CN208065963U - Oil and gas separating system and industrial oxygenerating system including the oil and gas separating system - Google Patents
Oil and gas separating system and industrial oxygenerating system including the oil and gas separating system Download PDFInfo
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- CN208065963U CN208065963U CN201820113093.2U CN201820113093U CN208065963U CN 208065963 U CN208065963 U CN 208065963U CN 201820113093 U CN201820113093 U CN 201820113093U CN 208065963 U CN208065963 U CN 208065963U
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Abstract
The utility model is related to Oil-gas Separation technical fields, are specifically related to a kind of oil and gas separating system and the industrial oxygenerating system including the oil and gas separating system.The utility model aim to solve the problem that in fuel tank in the prior art the excessively high fluid caused in industrial oxygenerating system of air pressure cannot oil return normal to fuel tank the problem of.For this purpose, the oil and gas separating system of the utility model includes：Gs-oil separator, the oil and gas import of gs-oil separator are connected to the oil gas vent of fuel tank；Drainage device, drainage device are connected to the oil and gas import of the oil gas vent of fuel tank and gs-oil separator respectively, for introducing the oil gas in fuel tank in gs-oil separator.The utility model is by the way that drainage device to be connected to the oil and gas import of the oil gas vent of fuel tank and gs-oil separator respectively; oil gas in fuel tank is introduced in gs-oil separator; to reduce the air pressure in fuel tank; enable the fluid in industrial oxygenerating system to the normal oil return of fuel tank, to improve the oil return stability of industrial oxygenerating system.
Description
Technical field
The utility model is related to Oil-gas Separation technical fields, more particularly to a kind of oil and gas separating system and including the oil gas point
Industrial oxygenerating system from system.
Background technology
This part provide be only with the relevant background information of the disclosure, be not necessarily the prior art.
Oxygen compressor processed in industrial oxygenerating system needs that oil lubrication, lubricating oil is used generally to use and follow at work
The mode of ring centralized oil supply, i.e., oxygen compressor processed are connected with fuel tank, and fuel tank provides lubricating oil to oxygen compressor processed, and lubricating oil flows through
Fuel tank is flowed back into after oxygen compressor processed again to use as lubrication next time, lubricating oil is usually taken back largely during reflux
To fuel tank, the mixed oil and gas of these high temperature forms mist of oil in fuel tank, fuel tank internal is made to be formed just for frictional heat and high-temperature gas
Pressure, interferes the oil return of lubricating oil, causes the lubricating oil in industrial oxygenerating system without the normal oil return of normal direction fuel tank.
In order to solve the above-mentioned technical problem, fuel tank is connected to air-extractor by technical staff, will be in fuel tank by air-extractor
Gas be discharged fuel tank, reduce fuel tank in air pressure, enable lubricating oil to the normal oil return of fuel tank, meanwhile, air-extractor will
During gas discharge fuel tank in fuel tank, the mist of oil in fuel tank is discharged oil with the gas in fuel tank together in order to prevent
Case causes lubricating oil waste and environmental pollution, technical staff to connect gs-oil separator, oil gas between air-extractor and fuel tank
The gas in the mixed gas that be discharged from fuel tank can be discharged for separator, and the fluid in mixed gas is made to flow back into oil again
In case, to reduce lubricating oil waste and environmental pollution.
Although lubricating oil wave can be solved substantially by way of connecting gs-oil separator between air-extractor and fuel tank
Take and the problem of environmental pollution, still, in actual application, there are security risks, such as when air-extractor powers off suddenly
When, the mist of oil in fuel tank can not normally be discharged, and the gas pressure in fuel tank is caused to increase, in fuel tank air pressure increase cause to flow through system
Fluid after oxygen compressor can not lead to the fluid evaporating, emitting, dripping or leaking of liquid or gas in oxygen compressor processed, seriously affect in normal reflow to fuel tank
Environment and there are security risks, meanwhile, fluid can not normal reflow to fuel tank can cause fuel tank can not be normally to oxygen pressure processed
Contracting machine fuel feeding, eventually even will appear the phenomenon that oxygen compressor processed is burned due to non lubricant oil.
