CN211677001U - Oil gas treatment system - Google Patents
Oil gas treatment system Download PDFInfo
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- CN211677001U CN211677001U CN201922324734.6U CN201922324734U CN211677001U CN 211677001 U CN211677001 U CN 211677001U CN 201922324734 U CN201922324734 U CN 201922324734U CN 211677001 U CN211677001 U CN 211677001U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/30—Use of alternative fuels, e.g. biofuels
Abstract
The embodiment of the invention provides an oil and gas treatment system. The oil gas treatment system comprises a condensing device, a condensing device and a control device, wherein the condensing device is used for condensing oil gas to be treated so as to obtain liquid organic matters and non-condensable gas; and the gas generator is connected with the condensing device to obtain the non-condensable gas for combustion power generation, wherein the electric energy generated by the gas generator is used for providing a low-temperature environment for the condensing device. According to the oil-gas treatment system provided by the embodiment of the invention, the oil-gas treatment can be conveniently and quickly realized.
Description
Technical Field
The invention relates to the technical field of oil-gas treatment, in particular to an oil-gas treatment system.
Background
Petroleum and its products are mixtures of various hydrocarbons in which the light hydrocarbon components are highly volatile. In the processes of oil product production, transportation and sale, a part of light liquid components are inevitably vaporized and mixed into the atmosphere to form oil gas. The dissipation of oil gas not only can generate huge resource waste, but also can cause huge environmental pollution.
The existing oil gas treatment methods comprise an adsorption method, a condensation method, a membrane separation method and the like, and corresponding treatment equipment is often complex and has harsh use conditions.
Therefore, it is desirable to have a new oil and gas treatment device that can flexibly and conveniently perform oil and gas treatment.
Disclosure of Invention
In view of the above problems, an object of the present invention is to provide an oil and gas treatment system, so as to conveniently and rapidly perform oil and gas treatment.
According to an aspect of the invention, there is provided an oil and gas treatment system comprising: the condensing device is used for condensing the oil gas to be treated to obtain liquid organic matters and non-condensable gas; and the gas generator is connected with the condensing device to obtain the non-condensable gas for combustion power generation, wherein the electric energy generated by the gas generator is used for providing a low-temperature environment for the condensing device.
Preferably, the oil and gas treatment system further comprises: and the pressurizing device is connected with the condensing device and used for pressurizing oil gas to obtain the oil gas to be treated and providing the oil gas to be treated for the condensing device, wherein the electric energy generated by the gas generator is used for driving the pressurizing device.
Preferably, the oil and gas treatment system further comprises: and the heat exchange device is connected with the gas inlet end of the condensing device to provide the oil gas to be treated for the condensing device, and is connected with the gas outlet end of the condensing device to receive the non-condensable gas, wherein the oil gas to be treated is used as a hot fluid, and the non-condensable gas is used as a cold fluid to perform heat exchange in the heat exchange device.
Preferably, the oil and gas treatment system further comprises: and the pressure equalizing device is connected with the condensing device to receive the non-condensable gas and is used for adjusting the air pressure of the non-condensable gas.
Preferably, the oil and gas treatment system further comprises: and the liquid storage tank is connected with the condensing device to receive the liquid organic matters, wherein the liquid storage tank is connected with the pressure equalizing device, and gas generated in the liquid storage tank is conveyed to the pressure equalizing device.
Preferably, the condensing device is connected with the gas generator through a pipeline to provide the non-condensable gas for the gas generator; the oil and gas treatment system further comprises: the gas storage tank is used for storing combustible gas and is connected with the pipeline to provide the combustible gas into the pipeline, wherein the non-condensable gas and the combustible gas are mixed and then are conveyed into the gas generator.
Preferably, the oil and gas treatment system further comprises: and the refrigerating device is connected with the condensing device and used for providing a low-temperature environment for the condensing device, wherein the electric energy generated by the gas generator is used for driving the refrigerating device to refrigerate.
Preferably, the refrigerating apparatus comprises: a refrigeration compressor connected to the condensing device to receive a refrigerant and pressurize the refrigerant; the liquid separator is connected with the refrigeration compressor to receive the pressurized refrigerant and separate the liquid of the pressurized refrigerant; the air cooler is connected with the liquid separator to receive the refrigerant after liquid separation and cool the refrigerant after liquid separation; the gas generator is respectively connected with the refrigeration compressor and the air cooler and used for driving the refrigeration compressor and the air cooler.
