CN106338004A - Self-circulating gas-liquid mixed delivery supercharging device and method - Google Patents
Self-circulating gas-liquid mixed delivery supercharging device and method Download PDFInfo
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- CN106338004A CN106338004A CN201610876743.4A CN201610876743A CN106338004A CN 106338004 A CN106338004 A CN 106338004A CN 201610876743 A CN201610876743 A CN 201610876743A CN 106338004 A CN106338004 A CN 106338004A
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- 239000007788 liquid Substances 0.000 title claims abstract description 120
- 238000000034 method Methods 0.000 title claims abstract description 26
- 238000005406 washing Methods 0.000 claims abstract description 92
- 238000000926 separation method Methods 0.000 claims description 32
- 230000001737 promoting effect Effects 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000011084 recovery Methods 0.000 abstract description 4
- 230000010354 integration Effects 0.000 abstract description 3
- 238000001914 filtration Methods 0.000 description 12
- 239000012530 fluid Substances 0.000 description 9
- 230000008901 benefit Effects 0.000 description 6
- 230000005055 memory storage Effects 0.000 description 5
- 238000010276 construction Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- 238000005191 phase separation Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000007726 management method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 230000001914 calming effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D1/00—Pipe-line systems
- F17D1/005—Pipe-line systems for a two-phase gas-liquid flow
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
The invention relates to a gas-liquid mixed delivery supercharging device and method, in particular to a self-circulating gas-liquid mixed delivery supercharging device and method, and belongs to the technical field of gas-liquid mixed delivery supercharging. The device comprises a washing tank, a medium inlet of the washing tank is connected with a mixed delivery inlet A, a medium outlet of the washing tank is connected with a mixed delivery outlet B, a gas outlet of the washing tank is connected with a compressor, and an outlet of the compressor is connected with a gas inlet of the washing tank. The device and method can achieve gas-liquid mixed delivery. The device is high in integration level, good in stability, wide in application range, low in manufacturing cost, particularly suitable for gas-liquid mixed delivery and oil and gas recovery projects of an oil and gas field, and convenient to assemble on site and move.
Description
Technical field
The present invention relates to a kind of gas-liquid delivery pressurizer and method, belong to gas-liquid delivery supercharging technology field, specifically relate to
And a kind of circulating gas-liquid mixes defeated pressurizer and method.
Background technology
With the development in desert, the exploitation in marine oil gas field and oil-gas gathering and transportation supporting technology, oil gas water multi-phase mixed delivering skill
Art has obtained increasingly being widely applied.It is current oil by multi-product pipeline after the low pressure oil gas medium supercharging that well head is produced
Gas distance, the most effective approach of high efficiency transport, have great Social benefit and economic benefit.
Traditional well site mixed transportation process is as follows: first low pressure mixed with defeated medium and heats, then carry out gas-liquid separation again,
The liquid medium isolated is stored in fluid reservoir, enters mixed transporting tube net after output pump extracts supercharging；The gas isolated
Medium is pressurized by compressor after filtering again, and the high-pressure gas medium after supercharging enters gas line network, realizes gas-liquid
Mixed defeated.Wellsite facility is mainly made up of mechanical commprssor, heating furnace, separator, filter, fluid reservoir, output pump etc., equipment
More, complex process, fault is more, and is difficult into sled it is impossible to centralized Control, in-site installation trouble, and installation period is long, takes up an area face
Long-pending big, be not suitable for transition transport.In addition, mechanical compressor is very narrow to the area requirement of admission pressure, and mix defeated pressure medium model
Enclose too wide, pressure need to be depressured in the range of compressor permission, then be pressurized, energy loss is serious；Saturation water (liquid in gas
Body) compressor risen with destruction, compressor fault rate is high.
Also have a kind of well site mixed transportation process at present: first low pressure is mixed with defeated medium and carry out gas-liquid separation, the liquid isolated
In fluid reservoir, the gas medium isolated is pressurized after filtering media storage again by compressor, the height after supercharging
Pressure gas medium enters fluid reservoir again, liquid medium is released and enters mixed transporting tube net, realize gas-liquid delivery.Wellsite facility is mainly
Hydraulic compressor, separator, filter, fluid reservoir etc. form, and wellsite facility is less, and technique is simpler.Mixed defeated pressure medium is high
When, using hydraulic compressed machine, there is discharge capacity greatly, energy consumption is low, the low advantage of fault rate；But when well head, to mix defeated pressure medium relatively low
When, hydraulic compressor discharge capacity very low it is impossible to meet field working conditions demand, such as need to meet discharge capacity demand, then need increase equipment chi
Very little, improve plant capacity, equipment energy consumption is big, and manufacturing cost is very high, and Project in Operation benefit is low.Also has the height it is simply that after compression
When body of calming the anger pushes away the liquid in fluid reservoir, the separator of front end also in work, cannot discharge, if liquid by the big quantity of fluid that it produces
Amount is larger, then liquid easily diffuses out separator, enters in compressor, compressor is damaged.
