710839741.2A CN201710839741A CN107620588A CN 107620588 A CN107620588 A CN 107620588A CN 201710839741 A CN201710839741 A CN 201710839741A CN 107620588 A CN107620588 A CN 107620588A
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid
- unit
- separation
- outlet
- 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.)
- Withdrawn
Links
Landscapes
- Degasification And Air Bubble Elimination (AREA)
Abstract
The invention discloses a kind of gas-liquid continuous separation device of the more tube group types of intelligence, the present apparatus gas-liquid separation number of plies is more, separation group number is more, isolating construction is unique, the gas after separation is efficient, gas is pure and device itself uses with the multi-faceted detection unit such as temperature, pressure, liquid level, robot control system(RCS), the occasion higher available for gas phase demand after Oil-gas Separation（Such as：Internal combustion unit, heating furnace）, it may also be used for the air discharge of gas after separation（Such as：Carbon dioxide injection displacement of reservoir oil production operation, nitrogen injection displacement of reservoir oil production operation）After device can be directly installed on onsite application, do not limited by region location, device can also solve defeated individual well region, branch line collection, gas metering demand in multi-purpose station, fluid path metering requirements, the gas-liquid separation measuring requirement of individual well, branch line block is reached, improve provide high range than separating technology technology, device itself measurement accuracy is high, automatically controls that ability is strong, realizes the demand of current oil field development.
Description
Technical field
The present invention relates to individual well or the Oil-gas Separation metering field of multi-purpose station, and in particular to a kind of crude oil single well production process
Or the more tube group type gas-liquid continuous separation devices of intelligence of multi-purpose station gathering line.
Background technology
The Oil-gas Separation of process mainly still uses bedroom or vertical point in domestic individual well production or multi-purpose station gathering production
From device, both separators are mainly to realize that separation between liquid, gas and water, the gas-liquid control of rear end be main or mechanical thick stick
Bar or pressure title formula manual control mode, when running into the high oil-gas ratio in scene or slug operating mode, regulation, the production fortune of separator can be given
Row brings very big difficulty, and manual control relative frequency is high, and adjustment factor difficulty is big, and do not reach will for the separating effect of separator
Ask, or even cause separator not efficiently separate, the disturbance even situation of canful or gas circuit feed liquor occurs in liquid phase.Work as oil field region
When the scene a large amount of natural gases of needs need to use as source of the gas or when based on crude work production needs discharge, gas-liquid point is faced with
It is big from difficulty, floor space is wide, mechanical degreeization is low, when will scene it is hydraulic control linked when more difficult, isolating at the scene
When natural gas will enter internal combustion engine or Large-scale Heater or carry out air emptying, because requiring higher to natural gas, it is impossible to containing a large amount of
Crude oil condensed water, other debris, so wanting just use new-type separator or more using qualified natural gas
The separator of level, while consumption statistics carried out to the tolerance after separation and also lead to not carry out because being unable to reach metered condition
Clearing, it is badly in need of a kind of new crude oil production separate measurement technology to meet the production requirement of current Oil Field.
The content of the invention
It is an object of the invention to provide a kind of more tube group type gas-liquid continuous separation devices of intelligence, to overcome current crude monoglyceride
The separation that runs into of the crude oil vapor of well production process or multi-purpose station gathering line separation not thoroughly, separation operation difficulty is big, separation
The relevant issues such as automatic control level is low, not up to standard, the gas circuit measuring accuracy bottom of separation gas phase.