Preferably, the oil and gas treatment system is mounted on a mobile platform to form a skid-mounted device.
According to the oil gas treatment system provided by the embodiment of the invention, oil gas to be treated is treated in a mode of combining the condensing device and the gas generator; the condensed noncondensable gas is used as the fuel of the gas generator, and the electric energy generated by the gas generator is used for the condensing device, so that the oil gas treatment with low power consumption and high efficiency can be realized.
According to the oil gas treatment system provided by the embodiment of the invention, a treatment method combining condensation and combustion is adopted, the treatment effect is good, and the higher emission requirement can be met.
According to the oil gas treatment system provided by the embodiment of the invention, the skid-mounted mode is adopted to install on the mobile equipment, the non-condensable gas is used for generating electricity to provide the electric power required by operation for the whole system, any external public engineering condition is not required, and the treatment requirements under different environments can be met.
Drawings
The above and other objects, features and advantages of the present invention will become more apparent from the following description of the embodiments of the present invention with reference to the accompanying drawings, in which:
FIG. 1 shows a device schematic of an oil and gas treatment system according to a first embodiment of the present invention;
FIG. 2 shows a device schematic of an oil and gas treatment system according to a second embodiment of the present invention;
FIG. 3 shows a device schematic of an oil and gas treatment system according to a third embodiment of the present invention;
FIG. 4 shows a device schematic of an oil and gas treatment system according to a fourth embodiment of the present invention;
FIG. 5 shows a device schematic of an oil and gas treatment system according to a fifth embodiment of the present invention;
figure 6 shows a device schematic of an oil and gas treatment system according to a sixth embodiment of the invention.
Detailed Description
Various embodiments of the present invention will be described in more detail below with reference to the accompanying drawings. Like elements in the various figures are denoted by the same or similar reference numerals. For purposes of clarity, the various features in the drawings are not necessarily drawn to scale. Moreover, certain well-known elements may not be shown in the figures.
The following detailed description of embodiments of the present invention is provided in connection with the accompanying drawings and examples. In the following description, numerous specific details of the invention, such as structure, materials, dimensions, processing techniques and techniques of components, are set forth in order to provide a more thorough understanding of the invention. However, as will be understood by those skilled in the art, the present invention may be practiced without these specific details.
It will be understood that when a layer, region or layer is referred to as being "on" or "over" another layer, region or layer in describing the structure of the component, it can be directly on the other layer, region or layer or intervening layers or regions may also be present. Also, if the component is turned over, one layer or region may be "under" or "beneath" another layer or region.
Figure 1 shows a device schematic of an oil and gas treatment system according to a first embodiment of the invention. As shown in fig. 1, the oil and gas treatment system according to the first embodiment of the present invention includes a condensing device 101, a refrigerating device 102, and a gas generator 201.
Volatile organic compounds (VCOS), such as oil and gas, to be treated are first fed into a condensing unit 101 for condensation. The VOCS gas is condensed in the condensing unit 101 to obtain liquid organic matter and non-condensable gas, respectively. The condensing unit 101 is connected to a gas generator 201. The condensed noncondensable gas is led out from the condensing unit 101 and is output to the gas generator 201. The liquid organic matter obtained by condensation is led out from the condensing unit 101 and recovered.
In an alternative embodiment of the present invention, the oil and gas treatment system further comprises a reservoir. The liquid storage tank is connected with the condensing device 101 and is used for recovering liquid organic matters obtained after condensation.
The condensing means 101 is also connected to a refrigerating means 102. The refrigeration device 102 is used to provide a low temperature environment for the condensation device 101. Optionally, the refrigeration device 102 is a mechanical refrigeration apparatus.
The non-condensable gases delivered by the condensing unit 101 serve as energy source for the gas generator 201. The gas generator 201 is, for example, a gas generator. The non-condensable gas delivered by the condensing unit 101 is used as fuel for the gas generator. The gas generator generates electricity by burning, and converts the internal energy of the non-condensable gas into electric energy.
