CN204126626U - Automatic control of liquid vertical oil-gas separator - Google Patents
Automatic control of liquid vertical oil-gas separator Download PDFInfo
- Publication number
- CN204126626U CN204126626U CN201420583378.4U CN201420583378U CN204126626U CN 204126626 U CN204126626 U CN 204126626U CN 201420583378 U CN201420583378 U CN 201420583378U CN 204126626 U CN204126626 U CN 204126626U
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- tank body
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- pipe
- separated
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- Expired - Lifetime
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- 239000007788 liquid Substances 0.000 title claims abstract description 48
- 238000000926 separation method Methods 0.000 claims abstract description 55
- 230000008676 import Effects 0.000 claims abstract description 16
- 230000003628 erosive effect Effects 0.000 claims abstract description 10
- 239000011521 glass Substances 0.000 claims description 8
- 239000010865 sewage Substances 0.000 claims description 6
- 239000012530 fluid Substances 0.000 abstract description 15
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 238000000034 method Methods 0.000 abstract description 7
- 230000008569 process Effects 0.000 abstract description 7
- 230000007423 decrease Effects 0.000 abstract description 5
- 238000012795 verification Methods 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 67
- 239000003921 oil Substances 0.000 description 41
- 238000012360 testing method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000009194 climbing Effects 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
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- Supply Devices, Intensifiers, Converters, And Telemotors (AREA)
Abstract
The utility model relates to controllable level gas and oil separating plant technical field, it is a kind of automatic control of liquid vertical oil-gas separator, it comprises separation tank body, oil and gas import is had outside the middle part being separated tank body, the erosion control baffle plate corresponding with oil and gas import is had at separation tank body internal fixtion, separation tank body internal fixtion below erosion control baffle plate has in reverse V-shaped shunt umbrella plate, and the separation tank body below shunt umbrella plate is fixed with flowline.The utility model reasonable and compact in structure, easy to use, it is in the process of Oil-gas Separation, leveling device can control the liquid level being separated tank body inner fluid effectively, effectively prevents separation tank body inner fluid liquid level too high and roof fall accident occurs, ensure that the safety of production is carried out, carrying of the present utility model is convenient in the setting of skid-mounted device, decrease dismounting and the verification number of times of safety valve, reduce the spoilage of safety valve, ensure that carrying out in order of production.
Description
Technical field
the utility model relates to controllable level gas and oil separating plant technical field, is a kind of automatic control of liquid vertical oil-gas separator.
Background technology
oilfield oil testing Conventional upright gas and oil separating plant needs manual observation liquid level, and by the liquid level of manual switch Valve controlling Conventional upright gas and oil separating plant, thus, easily there is roof fall accident in Conventional upright gas and oil separating plant, be unfavorable for that the safety of producing is carried out, and Conventional upright gas and oil separating plant according to actual needs frequent roping carries out operation to different well sites, during each mobile Conventional upright gas and oil separating plant, need dismounting safety valve and verification safety valve, frequent dismounting and verification safety valve easily cause the damage of safety valve, adverse influence is caused to production, in addition, when adopting controllable level three phase separator to carry out Oil-gas Separation in oilfield oil testing operation process, because controllable level three phase separator needs import to purchase, and controllable level three phase separator is expensive, make cost of production higher.
Summary of the invention
the utility model provides a kind of automatic control of liquid vertical oil-gas separator, overcomes the deficiency of above-mentioned prior art, and it effectively can solve the uppity problem of liquid level that the existing gas and oil separating plant used in oil test operation process exists.
the technical solution of the utility model is realized by following measures: a kind of automatic control of liquid vertical oil-gas separator, comprise separation tank body, oil and gas import is had outside the middle part being separated tank body, the erosion control baffle plate corresponding with oil and gas import is had at separation tank body internal fixtion, separation tank body internal fixtion below erosion control baffle plate has in reverse V-shaped shunt umbrella plate, separation tank body below shunt umbrella plate is fixed with flowline, shunt umbrella plate be separated leveling device tank body being provided with and can controlling to be separated liquid level in tank body between flowline, leveling device and flowline are fixedly installed togather, separation tank body internal fixtion above oil and gas import has T.P panel assembly, separation tank body above T.P panel assembly there is gas outlet.