Concrete technical scheme of the present invention is：
A kind of more tube group type gas-liquid continuous separation devices of intelligence, including entrance end unit, a shunting zone unit, first separation layer
Unit, secondary separation layer unit, secondary separation pipe group unit, hydraulic control unit, gas circuit control coagulate unit, gas circuit meter unit,
Gas circuit outlet end unit, fluid path meter unit, fluid path outlet port unit and host computer unit；
The entrance end unit includes entrance pipe fitting and the instrument and valve installed thereon；The instrument includes temperature pick-up
Device and pressure transmitter, the valve include self-contained pressure regulator and safety valve；
Shunting zone unit includes vertical tube main body peace pipe isocon, and the entrance point of the bottom of the vertical tube main body is with entering
Mouth pipe fitting connection communicates；The flat pipe isocon is branched and equidistant parallel arrangement up and down, each flat pipe isocon
Entrance point is sequentially connected with the port of export of vertical tube body top and communicated；
The first separation layer unit includes the first gas-liquid amplifier tube, the first rotational flow generator and the second separation body, described
First gas-liquid amplifier tube is connected respectively for the port of export of branched and its entrance point and each flat pipe isocon, each branch institute
The first gas-liquid amplifier tube homocline is stated to tilt down and first separate body with what is be vertically arranged by the first rotational flow generator respectively
The entrance point connection on top communicates；
The secondary separation layer unit includes gas-liquid isocon, the second gas-liquid amplifier tube, the second rotational flow generator and second point
From body, the gas-liquid isocon is branched and equidistantly parallel arrangement, the entrance point of each gas-liquid isocon divide up and down
It is not sequentially connected and communicates with first port of export for separating body top；The second gas-liquid amplifier tube is branched and it enters
Mouth end and the port of export of each gas-liquid isocon are connected respectively；The port of export of each the second gas-liquid amplifier tube is equal
Tilt obliquely and phase is connected with the second entrance point for separating body top being vertically arranged by the second rotational flow generator respectively
It is logical；
The hydraulic control unit includes the liquid level monitoring device being arranged in the second separating pipe body；
The port of export connection that the gas circuit outlet end unit separates body top with described second communicates；The gas circuit port of export list
Member includes outlet gas line and the valve installed thereon, instrument；
The front end that unit is arranged on the outlet gas line is coagulated in the gas circuit control, and it includes gas circuit and catches mist component and pacify respectively
The pressure transmitter of mist component front and back ends is caught mounted in gas circuit；
The gas circuit meter unit includes the temperature transmitter at the front and rear middle part for being sequentially arranged at the outlet gas line
And gas meter；
The fluid path outlet port unit separates body with described first and the second port of export connection for separating body bottom communicates；Institute
Stating the fluid path outlet port unit includes liquid exit line and the pressure transmitter installed thereon.
The fluid path meter unit includes the liquid phase instrument being arranged in the middle part of the outlet gas line and is located at
Pressure transmitter, temperature transmitter before it.
The host computer unit includes plc data collecting unit and host computer computer, and the plc data collecting unit is used
In the meter information collection by each test point and data transfer, the host computer computer is used to receive plc data collecting unit
The data of transmission simultaneously carry out data processing.
Further, a shunting zone unit and first separation layer unit are the multigroup of mutual corresponding connection,
And it is multigroup between in the multiple rows of front and rear arrangement of run-in index form multistage side-by-side first separation pipe group unit.
Further, the secondary separation layer unit is forms between multigroup and multigroup in the multiple rows of front and rear arrangement of run-in index
Multistage side-by-side secondary separation pipe group unit.
Further, the gas-liquid continuous separation device also includes sampling emptying unit, and the sampling emptying unit includes
Sampling atmospheric valve installed in fluid path meter unit flow low side and/or outlet gas line top.
Further, the inclination angle of the first gas-liquid amplifier tube, the second gas-liquid amplifier tube and horizontal plane is 30 degree.
Further, the valve on gas circuit outlet end unit, instrument include being sequentially arranged at the gas outlet tube
The self-contained pressure regulator and pressure transmitter of the rear end of line.
Further, the liquid level monitoring device is flexible liquid level flowmeter sensor, and the flexible liquid level flowmeter sensor is with stretching
Contracting liquid level gauge transmitter connects；Electric control valve is connected with gas circuit outlet end unit；The flexible liquid level gauge passes
Sensor, both electric control valves pass through host computer unit coordinated signals.