In an alternative embodiment of the invention, the gas generator 201 is a reciprocating piston engine generator set. The non-condensable gas delivered by the condensing device 101 is used as fuel of the piston type internal combustion engine generator set. The piston type internal combustion engine mixes fuel (non-condensable gas) and air, and the mixture is combusted in a cylinder of the piston type internal combustion engine, and the released heat energy enables the cylinder to generate high-temperature and high-pressure gas. The gas expands to push the piston to do work, and then the mechanical work is output through a crank-link mechanism or other mechanisms to drive the generator to generate electricity.
The gas generator 201 is also connected to the cooling device 102. A part of the electric power generated by the gas generator 201 is supplied to the refrigerating apparatus 102 to be used as a driving power source of the refrigerating apparatus 102. The electric power generated by the gas generator 201 is also supplied to other devices.
Figure 2 shows a device schematic of an oil and gas treatment system according to a second embodiment of the invention. As shown in fig. 2, the oil and gas treatment system according to the second embodiment of the present invention includes a pressurizing device 301, a condensing device 101, a refrigerating device 102, and a gas generator 201.
Volatile organic compounds (VCOS), such as oil and gas, to be treated are first fed into a pressurizing device 301 for pressurization. The VCOS gas is pressurized in the pressurizing device 301 to obtain a high-pressure VOCS gas. The pressurizing device 301 is connected to the condensing device 101, and the high-pressure VOCS gas is sent to the condensing device 101 to be condensed.
The high-pressure VOCS gas is condensed in the condensing unit 101 to obtain liquid organic matter and non-condensable gas, respectively. The condensing unit 101 is connected to a gas generator 201. The condensed noncondensable gas is led out from the condensing unit 101 and is output to the gas generator 201. The liquid organic matter obtained by condensation is led out from the condensing unit 101 and recovered.
The condensing means 101 is also connected to a refrigerating means 102. The refrigeration device 102 is used to provide a low temperature environment for the condensation device 101.
The non-condensable gases delivered by the condensing unit 101 serve as energy source for the gas generator 201. Optionally, the gas generator 201 is a gas generator. The non-condensable gas delivered by the condensing unit 101 is used as fuel for the gas generator. The gas generator generates electricity by burning, and converts the internal energy of the non-condensable gas into electric energy.
The gas generator 201 is also connected to the cooling device 102. A part of the electric power generated by the gas generator 201 is supplied to the refrigerating apparatus 102 to be used as a driving power source of the refrigerating apparatus 102. Another part of the electric power generated by the gas generator 201 is supplied to the pressurizing device 301, and is used as a driving power source of the pressurizing device 301. The electric power generated by the gas generator 201 is also supplied to other devices.
In an alternative embodiment of the invention, the pressurizing means 301 comprises a claw compressor. The claw type compressor is a driven fluid machine which uses the rotation of two claw-shaped rotors meshed with each other to generate volume change so as to realize pressurization of low-pressure gas into high-pressure gas. The gas generator 201 is connected with the claw type compressor and used for driving the claw type compressor to work.
In the above embodiments, the oil and gas treatment system comprises a pressurizing device. The oil gas to be treated is condensed after being pressurized, so that the condensation efficiency is higher and the condensation effect is better; and the pressurizing device is driven by the electric power provided by the non-condensable gas combustion, so that additional energy is not needed, and the low power consumption of the whole system is ensured.
Figure 3 shows a device schematic of an oil and gas treatment system according to a third embodiment of the invention. As shown in fig. 3, the oil and gas treatment system according to the third embodiment of the present invention includes a heat exchanging device 401, a condensing device 101, and a gas generator 201.
Volatile organic compounds (VCOS), such as oil and gas, to be treated are introduced into the heat exchanger 401 for heat exchange. The VOCS gas exchanges heat in the heat exchange device 401 as a hot fluid to perform preliminary cooling. The VOCS gas after heat exchange enters a condensing device 101 for condensation treatment.
The heat-exchanged VOCS gas is condensed in the condensing device 101, and liquid organic matters and non-condensable gas are obtained after condensation. The condensed noncondensable gas is sent to the heat exchanger 401, and exchanges heat with the VCOS gas as the hot fluid in the heat exchanger 401 as the cold fluid.