For this reason, the designer of the present invention is in view of drawbacks described above, by concentrating on studies and designing, comprehensively it is engaged in for many years for a long time
The experience of related industry and achievement, research design goes out a kind of circulating gas-liquid and mixes defeated pressurizer and method, to overcome above-mentioned lacking
Fall into.
Content of the invention
The present invention is mainly the above-mentioned technical problem solving existing for prior art, there is provided a kind of circulating gas-liquid mixes defeated
Pressurizer and method.This device and method enables gas-liquid delivery, and device integrated level is high, and good stability is applied widely, system
Make low cost, be particularly well-suited to oil gas field gas-liquid delivery and petroleum vapor recovery project, and in-site installation and convenient removal.
The above-mentioned technical problem of the present invention is mainly addressed by following technical proposals:
A kind of circulating gas-liquid mixes defeated pressurizer, comprising: washing tank, and the medium input port of described washing tank is input into mixed
Mouth a is connected, and medium delivery outlet is connected with mixed delivery outlet b；The gas outlet of described washing tank is connected with compressor, described compressor
Delivery outlet connect washing tank the gas input port within device.
Optimize, a kind of above-mentioned circulating gas-liquid mixes defeated pressurizer, and described washing tank includes: the first washing tank (1),
Second washing tank (2)；Wherein:
Described first washing tank (1), the medium input port of the second washing tank (2) and mixed be input into a mouthful a and be connected, medium delivery outlet
It is connected with mixed delivery outlet b；
Described first washing tank (1), the gas outlet of the second washing tank (2) are connected with compressor (4), described compressor
(4) delivery outlet connects the first washing tank (1), the gas input port within device of the second washing tank (2).
Optimize, a kind of above-mentioned circulating gas-liquid mixes defeated pressurizer, the gas outlet of described washing tank passes through to filter
Device (3) is connected with compressor (4).
Optimize, a kind of above-mentioned circulating gas-liquid mixes defeated pressurizer, is provided with liquid level sensor in described washing tank.
Optimize, a kind of above-mentioned circulating gas-liquid mixes defeated pressurizer, is provided with wire mesh demister in described washing tank.
A kind of circulating gas-liquid mixes defeated boosting method, comprising:
Medium is inputted in washing tank and carries out gas-liquid separation, be re-entered into after the gas medium after separation is pressurizeed
Discharge with the liquid medium in washing tank after washing tank.
Optimize, a kind of above-mentioned circulating gas-liquid mixes defeated boosting method, comprising:
At least two washing tanks are in parallel, medium is inputted and carries out gas-liquid separation to one of washing tank, after separating
Gas medium pressurization after input to another washing tank with another washing tank liquid medium discharge；
When detect for the liquid level in the washing tank of gas-liquid separation exceeded when, medium is inputted in another washing tank
Row gas-liquid separation, and discharge inputting to the exceeded washing tank of liquid level after the gas medium pressurization after separation with liquid medium.
Optimize, a kind of above-mentioned circulating gas-liquid mixes defeated boosting method, comprising: after being filtered the gas after separation
Pressurizeed again.
Therefore, the present invention has the advantage that
1., using the mixed transportation process separating, filter, be pressurized, liquid medium is entered by the high-pressure gas medium after supercharging
Mixed delivery outlet, saves the equipment such as fluid reservoir, output pump, optimize technique, reduces fault, reducing energy consumption, reduces manufacturing cost, more
Energy-conserving and environment-protective；
2. gas-liquid separation part, gas filtration section, gas boosting part are integrated into sled, device integration is high, is easy to
Transport and unified management, save floor occupying area, and shorten the construction period, reducing the construction costs；
3. pair compressor no particular/special requirement, can mate adaptable according to the dissimilar mixed defeated medium in scene and operating mode
Type of compressor；
4. application range of products is wide, low to mixed defeated medium requirements, is particularly suited for oil gas field gas-liquid delivery and petroleum vapor recovery
Project；
5. liang set washing tank parallel operation, gas-liquid separation and gas-liquid discharge are individually carried out, and will not produce that liquid level is too high or liquid
Body medium is difficult to separate, and leads to equipment fault to shut down phenomenon, and more preferably, equipment safety stability can get more preferably gas-liquid separation effect
Ensure.