Further, the gas meter selects vortex precession flowmeter.
Further, the liquid phase meter selection mass flowmenter.
Further, the electric control valve selects anti-explosion electric regulation ball valve.
Beneficial effects of the present invention：The gas-liquid continuous separation device of this novel intelligent multiple group type provided by the invention, it is real
Showed single-well crude oil production, gas-liquid mixed branch line collection is defeated, enter in multi-purpose station crude oil production gas liquid high-efficiency separation and continuous metering,
Solving the height in traditional separate measurement, manually intensity, high gas-liquid ratio, gas phase are separately separated, gas phase filtration, gas phase are measured, production
During real-time detection, in real time control and digitization information platform application, reached individual well production, gas-liquid mixed branch
The input that line collection is defeated, enters the automated production of multi-purpose station crude oil production, reduces manual resource and ground resource, after the separation of scene
Gas can directly enter internal combustion unit, heating furnace or directly emptying, and without carrying out the processing again of miscellaneous equipment, advantage improves oil well
The technology of the multinomial stream MIXED PHASE TRANSPORTATION IN of Produced Liquid, and metering method is simple, dependable performance, realizes national current energy-conservation and subtracts
Row, the demand of oil field dataization development.
Brief description of the drawings
Fig. 1 is the structural representation of the more tube group type gas-liquid continuous separation devices of intelligence；
In figure：Device portal pipe fitting 1, temperature transmitter 2, pressure transmitter 3, self-contained pressure regulator 4, safety valve 5, vertical tube
Main body 6, flat pipe isocon 7, gas-liquid amplifier tube 8, rotational flow generator 9, separation body 10, first separation pipe group 11, gas-liquid shunting
It is pipe 12, gas-liquid amplifier tube 13, rotational flow generator 14, outlet gas line 15, separation body 16, secondary separation pipe group 17, flexible
Liquid level gauge transmitter 18, flexible liquid level flowmeter sensor 20, anti-explosion electric regulation ball valve 25, pressure transmitter 19, gas circuit catch mist group
Part 21, pressure transmitter 22, temperature transmitter 23, gas meter 24, self-contained pressure regulator 26, pressure transmitter 27, gas circuit go out
Mouth pipe fitting 28, pressure transmitter 29, temperature transmitter 30, liquid phase instrument 31, sampling atmospheric valve 32, pressure transmitter 33, outlet
Pipe fitting 34.
Embodiment
Below in conjunction with accompanying drawing and specific embodiment, the present invention is described further.
Referring to Fig. 1, a kind of more tube group type gas-liquid continuous separation devices of intelligence, by entrance end unit, a shunting zone unit,
First separation layer unit, separating pipe group unit, secondary separation layer unit, secondary separation pipe group unit, hydraulic control unit, gas circuit control are coagulated
Unit, gas circuit meter unit, gas circuit outlet end unit, fluid path meter unit, emptying unit, fluid path outlet port unit,
Host computer unit collectively constitutes；Each unit is illustrated respectively below.
Entrance end unit by device portal pipe fitting 1, temperature transmitter 2, pressure transmitter 3, self-contained pressure regulator 4,
Safety valve 5 forms, wherein temperature transmitter 2, pressure transmitter 3, self-contained pressure regulator 4, safety valve 5 be sequentially arranged at into
On mouth pipe fitting 1.Entrance pipe fitting 1 is attached with profile flow, and scene carrys out liquid and enters device by entrance pipe fitting 1, passes through entrance
Pipe fitting 1, temperature transmitter 2, pressure transmitter perceive the temperature value and pressure value of entrance；Become suddenly when running into front pipeline pressure
During change, self-contained pressure regulator 4 can be balance pressure, reduce because pressure change makes the influence of twin installation；When device is because by mistake
Operation or rear end flow cause pipeline pressure rise for some reason, and safety valve 5 realizes pressure release power safeguard protection when reaching critical value.