The heat exchanging device 401 is also connected with the gas generator 201. The non-condensable gas after heat exchange is conveyed to the gas generator 201 by the heat exchange device 401. The non-condensable gas after heat exchange is used as energy source for the gas generator 201.
In an alternative embodiment of the invention, the condensing means 101 is connected to a heat exchanging means 401. The liquid organic matter obtained after condensation is led out from the condensing device 101 and exchanges heat with the VCOS gas as the hot fluid in the heat exchanging device 401 as the cold fluid. And recovering the liquid organic matters after heat exchange.
In the above embodiment, the oil and gas treatment system comprises a heat exchange device. The heat exchange device exchanges heat between the hot fluid entering the condensing device and the cold fluid flowing out of the condensing device, so that the temperature of the oil gas to be treated entering the condensing device is reduced, and the condensing efficiency is improved; on the other hand, the temperature of the non-condensable gas entering the gas generator is increased, and the stable operation of the gas generator is ensured.
Figure 4 shows a device schematic of an oil and gas treatment system according to a fourth embodiment of the invention. As shown in fig. 4, the oil and gas treatment system according to the fourth embodiment of the present invention includes a condensing unit 101, a pressure equalizing unit 501, and a gas generator 201.
Volatile organic compounds (VCOS), such as oil and gas, to be treated are first fed into a condensing unit 101 for condensation. The VOCS gas is condensed in the condensing unit 101 to obtain liquid organic matter and non-condensable gas, respectively. The liquid organic matter obtained by condensation is led out from the condensing unit 101 and recovered. The non-condensable gas obtained by condensation is led out from the condensing unit 101 and sent to the pressure equalizing unit 501.
The pressure equalizing device 501 adjusts the pressure of the non-condensable gas input thereto to obtain the non-condensable gas having an appropriate pressure value.
In an alternative embodiment of the present invention, the pressure equalizing device 501 is further connected to an air storage tank. The gas storage tank is used for storing gas fuel. The gas tank is used for supplying gas fuel to the pressure equalizing device 501. The gas fuel provided by the gas storage tank is mixed with the non-condensable gas. The mixed gas is sent to the gas generator 201. Optionally, the gas storage tank is a Liquefied Petroleum Gas (LPG) storage tank.
The gas generator 201 receives the non-condensable gas or the mixture of the non-condensable gas and the gas fuel which is transmitted by the pressure equalizing device 501 as energy.
In an alternative embodiment of the present invention, the reservoir is connected to a pressure equalization device 501. The organic gas (e.g., the generated respiratory gas) in the liquid storage tank is delivered to the pressure equalizing device 501. Optionally, the pressure equalization device 501 is connected to the upper portion of the storage tank by piping. The pipeline is provided with a safety valve. When the air pressure in the liquid storage tank is greater than the threshold value of the safety valve, the organic gas in the liquid storage tank is conveyed to the pressure equalizing device 501.
Figure 5 shows a device schematic of an oil and gas treatment system according to a fifth embodiment of the invention. As shown in fig. 5, the oil and gas treatment system according to the fifth embodiment of the present invention includes a pressurizing device 301, a heat exchanging device 401, a condensing device 101, a refrigerating device 102, a pressure equalizing device 501, and a gas generator 201.
Volatile organic compounds (VCOS) to be treated, such as oil and gas to be treated for loading, loading or washing a vessel, are fed to the pressurizing device 301 for pressurization. Optionally, the concentration of the oil gas to be treated is 10-40% (V/V), the pressurizing device 301 is an explosion-proof claw type compressor (the treatment capacity is 100-3H). The explosion-proof claw type compressor pressurizes the received oil gas to 200kpa (G).
The high-pressure oil gas pressurized by the pressurizing device 301 is conveyed to the heat exchange device 401 through a pipeline for heat exchange. The heat exchange device 401 outputs high-pressure oil gas with lower temperature. Optionally, the heat exchange device 401 is a cold recovery heat exchanger, and can pre-cool the high-pressure oil gas output by the pressurizing device 301, so as to reduce the temperature of the high-pressure oil gas to 45 ℃.