Utility model content
The purpose of this utility model is to propose one kind for improving tank drainback stabilization in view of the above shortcomings of the prior art
Property oil and gas separating system, oil and gas separating system by fuel tank oil gas introduce gs-oil separator in, to reduce the gas in fuel tank
Pressure enables fluid in industrial oxygenerating system to the normal oil return of fuel tank.The purpose is achieved through the following technical solutions.
The first aspect of the utility model provides a kind of oil and gas separating system for fuel tank, wherein Oil-gas Separation system
System includes：Gs-oil separator, the oil and gas import of gs-oil separator are connected to the oil gas vent of fuel tank；Drainage device, drainage device
It is connected to respectively with the oil and gas import of the oil gas vent of fuel tank and gs-oil separator, for the oil gas in fuel tank to be introduced Oil-gas Separation
In device.
Preferably, drainage device includes：Air source stores drainage gas in air source；First pipeline, the first of the first pipeline
The gas outlet of end connection air source, the second end of the first pipeline be respectively communicated with fuel tank oil gas vent and gs-oil separator oil gas into
Mouthful.
Preferably, drainage device further includes：Compressor, compressor are connected in the first pipeline, the air inlet of compressor with
Air source is connected to, and the exhaust outlet of compressor is connected to the second end of the first pipeline.
Preferably, drainage device further includes：Drainage component, drainage component is communicated in the second end of the first pipeline, and drains
Component is connected to the oil and gas import of the oil gas vent of fuel tank and gs-oil separator respectively.
Preferably, drainage component includes：Injection pipe, the jet port internal diameter of injection pipe are less than the interior of the second end of the first pipeline
Diameter, injection pipe are connected to the second end of the first pipeline；The receiving port internal diameter of reception pipe, reception pipe is more than jet port internal diameter, and connects
It closes up and is arranged with jet port relative gap, reception pipe is connected to the oil and gas import of gs-oil separator；Pipe is accommodated, pipe sleeve is accommodated and is set to
Outside receiving port and jet port, receiving port and jet port are located in the accommodating chamber for accommodating pipe, and accommodate pipe in receiving port and jet port
Between gap location and fuel tank oil gas vent penetrate through.
Preferably, oil and gas separating system further includes：Air-extractor, the exhaust of the bleeding point and gs-oil separator of air-extractor
Mouth connection, for extracting the gas in gs-oil separator.
Preferably, oil and gas separating system further includes：Second pipeline, the exhaust of one end connection gs-oil separator of the second pipeline
Mouthful, the exhaust outlet of the other end connection air-extractor of the second pipeline；By-passing valve, by-passing valve are connected in the second pipeline, and respectively
It is communicated with the exhaust outlet of the exhaust outlet of gs-oil separator and air-extractor.
Preferably, oil and gas separating system further includes：Controller, controller are connect with air-extractor and compressor respectively, are used
In the unlatching of control air-extractor and compressor.
The second aspect of the utility model additionally provides a kind of industrial oxygenerating system, wherein industrial oxygenerating system includes：System
Oxygen compressor；Fuel tank, fuel tank connect with oxygen compressor processed and to oxygen compressor fuel feeding processed and receive the oil return of oxygen compressor processed；
Oil and gas separating system, oil and gas separating system are connect with fuel tank, for the gas in the oil return in fuel tank to be discharged, wherein oil gas
Piece-rate system is the oil and gas separating system of the utility model first aspect.
It will be appreciated to those of skill in the art that in the technical solution of the utility model, by the way that drainage device is divided
It is not connected to the oil and gas import of the oil gas vent of fuel tank and gs-oil separator, the oil gas in fuel tank can be introduced oil by drainage device
In gas separating device, to reduce the air pressure in fuel tank, enable the fluid in industrial oxygenerating system to the normal oil return of fuel tank, to carry
The oil return stability of high industry oxygen generation system.Specifically, drainage device includes air source, compressor and drainage component, compressor with
For being high-speed flow by the gas compression in air source, high-speed flow flows into the injection through injection pipe in drainage component for air source connection
The oil gas at injection pipe jet port is brought into gs-oil separator afterwards, at this point, the air pressure at injection pipe jet port reduces, in order to mend
Repay the air pressure at injection pipe jet port, the fuel tank being connect with drainage component to conveying oil gas at drainage component jet port, fuel tank to
The injection through injection pipe flows into gs-oil separator the oil gas conveyed at drainage component jet port again, and recycling this process will be in fuel tank
Oil-gas jetting into gs-oil separator, be injected into oil gas exhaust of the gas from gs-oil separator after filtering in gs-oil separator
Mouth discharge, fluid are back to from the oil return opening of gs-oil separator in fuel tank, at this point, gs-oil separator is completed to the oil gas in fuel tank
Carry out the purpose of Oil-gas Separation.