Shunting zone unit is made up of vertical tube main body 6, flat pipe isocon 7.Wherein vertical tube main body 6 and the phase of entrance pipe fitting 1
Logical, flat pipe isocon 7 is connected with vertical tube main body 6 successively to be communicated, and flat pipe isocon 7 designs for horizontal configuration, can be according to current
Oil-gas ratio carries out the parallel equidistantly design of multiple-limb, and 3 layers are designed as in current figure；This mode structure design is unique, effective solution
The needs of certainly high oil-gas ratio or atm number shunting.
First separation layer unit is made up of gas-liquid amplifier tube 8, rotational flow generator 9, separation body 10, wherein each part is mutual
It is logical, it is connected with upper level unit and communicates, gas-liquid amplifier tube 8 mainly realizes that the internal duct for carrying out liquid after shunting is amplified suddenly, is
The gas-liquid separation of rear end reaches pre-separation, and gas-liquid amplifier tube 8 has 30 degree of inclination angle with horizontal plane, is the offer angle of departure of rear end
Degree；The liquid that comes of pre-separation is mainly carried out the change of flow direction property by rotational flow generator 9, is allowed to enter in separation body 10 along specific direction
Portion；Gas-liquid amplifier tube 8 and rotational flow generator 9 carry out intercommunication with flat pipe isocon 7, can carry out multiple field pre-separation design, effectively
For high oil-gas ratio, slug operating mode.Inside separation body 10 in the presence of centrifugal force, gravity and buoyancy, carry out liquid and formed
One turbination vortex field, the big liquid phase of density flow to separation body 10 bottom, the small gas phase edge of density along vertical tube wall
The center of whirlpool rises to the top of separation body 10；This mode structure design is unique, realizes that the single multilayer of air-liquid efficiently divides
From.
Separating pipe group unit is made up of first separation pipe group 11, wherein first separation pipe group 11 by a shunting zone unit,
First separation layer unit two parts, which form, it is put can carry out the multiple rows of front-end geometry design of run-in index, and quantity is according to current oil
Gas tolerance when to be separated is determined, is designed as 1 group in figure at present, and internal each part is connected with upper level unit to be communicated, this side
Formula structure design is unique, realizes that the first time multistage side-by-side of air-liquid efficiently separates.
Secondary separation layer unit is by 16 groups gas-liquid isocon 12, gas-liquid amplifier tube 13, rotational flow generator 14, separation of body
Into wherein each part and superordinate elements intercommunication, gas-liquid isocon 12 is mainly secondary pre- shunting operation；Gas-liquid amplifier tube 13 and water
Plane has 30 degree of inclination angle, is that the offer of rear end separates angle；Gas-liquid amplifier tube 13, rotational flow generator 14, separation body 16
Realize that function is identical with a gas liquid separating function, also equidistantly design, this mode structure are set overall alignment mode for layer separation
Meter is unique, realizes that the secondary multistage side-by-side of air-liquid efficiently separates.
Secondary separation pipe group unit is made up of secondary separation pipe group 17, and wherein secondary separation pipe group 17 is by device secondary separation
Layer unit, which forms, it is put can carry out the multiple rows of front-end geometry design of run-in index, and quantity is when to be separated according to current oil gas
Tolerance is determined, is designed as 1 group in figure at present, and internal each part is connected with upper level unit to be communicated, and this mode structure design is unique,
Realize that second of multistage side-by-side of air-liquid efficiently separates.
Hydraulic control unit by flexible liquid level gauge transmitter 18, flexible liquid level flowmeter sensor 20, anti-explosion electric regulation ball valve 25, on
Position machine unit composition.Wherein each component is communicated with upper level unit, and liquid level of stretching flowmeter sensor 20 is realized inside separation body 16
The real-time detection of liquid level, contracting liquid level gauge transmitter 18 is arranged on the top of separation body 16, by the signal of inside liquid level according to signal
Mode is transferred to plc data acquisition system, and host computer unit can carry out early warning according to the signal that contracting liquid level gauge transmitter 18 is sent
Prompt, transfinite after adjust the passage regulation shut-off of anti-explosion electric regulation ball valve 25, gas circuit is entered after preventing liquid level from transfiniting, after influenceing
The use of end equipment device.