The oil gas after heat exchange by the heat exchange device 401 is conveyed to the condensing device 101 for condensation. Liquid organic matters and non-condensable gas are respectively obtained after condensation. The liquid organic matter is conveyed to the liquid storage tank through a pipeline for recovery. Optionally, the condensing device 101 is a VOC condenser. The condensation temperature of the VOC condenser was-25 ℃. And condensing the oil gas in a VOC condenser to obtain liquid organic matters and non-condensable gas. The oil gas concentration in the obtained non-condensable gas is reduced to 5-10% (V/V). After condensation, the heavy hydrocarbon is condensed into liquid and recovered to the liquid storage tank. The storage pressure of the liquid storage tank is, for example, 200 kpa. VOC condensers employ, for example, mechanical refrigeration with refrigerants R22 or R404A.
The refrigeration device 102 is connected to the condensation device 101 for providing a low temperature environment for the condensation device 101. The refrigeration apparatus 102 includes, for example, a refrigeration compressor 1021, a liquid separator 1022, an air cooler 1023, and an expansion valve 1024. Optionally, the refrigerant is pressurized by the refrigeration compressor 1021, separated by the liquid separator 1022, and cooled by the air cooler 1023 in sequence, and then is decompressed by the expansion valve 1024 to realize evaporation refrigeration in the condensation device 101. The refrigerant temperature was controlled at-30 ℃.
The condensing unit 101 is also connected to a heat exchanging unit 401. After passing through the condensing unit 101, the uncondensed noncondensable gas enters the heat exchange unit 401 to exchange heat. Optionally, heat exchange device 401 is a cold recovery heat exchanger. The temperature of the-25 ℃ non-condensable gas output by the condensing device 101 is raised to 20 ℃ in the cold recovery heat exchanger.
The heat exchange device 401 is connected with the pressure equalizing device 501. The pressure value of the non-condensable gas after heat exchange is adjusted in the pressure equalizing device 501. Optionally, the pressure equalizing device 501 is a gas mixture pressure equalizer. The gas mixing pressure equalizer is connected with the heat exchange device 401 and is connected with the liquid storage tank through a pipeline.
The gas generator 201 is, for example, a piston-type gas generator set. The generator set receives the non-condensable gas conveyed by the pressure equalizing device 501, and the non-condensable gas is combusted, so that power generation is realized. Optionally, the pressure equalization device 501 is also connected to a Liquefied Petroleum Gas (LPG) storage tank. The non-condensable gas passing through the pressure equalizing device 501 is sent to the piston type gas generator set to generate electricity. Liquefied Petroleum Gas (LPG) storage tanks are used to vary the composition of the gas delivered to a piston engine to equalize the heating value of the gas delivered to the piston engine. The piston engine drives the generator to generate electricity, and the generated power is 30-100kw, for example. Alternatively, the piston engine is selected according to national VI emission standards and has controlled emissions of less than 20mg/m NMHC (non-methane total hydrocarbons)3。
The gas generator 201 is connected to the claw compressor, the refrigeration compressor 1021, and the air cooler 1023, respectively. The power generated by the gas generator 201 is supplied to the claw compressor, the refrigerating compressor 1021, and the air cooler 1023 as operating power.
In the above embodiment, the oil gas treatment system includes a pressure equalizing device and a gas storage tank, and can adjust the components and pressure of the gas delivered to the gas generator, thereby ensuring the stability of combustion power generation.
Figure 6 shows a device schematic of an oil and gas treatment system according to a sixth embodiment of the invention. As shown in fig. 6, the oil and gas treatment system according to the sixth embodiment of the present invention is a skid mounted device. Optionally, the oil and gas treatment system is mounted on a mobile platform to form a mobile skid.
In an alternative embodiment of the invention, the oil and gas treatment system is mounted on the truck chassis using a mobile skid. The oil gas treatment system comprises a pressurizing device 301, a control device 601, a heat exchange device 401, a condensing device 101, a liquid storage tank 602, an air cooler 1023, a Liquefied Petroleum Gas (LPG) storage tank 603, a refrigeration compressor 1021, a pressure equalizing device 501 and a gas generator 201. The control device 601 is used for controlling the oil and gas treatment system, such as a PLC control cabinet. The layout positions of various devices in the oil and gas treatment system are shown in the figure. The connection relationship between the respective devices can be referred to above. The control device 601 is connected to a device to be controlled. The oil and gas treatment system according to this embodiment is arranged apart from width 2.8 meters, and is 13 meters long, adopts standard transport vechicle width can place on flatbed trailer and transport.