here is the further optimization and/or improvements to above-mentioned utility model technical scheme:
above-mentioned leveling device can be mechanical type float liquid level adjuster, and the ball float of mechanical type float liquid level adjuster is positioned at knockout drum body, and delivery valve and the flowline of mechanical type float liquid level adjuster are fixedly installed togather.
above-mentioned oil and gas import can be installed with Oil/Gas Pipe, escape pipe is installed with in gas outlet, sewage draining exit is had in the bottom being separated tank body, blow-off pipe is installed with between sewage draining exit and flowline, the first bypass pipe is installed with between Oil/Gas Pipe and escape pipe, the second bypass pipe is installed with between Oil/Gas Pipe and blow-off pipe, escape pipe is installed with detector tube, escape pipe is installed with safety dumping pipe, safety dumping pipe is installed with safety valve, at Oil/Gas Pipe, escape pipe, blow-off pipe, first bypass pipe, second bypass pipe and detector tube are all installed with switch valve.
above-mentioned T.P panel assembly can comprise overhead gage and lower baffle plate, lower baffle plate is positioned at the below of overhead gage, the right-hand member of overhead gage is fixed on and is separated in tank body, the left end of overhead gage has spacing with the left internal side being separated tank body, the left end of lower baffle plate is fixed on and is separated in tank body, and the right-hand member of lower baffle plate has spacing with the right inside side being separated tank body, and between overhead gage and lower baffle plate, interval is fixed with the separating plate of at least two, parallel before and after adjacent separating plate, separating plate is the separating plate in corrugation tabular.
above-mentioned separation tank body can be installed with the glass plate content gauge corresponding with leveling device, separation tank body is installed with pressure meter.
the outside of above-mentioned separation tank body can be fixed with skid-mounted device, skirt is fixed with at the lower outside being separated tank body, skid-mounted device comprises base and top frame, top frame is positioned at the top of base, skirt is fixedly mounted on base, between base and top frame, interval is fixed with the column being no less than two, first gripper shoe parallel with pushing up frame is all fixed with between two adjacent root posts, between top frame and the first gripper shoe, longitudinal separation is fixed with the riser being no less than two, second gripper shoe parallel with base is all fixed with between two adjacent root posts below the first gripper shoe, between base and the second gripper shoe, longitudinal separation is fixed with the riser being no less than two, the middle part of column be separated the fixed head being fixed with between tank body and being no less than, the upright hanger being no less than one is fixed with on the top of top frame, the parallel hanger vertical with upright hanger is fixed with in the outside of column, be fixed with between the first gripper shoe lower end and column top in skewed inclined board, be fixed with between base and column bottom in skewed declined board, Oil/Gas Pipe, flowline, escape pipe, blow-off pipe, first bypass pipe, second bypass pipe, safety dumping pipe and detector tube are all positioned at the inner side of column, the escape pipe corresponding with safety dumping pipe is fixed with support bar, the bottom of support bar is fixed on and is separated on tank body.
the utility model reasonable and compact in structure, easy to use, it is in the process of Oil-gas Separation, leveling device can control the liquid level being separated tank body inner fluid effectively, effectively prevents separation tank body inner fluid liquid level too high and roof fall accident occurs, ensure that the safety of production is carried out, carrying of the present utility model is convenient in the setting of skid-mounted device, decrease dismounting and the verification number of times of safety valve, reduce the spoilage of safety valve, ensure that carrying out in order of production.
Accompanying drawing explanation
accompanying drawing 1 is the main TV structure schematic diagram being separated tank body in the utility model most preferred embodiment.
accompanying drawing 2 is the process chart of the utility model most preferred embodiment.
accompanying drawing 3 is the main TV structure schematic diagram of the utility model most preferred embodiment.
coding in accompanying drawing is respectively: 1 for being separated tank body, 2 is erosion control baffle plate, 3 is shunt umbrella plate, 4 is flowline, 5 is mechanical type float liquid level adjuster, 6 is ball float, 7 is delivery valve, 8 is Oil/Gas Pipe, 9 is escape pipe, 10 is blow-off pipe, 11 is the first bypass pipe, 12 is the second bypass pipe, 13 is detector tube, 14 is safety dumping pipe, 15 is safety valve, 16 is switch valve, 17 is overhead gage, 18 is lower baffle plate, 19 is separating plate, 20 is glass plate content gauge, 21 is pressure meter, 22 is skirt, 23 is base, 24 is top frame, 25 is column, 26 is the first gripper shoe, 27 is riser, 28 is the second gripper shoe, 29 is fixed head, 30 is upright hanger, 31 is parallel hanger, 32 is inclined board, 33 is declined board, 34 is support bar.