Gas circuit control is solidifying, and unit catches mist component 21 by pressure transmitter 19, gas circuit, pressure transmitter 22 forms.Wherein, each group
Part is communicated with upper level unit, and pressure transmitter 19 is arranged on the front end that gas circuit catches mist component 21, and pressure transmitter 22 is arranged on
Gas circuit catches the rear end of mist component 21；Gas circuit catches the port of export that the one end of mist component 21 is arranged on pipeline center, the other end and gas circuit, main
The collecting for the condensed water being used in gas circuit, the filtering of other debris, realize the purification of separation gas；Pressure transmitter 19 and pressure
Power transmitter 22 is mainly used in controlling the front and rear pressure differential detection of solidifying unit, plays forewarning function.
Gas circuit meter unit is made up of temperature transmitter 23, gas meter 24.Wherein, each component and upper level unit phase
Logical, temperature transmitter 23 is arranged on before gas meter 24, predominantly detects temperature before table；Gas meter 24 is currently vortex precession flowmeter,
Also other type gas meters are chosen as, predominantly detect gas phase instantaneous delivery and integrated flux after separation.
Gas circuit exports end unit and is made up of self-contained pressure regulator 26, pressure transmitter 27, gas circuit outlet pipe fitting 28.Its
In, each component is communicated with upper level unit, and self-contained pressure regulator 26 is arranged on before gas circuit outlet pipe fitting 27, pressure inverting
Device 27 is arranged between the gentle way outlet pipe fitting 28 of self-contained pressure regulator 26；Pressure transmitter 27 is used to detect gas circuit outlet
Pressure, gas circuit outlet pipe fitting 28 are mainly realized to the connection between external pipeline.
Fluid path meter unit is made up of pressure transmitter 29, temperature transmitter 30, liquid phase instrument 31.Wherein, each group
Part is communicated with upper level unit, and pressure transmitter 29 and temperature transmitter 30 are arranged on before liquid phase instrument 31, for detecting liquid
Temperature and pressure before phase instrument；Liquid phase instrument 31 is currently mass flowmenter from instrument, is also chosen as other type instrument
Table, mainly for detection of the instantaneous delivery and integrated flux of liquid phase.
Sampling emptying unit is made up of sampling atmospheric valve 32.Wherein, sampling atmospheric valve 32 is arranged on fluid path measuring instrument list
Metaflow low side or gas phase pipeline top, current quantity are 1 group, multigroup can also be designed, and are mainly used in liquid phase sampling, gas phase takes
Sample and device are vented function when safeguarding.
Fluid path outlet port unit is made up of pressure transmitter 33, outlet pipe fitting 34.Wherein, each component and upper level unit phase
It is logical；Pressure transmitter 33 is used to detect fluid path outlet pressure, and fluid path outlet pipe fitting 34 is mainly realized to the connection between external pipeline.
Host computer unit is made up of host computer computer, plc data collecting unit, auxiliary line, and host computer computer is mainly real
Now each test point Data Position is shown, dynamic data are shown in real time, the prompting of formation, the early warning order of yield data form,
The prompting of fault alarm；Plc data collecting unit is mainly by the collection of the meter information of each test point and data transfer, boost line
Realize the connection between each test point, and the fixation of plc data collecting unit, and the externally connection between electric wire in road.