In the embodiment, the oil and gas treatment system is skid-mounted equipment installed on mobile equipment, and can meet treatment requirements in different environments.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrase "comprising an … …" does not exclude the presence of other identical elements in a process, method, article, or apparatus that comprises the element.
While embodiments in accordance with the invention have been described above, these embodiments are not intended to be exhaustive or to limit the invention to the precise embodiments described. Obviously, many modifications and variations are possible in light of the above teaching. The embodiments were chosen and described in order to best explain the principles of the invention and the practical application, to thereby enable others skilled in the art to best utilize the invention and various embodiments with various modifications as are suited to the particular use contemplated. The invention is limited only by the claims and their full scope and equivalents.
Claims (9)
1. An oil and gas treatment system, comprising:
the condensing device is used for condensing the oil gas to be treated to obtain liquid organic matters and non-condensable gas; and
the gas generator is connected with the condensing device to obtain the non-condensable gas for combustion power generation,
wherein, the electric energy that the gas generator produced is used for providing low temperature environment for condensing equipment.
2. The hydrocarbon processing system of claim 1, further comprising:
the pressurizing device is connected with the condensing device and used for pressurizing oil gas to obtain the oil gas to be treated and providing the oil gas to be treated for the condensing device,
wherein the electric energy generated by the gas generator is used for driving the pressurizing device.
3. The hydrocarbon processing system of claim 1, further comprising:
the heat exchange device is connected with the gas inlet end of the condensing device to provide the oil gas to be treated for the condensing device, and is connected with the gas outlet end of the condensing device to receive the non-condensable gas,
and the oil gas to be treated is used as hot fluid, the non-condensable gas is used as cold fluid, and heat exchange is carried out in the heat exchange device.
4. The hydrocarbon processing system of claim 1, further comprising:
and the pressure equalizing device is connected with the condensing device to receive the non-condensable gas and is used for adjusting the air pressure of the non-condensable gas.
5. The hydrocarbon processing system of claim 4, further comprising:
a liquid storage tank connected with the condensing device to receive the liquid organic matter,
the liquid storage tank is connected with the pressure equalizing device, and gas generated in the liquid storage tank is conveyed to the pressure equalizing device.
6. The oil and gas treatment system according to claim 1, wherein said condensing means is connected to said gas generator by a conduit to provide said non-condensable gasses to said gas generator;
the oil and gas treatment system further comprises:
a gas storage tank for storing combustible gas and connected with the pipeline to provide the combustible gas into the pipeline,
and the non-condensable gas and the combustible gas are mixed and then are conveyed to the gas generator.
7. The hydrocarbon processing system of claim 1, further comprising:
a refrigerating device connected with the condensing device and used for providing a low-temperature environment for the condensing device,
the electric energy generated by the gas generator is used for driving the refrigerating device to refrigerate.
8. The oil and gas treatment system of claim 7, wherein the refrigeration device comprises:
a refrigeration compressor connected to the condensing device to receive a refrigerant and pressurize the refrigerant;
the liquid separator is connected with the refrigeration compressor to receive the pressurized refrigerant and separate the liquid of the pressurized refrigerant;
the air cooler is connected with the liquid separator to receive the refrigerant after liquid separation and cool the refrigerant after liquid separation;
the gas generator is respectively connected with the refrigeration compressor and the air cooler and used for driving the refrigeration compressor and the air cooler.
9. The oil and gas treatment system of claim 1, wherein the oil and gas treatment system is mounted on a mobile platform to form a skid-mounted facility.
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| CN110960952A (en) * | 2019-12-20 | 2020-04-07 | 海湾环境科技（北京）股份有限公司 | Oil and gas treatment system and oil and gas treatment method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110960952A (en) * | 2019-12-20 | 2020-04-07 | 海湾环境科技（北京）股份有限公司 | Oil and gas treatment system and oil and gas treatment method |
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