Further, it is that opposite pumping is set that the drainage device of the utility model, which includes air source, compressor and drainage component,
Standby independent equipment, therefore, when air-extractor failure, the drainage device of the utility model remains to work normally, will be in fuel tank
Oil gas introduce gs-oil separator in then after filtering gas from the exhaust outlet of gs-oil separator be discharged, from gs-oil separator
The gas of exhaust outlet discharge drains into the exhaust outlet of air-extractor by by-passing valve again, and so far gs-oil separator completion will be oily in fuel tank
The purpose of gas discharge in gas.
Description of the drawings
By reading the detailed description of hereafter preferred embodiment, various other advantages and benefit are common for this field
Technical staff will become clear.Attached drawing only for the purpose of illustrating preferred embodiments, and is not considered as to this practicality
Novel limitation.And throughout the drawings, the same reference numbers will be used to refer to the same parts.In the accompanying drawings：
Fig. 1 is the structural schematic diagram of the oil and gas separating system of the utility model one embodiment.
Fig. 2 is the structural schematic diagram of drainage device in oil and gas separating system shown in Fig. 1.
Wherein, 01, oil and gas separating system；10, fuel tank；11, the oil gas vent of fuel tank；12, the oil return opening of fuel tank；13, oily
The oil outlet of case；14, oil pipe；20, gs-oil separator；21, the oil and gas import of gs-oil separator；22, the filter core of gs-oil separator；
23, the exhaust outlet of gs-oil separator；30, drainage device；31, air source；32, compressor；33, drainage component；331, injection pipe；
332, jet port；333, reception pipe；334, receiving port；335, pipe is accommodated；336, the first pipeline；40, air-extractor；50, second
Pipeline；51, by-passing valve；60, controller.
Specific implementation mode
The illustrative embodiments of the disclosure are more fully described below with reference to accompanying drawings.Although showing this public affairs in attached drawing
The illustrative embodiments opened, it being understood, however, that may be realized in various forms the disclosure without the reality that should be illustrated here
The mode of applying is limited.It is to be able to be best understood from the disclosure on the contrary, providing these embodiments, and can be by this public affairs
The range opened completely is communicated to those skilled in the art.
It should be understood that term used herein merely for description particular example embodiment purpose, and have no intention into
Row limitation.Unless the context clearly indicates otherwise, otherwise singulative " one " as used in the text, "one" and " described "
Can also indicate to include plural form.Term " comprising ", " having " are inclusives, and therefore indicate stated feature,
The presence of element and/or component, but be not precluded presence or add one or more of the other feature, component, assembly unit, and/or
Combination thereof.
Although can multiple element, component, region, layer and/or portion be described using term first, second etc. in the text
Section still these component, assembly units, region, layer and/or is limited by these terms than Duan Buying.These terms can only be used for
One component, assembly unit, region, layer or section are distinguished with another region, layer or section.Unless context it is manifestly intended that
Otherwise sequence or secondary is not implied that when the term and other numerical terms of such as " first ", " second " etc use in the text
Sequence.Therefore, title can be in the case where not departing from the introduction of example embodiment for the first pipeline discussed below, the second pipeline
It exchanges.
For ease of description, an element as illustrated in the diagram can be described use space relativeness term in the text
Either feature is relative to another element or the relationship of feature, these relativeness terms are, for example, " inside ", " outside ", " interior
Side ", " outside ", " following ", " lower section ", " above ", " top " etc..This spatial correlation term is intended to include removing to retouch in figure
The different direction of device in use or operation except the orientation painted.For example, if the device in figure is overturn, retouch
State the element for " below other elements either feature " or " below other elements or feature " will then be orientated "
Other elements are either above feature " or " above other elements or feature ".Therefore, exemplary term can " in ... lower section "
To include in orientation upper and under.In addition device can be oriented and (be rotated by 90 ° or in other directions) and used herein
Spatial correlation descriptor correspondingly explains.