Apparatus of the present invention advantage：
1. because device have more than separating layer, separating pipe group, atm number, high gas-liquid ratio, the gas-liquid separation under slug operating mode can be achieved；
2. the resistance to interference performance of device is strong, when device front and back ends pressure changes, device is influenceed smaller；
3. liquid level measurement precision is high, system is strong.Because Sensors on Data Buoy is in separation inside, contacted with homogeneous media, can be in real time
The variation of liquid level is perceived, reliable liquid level data is provided to device；
4. the shut-off control accuracy of gas circuit is high.What it is because of selection is anti-explosion electric regulation ball valve, and inner section is realized high-precision, polygonal
The regulation shut-off of position, under the finger life control of host computer, the signal for receiving flexible liquid level gauge transmitter at any time carries out multi-angle, height
The Liquid level of automation；
5. because there is the solidifying unit of control, the gas phase of separation can more totally, more meet the use at scene；
6. range ability is wide, it is adapted to individual well, branch line, the liquid gas separate measurement in multi-purpose station, realizes multi-parameter（Liquid phase, gas phase,
Temperature, pressure）Realization measurement；
7. automaticity is high, without manual adjustment；
8. rational in infrastructure, floor space is small；Instrument measurement parameter can be analyzed and processed using computer, automatically generate liquid
Phase, gas phase, temperature, the experiment curv and production report of pressure, ensure to realize that oil field fine-grained management provides science；
9. device can realize data network teletransmission, it is easy to remote monitoring.
In summary, structure design of the present invention is unique, novel, and exemplified as above is only illustrating to the present invention
It is bright, the limitation to protection scope of the present invention is not formed, it is every to belong to the present invention with the same or analogous design of the present invention
Protection domain within.
Claims (10)
- A kind of 1. more tube group type gas-liquid continuous separation devices of intelligence, it is characterised in that：Including entrance end unit, a shunting zone list Unit, gas circuit are coagulated in member, first separation layer unit, secondary separation layer unit, secondary separation pipe group unit, hydraulic control unit, gas circuit control Meter unit, gas circuit outlet end unit, fluid path meter unit, fluid path outlet port unit and host computer unit；The entrance end unit includes entrance pipe fitting（1）And the instrument and valve installed thereon；The instrument includes temperature Transmitter（2）And pressure transmitter（3）, the valve includes self-contained pressure regulator（4）And safety valve（5）；Shunting zone unit includes vertical tube main body（6）Peaceful pipe isocon（7）, the vertical tube main body（6）Bottom Entrance point and entrance pipe fitting（1）Connection communicates；The flat pipe isocon（7）For it is branched and up and down equidistantly parallel arrangement, each The flat pipe isocon（7）Entrance point with vertical tube main body（6）The port of export on top, which is sequentially connected, to be communicated；The first separation layer unit includes the first gas-liquid amplifier tube（8）, the first rotational flow generator（9）And second separation body （10）, the first gas-liquid amplifier tube（8）For branched and its entrance point and each flat pipe isocon（7）The port of export difference Corresponding connection, each the first gas-liquid amplifier tube（8）Homocline tilts down and respectively by the first rotational flow generator（9）With erecting The the first separation body directly set（10）The entrance point connection on top communicates；The secondary separation layer unit includes gas-liquid isocon（12）, the second gas-liquid amplifier tube（13）, the second rotational flow generator （14）And second separation body（16）, the gas-liquid isocon（12）For it is branched and up and down equidistantly parallel arrangement, each branch institute State gas-liquid isocon（12）Entrance point separate body with described first respectively（10）The port of export on top, which is sequentially connected, to be communicated； The second gas-liquid amplifier tube（13）For branched and its entrance point and each gas-liquid isocon（12）The port of export it is right respectively It should connect；Each the second gas-liquid amplifier tube（13）Port of export homocline tilt down and respectively by the second rotational flow generator （14）Second with being vertically arranged separates body（16）The entrance point connection on top communicates；The hydraulic control unit includes being arranged on the second separation body（16）Interior liquid level monitoring device；Gas circuit outlet end unit separates body with described second（16）The port of export connection on top communicates；The gas circuit outlet End unit includes outlet gas line（15）And install thereon valve, instrument；The gas circuit control coagulates unit and is arranged on the outlet gas line（15）Front end, it includes gas circuit and catches mist component（21）With And it is separately mounted to gas circuit and catches mist component（21）The pressure transmitter of front and back ends；The gas circuit meter unit is sequentially arranged at the outlet gas line before and after including（15）Middle part temperature become Send device（23）And gas meter（24）；The fluid path outlet port unit separates body with described first（10）And second separation body（16）The port of export of bottom connects Connect and communicate；The fluid path outlet port unit includes liquid exit line and the pressure transmitter installed thereon（33）.The fluid path meter unit includes being arranged on the outlet gas line（15）The liquid phase instrument at middle part（31）And Pressure transmitter before it（29）, temperature transmitter（30）.The host computer unit includes plc data collecting unit and host computer computer, and the plc data collecting unit is used for will The meter information collection of each test point and data transfer, the host computer computer are used to receive the transmission of plc data collecting unit Data and carry out data processing.