Detailed description of the invention
the utility model by the restriction of following embodiment, can not determine concrete embodiment according to the technical solution of the utility model and actual conditions.
in the utility model, for convenience of description, the description of the relative position relation of each parts is all be described according to the Butut mode of Figure of description 1, as: the position relationship of forward and backward, upper and lower, left and right etc. determines according to the Butut direction of Figure of description 1.
below in conjunction with embodiment and accompanying drawing, the utility model is further described:
as shown in accompanying drawing 1 to 3, this automatic control of liquid vertical oil-gas separator comprises separation tank body 1, oil and gas import is had outside the middle part being separated tank body 1, the erosion control baffle plate 2 corresponding with oil and gas import is had at separation tank body 1 internal fixtion, separation tank body 1 internal fixtion below erosion control baffle plate 2 has in reverse V-shaped shunt umbrella plate 3, separation tank body 1 below shunt umbrella plate 3 is fixed with flowline 4, leveling device tank body 1 being provided with and can controlling to be separated liquid level in tank body 1 is separated between shunt umbrella plate 3 with flowline 4, leveling device and flowline 4 are fixedly installed togather, separation tank body 1 internal fixtion above oil and gas import has T.P panel assembly, separation tank body 1 above T.P panel assembly there is gas outlet.Oil gas is entered by oil and gas import and is separated in tank body 1, enter and be separated oil gas in tank body 1 and erosion control baffle plate 2 collides, due to oil, the flow direction of gas and flow velocity change suddenly and make oil, gas generation pre-separation, fluid after pre-separation falls in the separation tank body 1 below shunt umbrella plate 3 by the guide functions of shunt umbrella plate 3, gas (carrying part fluid) after pre-separation continues to rise, the gas risen carries out the separation again of oil gas by T.P panel assembly, gas after being again separated is discharged by gas outlet, the fluid obtained after being again separated can fall into the bottom be separated in tank body 1, in above process, leveling device can control the liquid level being separated tank body 1 inner fluid effectively, effectively prevent separation tank body 1 inner fluid liquid level too high and roof fall accident occurs, ensure that the safety of production is carried out.
according to actual needs, above-mentioned automatic control of liquid vertical oil-gas separator can be made further optimization and/or improvements:
as shown in accompanying drawing 1 to 3, leveling device is mechanical type float liquid level adjuster 5, and the ball float 6 of mechanical type float liquid level adjuster 5 is positioned at and is separated tank body 1, and delivery valve 7 and the flowline 4 of mechanical type float liquid level adjuster 5 are fixedly installed togather.Mechanical type float liquid level adjuster 5 is existing known technology, mechanical type float liquid level adjuster 5 comprises ball float 6, ball lever, delivery valve 7 and connecting rod, when the liquid level being separated tank body 1 inner fluid constantly rises, ball float 6 and ball lever rise along with the rising of the liquid level of fluid, when ball float 6 rises to certain position, the moving belt of ball lever is dynamically connected the motion of bar, the connecting rod of motion opens the valve of the delivery valve 7 corresponding with flowline 4, the fluid be separated in tank body 1 is made sequentially to be separated tank body 1 by flowline 4 with delivery valve 7 discharge, now, the decline being separated tank body 1 inner fluid liquid level drives ball float 6 and ball lever to move downward, thus cause connecting rod can close delivery valve 7 valve corresponding with flowline 4, effectively control the liquid level be separated in tank body 1.