Brief description
Accompanying drawing 1 is a kind of schematic diagram of the present invention；
Specific embodiment
Below by embodiment, and combine accompanying drawing, technical scheme is described in further detail.
In figure, the first washing tank 1, the second washing tank 2, filter 3, compressor 4, the first check valve 11, the second check valve
12, the 3rd check valve 13, the 4th check valve 14, the first pneumatic ball valve 21, the second pneumatic ball valve 22, the 3rd pneumatic ball valve 23, the
Four pneumatic ball valves 24, the first relief valve 31, the second relief valve 32, the first liquid level sensor 41, the second liquid level sensor 42, first
Wire mesh demister 51, the second wire mesh demister 52, a mixes and is input into mouth, and b mixes delivery outlet.
Embodiment:
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation description is it is clear that described embodiment is only a part of embodiment of the present invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of not making creative work
Embodiment, broadly falls into the scope of protection of the invention.
Refer to Fig. 1, the present embodiment provides a kind of technical scheme: a kind of circulating gas-liquid mixes defeated pressurizer, including gas
Liquid separate section, gas filtration section, gas boosting part；Described gas-liquid separation part is arranged on gas filtration section front end simultaneously
Be communicated in mixed be input into a mouthful a, described gas-liquid separation is partly input into mouthful medium and carries out gas-liquid separation to mixed, and the gas medium isolated enters
Enter gas filtration section, the liquid medium isolated is stored in separator, described gas-liquid separation part is communicated in mixed delivery outlet
b；Described gas filtration section is arranged on gas-liquid separation portion rear end, and its entrance is connected to gas-liquid separation part, to separated
Gas medium is filtered；Described gas boosting part is arranged on gas filtration section rear end, and its entrance connects gas filtration portion
Point, to filter after gas medium be pressurized, its outlet connect gas-liquid separation part, intensified after high-pressure gas medium enter
Enter gas-liquid separation part, the liquid medium with storage enters mixed delivery outlet b.
Wherein, described gas-liquid separation part comprises the first washing tank 1 of parallel connection, the second washing tank 2, described first washing tank
Set liquid level sensor 41, the first wire mesh demister 51 on 1, described second washing tank 2 is provided with the second relief valve 32, the second liquid
Level sensor 42, the second wire mesh demister 52；
When described first washing tank 1, the second washing tank 2 superpressure, described first relief valve 31, the second relief valve 32 are opened automatically
Open, pipeline is carried out be vented release it is ensured that tank body safety；Described first liquid level sensor 41, the second liquid level sensor 42 detect
Described first washing tank 1, the liquid level of the second washing tank 2 memory storage liquid medium, when liquid medium level reaches the liquid level of setting
During high alarming value, control described first pneumatic ball valve 21, the second pneumatic ball valve 22, the 3rd pneumatic ball valve 23, the 4th pneumatic ball valve
24 keyings, described first washing tank 1, the second washing tank 2 automatic drain；Described 51,52 pairs of gas mediums of first wire mesh demister
In the drop that is mingled with carry out separating, reduce gas liquid content.
Described first washing tank 1, the second washing tank 2 parallel operation, wherein a set of described washing tank mixes defeated Jie for low pressure
Matter gas-liquid separation, another set of described washing tank mixes defeated medium automatic-discharging for high pressure, and its mode of operation can automatically switch.
It is provided with filter element in described accurate filter 3, the bulky grain thing in gas medium is filtered, remove gas and be situated between
Larger solid impurity in matter, ensures rear end equipment safety.
Described compressor 4 version no particular requirement, can be hydraulic piston type compressor or mechanical piston
Formula compressor or other compressor types, can be single stage compress or compound compressor.