- 2. the more tube group type gas-liquid continuous separation devices of intelligence according to claim 1, it is characterised in that：It is described once to shunt Area's unit and first separation layer unit are the multigroup of mutual corresponding connection, and it is multigroup between front and rear arranged in run-in index is multiple rows of And form multistage side-by-side first separation pipe group unit.
- 3. the more tube group type gas-liquid continuous separation devices of intelligence according to claim 1, it is characterised in that：The secondary separation Layer unit is forms multistage side-by-side secondary separation pipe group unit between multigroup and multigroup in the multiple rows of front and rear arrangement of run-in index.
- 4. the more tube group type gas-liquid continuous separation devices of intelligence according to claim 1, it is characterised in that：First gas-liquid Amplifier tube（8）, the second gas-liquid amplifier tube（13）Inclination angle with horizontal plane is 30 degree.
- 5. the more tube group type gas-liquid continuous separation devices of intelligence according to claim 1, it is characterised in that：The gas-liquid is continuous Separator also includes sampling emptying unit, and the sampling emptying unit includes being arranged on fluid path meter unit flow low side And/or outlet gas line（15）The sampling atmospheric valve on top（32）.
- 6. the more tube group type gas-liquid continuous separation devices of intelligence according to claim 1, it is characterised in that：The gas circuit outlet Valve, instrument on end unit include being sequentially arranged at the outlet gas line（15）Rear end self-contained pressure regulator （26）And pressure transmitter（27）.
- 7. the more tube group type gas-liquid continuous separation devices of intelligence according to claim 1, it is characterised in that：The liquid level monitoring Device is flexible liquid level flowmeter sensor（20）, the flexible liquid level flowmeter sensor（20）With flexible liquid level gauge transmitter（18）Even Connect；Electric control valve is connected with gas circuit outlet end unit；The flexible liquid level flowmeter sensor（20）, motorized adjustment Both valves pass through host computer unit coordinated signals.
- 8. the more tube group type gas-liquid continuous separation devices of intelligence according to claim 1, it is characterised in that：The gas meter（24） From vortex precession flowmeter.
- 9. the more tube group type gas-liquid continuous separation devices of intelligence according to claim 1, it is characterised in that：The liquid phase instrument （31）From mass flowmenter.