as shown in accompanying drawing 1 to 3, oil and gas import is installed with Oil/Gas Pipe 8, escape pipe 9 is installed with in gas outlet, sewage draining exit is had in the bottom being separated tank body 1, blow-off pipe 10 is installed with between sewage draining exit and flowline 4, the first bypass pipe 11 is installed with between Oil/Gas Pipe 8 and escape pipe 9, the second bypass pipe 12 is installed with between Oil/Gas Pipe 8 and blow-off pipe 10, escape pipe 9 is installed with detector tube 13, escape pipe 9 is installed with safety dumping pipe 14, safety dumping pipe 14 is installed with safety valve 15, at Oil/Gas Pipe 8, escape pipe 9, blow-off pipe 10, first bypass pipe 11, second bypass pipe 12 and detector tube 13 are all installed with switch valve 16.When in the oil gas in Oil/Gas Pipe 8 without natural gas or tolerance few and do not need to enter be separated carry out Oil-gas Separation in tank body 1 time, oil gas can enter flowline 4 by the second bypass pipe 12; When in the oil gas in Oil/Gas Pipe 8 without liquid such as crude oil and do not need to enter be separated carry out Oil-gas Separation in tank body 1 time, oil gas can enter escape pipe 9 by the first bypass pipe 11; The parameter detecting each gas component in tracheae 9 is convenient in the setting of detector tube 13; When the pressure in escape pipe 9 occurs abnormal, safety valve 15 is opened, and the gas in escape pipe 9 can be discharged by safety dumping pipe 14.
as shown in accompanying drawing 1 to 3, T.P panel assembly comprises overhead gage 17 and lower baffle plate 18, lower baffle plate 18 is positioned at the below of overhead gage 17, the right-hand member of overhead gage 17 is fixed on and is separated in tank body 1, the left end of overhead gage 17 has spacing with the left internal side being separated tank body 1, the left end of lower baffle plate 18 is fixed on and is separated in tank body 1, the right-hand member of lower baffle plate 18 has spacing with the right inside side being separated tank body 1, between overhead gage 17 and lower baffle plate 18, interval is fixed with the separating plate 19 of at least two, parallel before and after adjacent separating plate 19, separating plate 19 is the separating plate 19 in corrugation tabular.T.P panel assembly is existing known technology.The gas rising to lower baffle plate 18 place arrives separating plate 19 place by the right-hand member of lower baffle plate 18 with the spacing of the right inside side being separated tank body 1, gas now enters the split tunnel formed between adjacent separating plate 19, gas collides with separating plate 19 in split tunnel, the fluid carried in gas is made to occur again to be separated with gas, and the fluid after being again separated flows down along separating plate 19 and finally falls into the bottom being separated tank body 1, when the gas motion after being again separated is to when being positioned at the left side of separating plate 19 of leftmost, gas enters with the spacing of the left internal side being separated tank body 1 upper end being separated tank body 1 by the left end of overhead gage 17, and then the gas be separated is discharged by gas outlet.
as shown in accompanying drawing 1 to 3, separation tank body 1 is installed with the glass plate content gauge 20 corresponding with leveling device, separation tank body 1 is installed with pressure meter 21.The setting of glass plate content gauge 20 is convenient to observe the liquid level be separated in tank body 1; The setting of pressure meter 21 can obtain the pressure condition be separated in tank body 1.