Specifically, during use, described first pneumatic ball valve 21, the 4th pneumatic ball valve 24 automatically turn on, and described second is pneumatic
Ball valve 22, the 3rd pneumatic ball valve 23, it is automatically switched off, it is unidirectional by described first that the described mixed low pressure being input in mouthful a mixes defeated medium
Valve 11 enters described first washing tank 1 and carries out gas-liquid two-phase separation, and the liquid medium that described first washing tank 1 is isolated is stored in
Tank base, the gas medium that described first washing tank 1 is isolated passes through the liquid that described first wire mesh demister 51 removing is mingled with
Described accurate filter 3 is entered through described first pneumatic ball valve 21, described accurate filter 3 is situated between to the gas after separated after dripping
In matter, bulky grain thing is filtered, and enters described compressor 4, described compressor 4 is right after removing larger solid impurity in gas
Gas medium after separated filtration is pressurized, and the gas medium after supercharging is entered described by described 4th pneumatic ball valve 24
Second washing tank 2, the liquid medium of described second washing tank 2 memory storage is unidirectional by the described 4th with high-pressure gas medium
Valve 14 enters mixed delivery outlet b, completes a gas-liquid delivery process；
It is provided with the first liquid level sensor 41, when the liquid of described first washing tank 1 memory storage in described first washing tank 1
When medium reaches setting liquid level high high alarm setting value, described first pneumatic ball valve 21, the 4th pneumatic ball valve 24 are automatically switched off, described
Second pneumatic ball valve 22, the 3rd pneumatic ball valve 23, automatically turn on, the described mixed low pressure being input in mouthful a mixes defeated medium by described
3rd check valve 13 enters described second washing tank 2 and carries out gas-liquid two-phase separation, and the liquid that described second washing tank 2 is isolated is deposited
In tank base, the gas medium that described second washing tank 2 is isolated passes through described second wire mesh demister 52 removing and is mingled with for storage
Drop after enter described accurate filter 3 through described 3rd pneumatic ball valve 23, described accurate filter 3 is to the gas after separated
In body medium, bulky grain thing is filtered, and enters described compressor 4, described compressor after removing larger solid impurity in gas
Gas medium after 4 pairs of separated filtrations is pressurized, and the gas medium after supercharging is entered by described second pneumatic ball valve 22
Described first washing tank 1, the liquid medium of described first washing tank 1 memory storage passes through described second with high-pressure gas medium
Check valve 12 enters mixed delivery outlet b, completes a gas-liquid delivery process；
It is provided with the second liquid level sensor 42, when the liquid of described second washing tank 2 memory storage in described second washing tank 2
When medium reaches setting liquid level high high alarm setting value, described second pneumatic ball valve 22, the 3rd pneumatic ball valve 23, it is automatically switched off, institute
State the first pneumatic ball valve 21, the 4th pneumatic ball valve 24 automatically turns on, the described mixed low pressure being input in mouthful a mixes defeated medium by described
3rd check valve 13 enters described first washing tank 1 and carries out gas-liquid two-phase separation, and circulates work by the above.
As can be seen here, it is an advantage of the current invention that:
1., using the mixed transportation process separating, filter, be pressurized, liquid medium is entered by the high-pressure gas medium after supercharging
Mixed delivery outlet, saves the equipment such as fluid reservoir, output pump, optimize technique, reduces fault, reducing energy consumption, reduces manufacturing cost, more
Energy-conserving and environment-protective；
2. gas-liquid separation part, gas filtration section, gas boosting part are integrated into sled, device integration is high, is easy to
Transport and unified management, save floor occupying area, and shorten the construction period, reducing the construction costs；
3. pair compressor no particular/special requirement, can mate adaptable compressor according to the dissimilar mixed defeated medium in scene
Type；
4. application range of products is wide, low to mixed defeated medium requirements, is particularly suited for oil gas field gas-liquid delivery and petroleum vapor recovery
Project；
5. liang set washing tank parallel operation, gas-liquid separation and gas-liquid discharge are individually carried out, and will not produce that liquid level is too high or liquid
Body medium is difficult to separate, and leads to equipment fault to shut down phenomenon, and more preferably, equipment safety stability can get more preferably gas-liquid separation effect
Ensure.
Specific embodiment described herein is only explanation for example to present invention spirit.The affiliated technology of the present invention is led
The technical staff in domain can be made various modifications or supplement or replaced using similar mode to described specific embodiment
Generation, but the spirit without departing from the present invention or surmount scope defined in appended claims.