- 10. the more tube group type gas-liquid continuous separation devices of intelligence according to claim 1, it is characterised in that：The electric adjustable Section valve selects anti-explosion electric regulation ball valve（25）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710839741.2A CN107620588A (en) | 2017-09-18 | 2017-09-18 | The more tube group type gas-liquid continuous separation devices of intelligence |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710839741.2A CN107620588A (en) | 2017-09-18 | 2017-09-18 | The more tube group type gas-liquid continuous separation devices of intelligence |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107620588A true CN107620588A (en) | 2018-01-23 |
Family
ID=61089935
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710839741.2A Withdrawn CN107620588A (en) | 2017-09-18 | 2017-09-18 | The more tube group type gas-liquid continuous separation devices of intelligence |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107620588A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108295513A (en) * | 2018-02-13 | 2018-07-20 | 中国石油天然气集团公司 | Weak eddy flow viscous crude defoams separator |
| CN108979615A (en) * | 2018-07-27 | 2018-12-11 | 中国石油大学(北京) | Natural gas system is recycled in high pressure gas well completing test |
| CN112443310A (en) * | 2019-08-29 | 2021-03-05 | 中国石油天然气股份有限公司 | Gas-liquid separation device and consumption reduction method for gas-liquid separation device |
-
2017
- 2017-09-18 CN CN201710839741.2A patent/CN107620588A/en not_active Withdrawn
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108295513A (en) * | 2018-02-13 | 2018-07-20 | 中国石油天然气集团公司 | Weak eddy flow viscous crude defoams separator |
| CN108979615A (en) * | 2018-07-27 | 2018-12-11 | 中国石油大学(北京) | Natural gas system is recycled in high pressure gas well completing test |
| CN108979615B (en) * | 2018-07-27 | 2019-07-26 | 中国石油大学(北京) | Natural gas system is recycled in high pressure gas well completing test |
| CN112443310A (en) * | 2019-08-29 | 2021-03-05 | 中国石油天然气股份有限公司 | Gas-liquid separation device and consumption reduction method for gas-liquid separation device |
| CN112443310B (en) * | 2019-08-29 | 2023-05-26 | 中国石油天然气股份有限公司 | Gas-liquid separation device and consumption reduction method for gas-liquid separation device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107620588A (en) | The more tube group type gas-liquid continuous separation devices of intelligence | |
| CN101525995B (en) | Gas and liquid multiphase quantitative measuring device and method thereof | |
| CN104266702A (en) | Multiphase wet air flow and phase content online measurement method and device | |
| CN106989942B (en) | A kind of pipe cleaner performance and pigging measure of merit device and method | |
| CN109141562B (en) | Natural gas moisture measurement device and method based on in-pipe phase separation and phase separation | |
| HU202978B (en) | Device for metering yield of an oil well | |
| CN207212320U (en) | The more tube group type gas-liquid continuous separation devices of intelligence | |
| CN202140078U (en) | Skid-mounted single-well triphase separation metering device | |
| CN105692784B (en) | Intelligent gun barrel oil removing system and control method | |
| CN207598224U (en) | A kind of shale gas special horizontal gas-liquid sand three-phase separator measurement sled | |
| CN105626029B (en) | Viscous crude tubular type separates multiphase measurement device | |
| CN107816636B (en) | Supercharging device and supercharging method for oil well metering station | |
| CN102580354A (en) | Multi-layer composite T-shaped pipe separator and separation method for separating two-phase flow or multiphase flow | |
| CN205012986U (en) | Portable well head measurement calibration device | |
| CN207033431U (en) | A kind of three-phase metering mechanism | |
| CN206002428U (en) | Flue gas detecting system | |
| CN206292237U (en) | A kind of diesel production detecting device for moisture content | |
| CN106753519B (en) | System and method for improving crude oil dehydration efficiency of united station | |
| CN109282965A (en) | It is a kind of to collect the quick identification device of nocuousness flow pattern and method in defeated standpipe | |
| CN205876292U (en) | Automatic well metering device that selects of integration | |
| CN102410862B (en) | Detecting device and detecting method for detecting height of liquid in extraction tower | |
| CN207245698U (en) | A kind of multistage separating single well metering device | |
| CN210049883U (en) | Gas well three-phase flow metering sledge | |
| CN204785578U (en) | Well head metering device and oil well measurement system | |
| CN204738803U (en) | Big cluster well natural gas gas -liquid separation measurement blending transportation skid -mounted device |
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 | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20180123 |
|
| WW01 | Invention patent application withdrawn after publication |