as shown in accompanying drawing 1 to 3, skid-mounted device is fixed with in the outside being separated tank body 1, skirt 22 is fixed with at the lower outside being separated tank body 1, skid-mounted device comprises base 23 and top frame 24, top frame 24 is positioned at the top of base 23, skirt 22 is fixedly mounted on base 23, between base 23 and top frame 24, interval is fixed with the column 25 being no less than two, first gripper shoe 26 parallel with pushing up frame 24 is all fixed with between two adjacent root posts 25, between top frame 24 and the first gripper shoe 26, longitudinal separation is fixed with the riser 27 being no less than two, second gripper shoe 28 parallel with base 23 is all fixed with between two adjacent root posts 25 below the first gripper shoe 26, between base 23 and the second gripper shoe 28, longitudinal separation is fixed with the riser 27 being no less than two, the middle part of column 25 be separated the fixed head 29 being fixed with between tank body 1 and being no less than, the upright hanger 30 being no less than one is fixed with on the top of top frame 24, the parallel hanger 31 vertical with upright hanger 30 is fixed with in the outside of column 25, be fixed with between the first gripper shoe 26 lower end and column 25 top in skewed inclined board 32, be fixed with between base 23 and column 25 bottom in skewed declined board 33, Oil/Gas Pipe 8, flowline 4, escape pipe 9, blow-off pipe 10, first bypass pipe 11, second bypass pipe 12, safety dumping pipe 14 and detector tube 13 are all positioned at the inner side of column 25, the escape pipe 9 corresponding with safety dumping pipe 14 is fixed with support bar 34, the bottom of support bar 34 is fixed on and is separated on tank body 1.The carrying being separated tank body 1 is convenient in the setting of skid-mounted device, decreases dismounting and the verification number of times of safety valve 15, reduces the spoilage of safety valve 15, ensure that carrying out in order of production; Upright hanger 30 arranges with parallel hanger 31 the carrying be convenient to further being separated tank body 1; The setting of fixed head 29 is convenient to staff and is stood on fixed head 29 and carry out operations; The setting of riser 27 is convenient to staff when the separation tank body 1 that fell is carried, and can be fixedly installed togather by parallel hanger 31, be convenient to carrying of the present utility model further by climbing riser 27 with hanging apparatus.The setting of support bar 34 can reduce the effect of jolting to safety dumping pipe 14 and safety valve 15 in handling process.
above technical characteristic constitutes most preferred embodiment of the present utility model, and it has stronger compliance and best implementation result, can increase and decrease non-essential technical characteristic according to actual needs, meet the demand of different situations.
Claims (10)
1. an automatic control of liquid vertical oil-gas separator, it is characterized in that comprising separation tank body, oil and gas import is had outside the middle part being separated tank body, the erosion control baffle plate corresponding with oil and gas import is had at separation tank body internal fixtion, separation tank body internal fixtion below erosion control baffle plate has in reverse V-shaped shunt umbrella plate, separation tank body below shunt umbrella plate is fixed with flowline, shunt umbrella plate be separated leveling device tank body being provided with and can controlling to be separated liquid level in tank body between flowline, leveling device and flowline are fixedly installed togather, separation tank body internal fixtion above oil and gas import has T.P panel assembly, separation tank body above T.P panel assembly there is gas outlet.
2. automatic control of liquid vertical oil-gas separator according to claim 1, it is characterized in that leveling device is mechanical type float liquid level adjuster, the ball float of mechanical type float liquid level adjuster is positioned at knockout drum body, and delivery valve and the flowline of mechanical type float liquid level adjuster are fixedly installed togather.
3. automatic control of liquid vertical oil-gas separator according to claim 1 and 2, it is characterized in that oil and gas import is installed with Oil/Gas Pipe, escape pipe is installed with in gas outlet, sewage draining exit is had in the bottom being separated tank body, blow-off pipe is installed with between sewage draining exit and flowline, the first bypass pipe is installed with between Oil/Gas Pipe and escape pipe, the second bypass pipe is installed with between Oil/Gas Pipe and blow-off pipe, escape pipe is installed with detector tube, escape pipe is installed with safety dumping pipe, safety dumping pipe is installed with safety valve, at Oil/Gas Pipe, escape pipe, blow-off pipe, first bypass pipe, second bypass pipe and detector tube are all installed with switch valve.
4. automatic control of liquid vertical oil-gas separator according to claim 1 and 2, it is characterized in that T.P panel assembly comprises overhead gage and lower baffle plate, lower baffle plate is positioned at the below of overhead gage, the right-hand member of overhead gage is fixed on and is separated in tank body, the left end of overhead gage has spacing with the left internal side being separated tank body, the left end of lower baffle plate is fixed on and is separated in tank body, the right-hand member of lower baffle plate has spacing with the right inside side being separated tank body, between overhead gage and lower baffle plate, interval is fixed with the separating plate of at least two, parallel before and after adjacent separating plate, separating plate is the separating plate in corrugation tabular.