Although more employing the first washing tank 1 herein, the second washing tank 2, filter 3, compressor 4, first is unidirectional
Valve 11, the second check valve 12, the 3rd check valve 13, the 4th check valve 14, the first pneumatic ball valve 21, the second pneumatic ball valve 22, the
Three pneumatic ball valves 23, the 4th pneumatic ball valve 24, the first relief valve 31, the second relief valve 32, the first liquid level sensor 41, the second liquid
Level sensor 42, the first wire mesh demister 51, the second wire mesh demister 52, a mixes and is input into mouth, and b mixes the terms such as delivery outlet, but not
Exclusion is using the probability of other terms.It is used for the purpose of more easily describing and explaining the basis of the present invention using these terms
Matter；It is all contrary with spirit of the present invention for being construed as any additional restriction.
Claims (8)
1. a kind of circulating gas-liquid mixes defeated pressurizer it is characterised in that including: washing tank, the medium input of described washing tank
Mouthful it is input into a mouthful a and is connected with mixed, medium delivery outlet is connected with mixed delivery outlet b；Gas outlet within the device of described washing tank with
Compressor is connected, and the delivery outlet of described compressor connects the gas input port within device of washing tank.
2. a kind of circulating gas-liquid according to claim 1 mixes defeated pressurizer it is characterised in that described washing tank bag
Include: the first washing tank (1), the second washing tank (2)；Wherein:
Described first washing tank (1), the medium input port of the second washing tank (2) and mixed be input into a mouthful a and be connected, medium delivery outlet with mix
Delivery outlet b is connected；
Described first washing tank (1), the gas outlet of the second washing tank (2) are connected with compressor (4), described compressor (4)
Delivery outlet connects the first washing tank (1), the gas input port within device of the second washing tank (2).
3. a kind of circulating gas-liquid according to claim 1 mixes defeated pressurizer it is characterised in that the gas of described washing tank
Body outlet is connected with compressor (4) by filter (3).
4. a kind of circulating gas-liquid according to claim 1 mixes defeated pressurizer it is characterised in that setting in described washing tank
It is equipped with liquid level sensor.
5. a kind of circulating gas-liquid according to claim 1 mixes defeated pressurizer it is characterised in that setting in described washing tank
It is equipped with wire mesh demister.
6. a kind of circulating gas-liquid mixes defeated boosting method it is characterised in that including:
Medium is inputted in washing tank and carries out gas-liquid separation, after the gas medium after separation is pressurizeed, be re-entered into washing
Discharge with the liquid medium in washing tank after tank.
7. a kind of circulating gas-liquid according to claim 1 mixes defeated boosting method it is characterised in that including:
At least two washing tanks are in parallel, medium is inputted and carries out gas-liquid separation to one of washing tank, by the gas after separation
Input to another washing tank after the pressurization of body medium and discharge with the liquid medium in another washing tank；
When detect for the liquid level in the washing tank of gas-liquid separation exceeded when, medium is inputted in another washing tank and enters circulation of qi promoting
Liquid separates, and discharges inputting to the exceeded washing tank of liquid level after the gas medium pressurization after separation with liquid medium.
8. a kind of circulating gas-liquid according to claim 1 mixes defeated boosting method it is characterised in that by the gas after separation
Pressurizeed again after being filtered.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811323807.3A CN109488882B (en) | 2016-10-08 | 2016-10-08 | Gas-liquid mixed transportation supercharging device with wire mesh demister and method |
| CN201610876743.4A CN106338004B (en) | 2016-10-08 | 2016-10-08 | A kind of circulating gas-liquid mixes defeated supercharging device and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610876743.4A CN106338004B (en) | 2016-10-08 | 2016-10-08 | A kind of circulating gas-liquid mixes defeated supercharging device and method |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811323807.3A Division CN109488882B (en) | 2016-10-08 | 2016-10-08 | Gas-liquid mixed transportation supercharging device with wire mesh demister and method |