5. automatic control of liquid vertical oil-gas separator according to claim 3, it is characterized in that T.P panel assembly comprises overhead gage and lower baffle plate, lower baffle plate is positioned at the below of overhead gage, the right-hand member of overhead gage is fixed on and is separated in tank body, the left end of overhead gage has spacing with the left internal side being separated tank body, the left end of lower baffle plate is fixed on and is separated in tank body, the right-hand member of lower baffle plate has spacing with the right inside side being separated tank body, between overhead gage and lower baffle plate, interval is fixed with the separating plate of at least two, parallel before and after adjacent separating plate, separating plate is the separating plate in corrugation tabular.
6. automatic control of liquid vertical oil-gas separator according to claim 1 and 2, is characterized in that separation tank body is installed with the glass plate content gauge corresponding with leveling device, separation tank body is installed with pressure meter.
7. automatic control of liquid vertical oil-gas separator according to claim 3, is characterized in that separation tank body is installed with the glass plate content gauge corresponding with leveling device, separation tank body is installed with pressure meter.
8. automatic control of liquid vertical oil-gas separator according to claim 4, is characterized in that separation tank body is installed with the glass plate content gauge corresponding with leveling device, separation tank body is installed with pressure meter.
9. automatic control of liquid vertical oil-gas separator according to claim 5, is characterized in that separation tank body is installed with the glass plate content gauge corresponding with leveling device, separation tank body is installed with pressure meter.
10. automatic control of liquid vertical oil-gas separator according to claim 9, it is characterized in that the outside being separated tank body is fixed with skid-mounted device, skirt is fixed with at the lower outside being separated tank body, skid-mounted device comprises base and top frame, top frame is positioned at the top of base, skirt is fixedly mounted on base, between base and top frame, interval is fixed with the column being no less than two, first gripper shoe parallel with pushing up frame is all fixed with between two adjacent root posts, between top frame and the first gripper shoe, longitudinal separation is fixed with the riser being no less than two, second gripper shoe parallel with base is all fixed with between two adjacent root posts below the first gripper shoe, between base and the second gripper shoe, longitudinal separation is fixed with the riser being no less than two, the middle part of column be separated the fixed head being fixed with between tank body and being no less than, the upright hanger being no less than one is fixed with on the top of top frame, the parallel hanger vertical with upright hanger is fixed with in the outside of column, be fixed with between the first gripper shoe lower end and column top in skewed inclined board, be fixed with between base and column bottom in skewed declined board, Oil/Gas Pipe, flowline, escape pipe, blow-off pipe, first bypass pipe, second bypass pipe, safety dumping pipe and detector tube are all positioned at the inner side of column, the escape pipe corresponding with safety dumping pipe is fixed with support bar, the bottom of support bar is fixed on and is separated on tank body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420583378.4U CN204126626U (en) | 2014-10-10 | 2014-10-10 | Automatic control of liquid vertical oil-gas separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420583378.4U CN204126626U (en) | 2014-10-10 | 2014-10-10 | Automatic control of liquid vertical oil-gas separator |
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| Publication Number | Publication Date |
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| CN204126626U true CN204126626U (en) | 2015-01-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420583378.4U Expired - Lifetime CN204126626U (en) | 2014-10-10 | 2014-10-10 | Automatic control of liquid vertical oil-gas separator |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107152269A (en) * | 2017-07-03 | 2017-09-12 | 新疆熙泰石油装备有限公司 | Independent external liquid level regulation device and the gs-oil separator of external liquid level regulation |
| CN107991152A (en) * | 2017-11-23 | 2018-05-04 | 四川速荣科技有限公司 | A kind of gas and oil separating plant for moisture content static measurement instrument |
| CN110856781A (en) * | 2018-08-26 | 2020-03-03 | 江苏中远环保科技有限公司 | Vertical oil-gas separation device |
-
2014
- 2014-10-10 CN CN201420583378.4U patent/CN204126626U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107152269A (en) * | 2017-07-03 | 2017-09-12 | 新疆熙泰石油装备有限公司 | Independent external liquid level regulation device and the gs-oil separator of external liquid level regulation |
| CN107991152A (en) * | 2017-11-23 | 2018-05-04 | 四川速荣科技有限公司 | A kind of gas and oil separating plant for moisture content static measurement instrument |
| CN110856781A (en) * | 2018-08-26 | 2020-03-03 | 江苏中远环保科技有限公司 | Vertical oil-gas separation device |
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