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| Publication Number | Publication Date |
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| CN106338004A true CN106338004A (en) | 2017-01-18 |
| CN106338004B CN106338004B (en) | 2019-01-22 |
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| CN201811323807.3A Active CN109488882B (en) | 2016-10-08 | 2016-10-08 | Gas-liquid mixed transportation supercharging device with wire mesh demister and method |
| CN201610876743.4A Active CN106338004B (en) | 2016-10-08 | 2016-10-08 | A kind of circulating gas-liquid mixes defeated supercharging device and method |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201811323807.3A Active CN109488882B (en) | 2016-10-08 | 2016-10-08 | Gas-liquid mixed transportation supercharging device with wire mesh demister and method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109812701A (en) * | 2019-03-25 | 2019-05-28 | 智马（北京）油气设备有限公司 | A kind of compression set and gas-liquid delivery method for realizing gas-liquid delivery system |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113550730B (en) * | 2021-09-18 | 2021-12-17 | 胜利油田胜机石油装备有限公司 | Multiphase metering mixed transportation system and multiphase metering mixed transportation method |
| CN116518303B (en) * | 2023-05-12 | 2024-06-07 | 延安众邦源实业有限公司 | Gas-dominant multiphase supercharging device and method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6354318B2 (en) * | 1998-08-28 | 2002-03-12 | Rosewood Equipment Company | System and method for handling multiphase flow |
| US20030010204A1 (en) * | 2000-01-17 | 2003-01-16 | Molyneux Peter David | Slugging control |
| US20120103188A1 (en) * | 2009-01-08 | 2012-05-03 | Aker Subesa As | Method and a device for liquid treatment when compressing a well flow |
| CN104500362A (en) * | 2014-09-15 | 2015-04-08 | 成都烃源科技有限责任公司 | Pressurization and mixed transportation process and device of gas field well station |
| CN105854420A (en) * | 2016-05-26 | 2016-08-17 | 成都正升能源技术开发有限公司 | Separator capable of achieving gas-liquid mixed delivery function |
| CN105864638A (en) * | 2016-05-26 | 2016-08-17 | 成都正升能源技术开发有限公司 | Compressor set capable of achieving gas-liquid mixed delivery function |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5290151A (en) * | 1988-10-28 | 1994-03-01 | Snamprogetti S.P.A. | Process for pumping a multi-phase gas-liquid mixture by means of the use of a pump |
| CN1161553C (en) * | 2002-11-14 | 2004-08-11 | 姚瑞忠 | Oil well gas-liquid mixed conveyor |
| CN102226499B (en) * | 2011-03-31 | 2013-03-20 | 中国海洋石油总公司 | Simulated deepwater oil-gas-water mixed transportation experimental device |
| CN202376885U (en) * | 2012-04-27 | 2012-08-15 | 沈阳鼓风机集团压力容器有限公司 | Gas-liquid mixing medium separator |
| CN104295269B (en) * | 2013-07-19 | 2017-02-08 | 中国石油天然气股份有限公司 | Integrated well group pressurization integrated device |
| CN104771938B (en) * | 2015-04-22 | 2016-06-08 | 武汉齐达康能源装备有限公司 | Gas-liquid delivery pressure charging system |
-
2016
- 2016-10-08 CN CN201811323807.3A patent/CN109488882B/en active Active
- 2016-10-08 CN CN201610876743.4A patent/CN106338004B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6354318B2 (en) * | 1998-08-28 | 2002-03-12 | Rosewood Equipment Company | System and method for handling multiphase flow |
| US20030010204A1 (en) * | 2000-01-17 | 2003-01-16 | Molyneux Peter David | Slugging control |
| US20120103188A1 (en) * | 2009-01-08 | 2012-05-03 | Aker Subesa As | Method and a device for liquid treatment when compressing a well flow |
| CN104500362A (en) * | 2014-09-15 | 2015-04-08 | 成都烃源科技有限责任公司 | Pressurization and mixed transportation process and device of gas field well station |
| CN105854420A (en) * | 2016-05-26 | 2016-08-17 | 成都正升能源技术开发有限公司 | Separator capable of achieving gas-liquid mixed delivery function |
| CN105864638A (en) * | 2016-05-26 | 2016-08-17 | 成都正升能源技术开发有限公司 | Compressor set capable of achieving gas-liquid mixed delivery function |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109812701A (en) * | 2019-03-25 | 2019-05-28 | 智马（北京）油气设备有限公司 | A kind of compression set and gas-liquid delivery method for realizing gas-liquid delivery system |
| CN109812701B (en) * | 2019-03-25 | 2024-01-23 | 智马（北京）油气设备有限公司 | Compression device for realizing gas-liquid mixed transportation system and gas-liquid mixed transportation method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109488882A (en) | 2019-03-19 |
| CN109488882B (en) | 2020-04-21 |
| CN106338004B (en) | 2019-01-22 |
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