Fig. 1 is the structural schematic diagram of the oil and gas separating system of the utility model one embodiment.
Fig. 2 is the structural schematic diagram of drainage device in oil and gas separating system shown in Fig. 1.
As depicted in figs. 1 and 2, preferred embodiment according to the present utility model provides a kind of oil gas for fuel tank 10
Piece-rate system 01, oil and gas separating system 01 include gs-oil separator 20 and drainage device 30, wherein the oil gas of gs-oil separator into
Mouthfuls 21 are connected to the oil gas vent 11 of fuel tank, the oil gas with the oil gas vent of fuel tank 11 and gs-oil separator respectively of drainage device 30
Import 21 is connected to, and for introducing the oil gas in fuel tank 10 in gs-oil separator 20, makes gs-oil separator 20 in fuel tank 10
Oil gas carries out Oil-gas Separation.Below by industrial oxygenerating system to the specific embodiment party of the oil and gas separating system 01 of the utility model
Formula and technique effect are described in detail, and the oxygen compressor processed in industrial oxygenerating system needs to use oil lubrication at work,
Fuel tank 10 generally uses the mode of cycle centralized oil supply for oxygen compressor fuel feeding processed, i.e., oxygen compressor processed is connected with fuel tank 10, oil
Case 10 provides lubricating oil by the oil outlet 13 of fuel tank to oxygen compressor processed, and lubricating oil passes through fuel tank again after flowing through oxygen compressor processed
Oil return opening 12 flow back into fuel tank 10 and used as lubrication next time, lubricating oil usually takes back during reflux and largely rubs
To fuel tank 10, the mixed oil and gas of these high temperature forms mist of oil in fuel tank 10, makes 10 inside shape of fuel tank for chafing amount and high-temperature gas
At positive pressure, the normal oil return of lubricating oil is interfered, in order to solve the above-mentioned technical problem, the oil and gas separating system 01 of the utility model exists
Gs-oil separator 20 is connected on fuel tank 10, gs-oil separator 20 is gs-oil separator 20 common in industrial oxygenerating system, oil
Gas separating device 20 is internally provided with filter core, and the filter core 22 of gs-oil separator can will flow into the mixed gas in gs-oil separator 20
In gas discharge, and the fluid in mixed gas is flowed back into again in fuel tank 10, to reduce lubricating oil waste and environment
Pollution, in order to which the mixed oil and gas in fuel tank 10 is introduced into gs-oil separator 20, the oil and gas separating system 01 of the utility model
Drainage device 30 is provided between fuel tank 10 and gs-oil separator 20, drainage device 30 is continuous by the mixed oil and gas in fuel tank 10
Ground is introduced into gs-oil separator 20, to realize that gs-oil separator 20 carries out Oil-gas Separation to the mixed oil and gas in fuel tank 10
Purpose.Only show it should be noted that the oil and gas separating system 01 of the utility model is described by industrial oxygenerating system
Example property, be not the limitation to 01 application range of oil and gas separating system of the utility model, the Oil-gas Separation of the utility model
System 01 is also applied in other systems, and in air-conditioning system, the adjustment of this application range is new without departing from this practicality
The protection domain of type.
With continued reference to Fig. 1 and Fig. 2, the drainage device 30 of preferred embodiment according to the present utility model, the utility model wraps
The first pipeline 336 for including air source 31 and being connect with air source 31, wherein drainage gas such as nitrogen, the first pipe are stored in air source 31
The gas outlet of the first end connection air source 31 on road 336, the second end of the first pipeline 336 are respectively communicated with 11 He of oil gas vent of fuel tank
The oil and gas import 21 of gs-oil separator.Wherein, the gas in air source 31 is flowed to through the first pipeline 336 in gs-oil separator 20,
During this, due to the second end of the first pipeline 336 be respectively communicated with fuel tank oil gas vent 11 and gs-oil separator oil gas into
Mouth 21, therefore, the gas in air source 31 can drive oily between the oil and gas import 21 of gs-oil separator and the oil gas vent 11 of fuel tank
Oil gas in pipe 14 flows into gs-oil separator 20, and the oil gas in fuel tank 10 passes through the oil gas vent of fuel tank 11 and Oil-gas Separation again
The oil and gas import 21 of device flows into oil pipe 14, recycles this flow process, final to realize gs-oil separator 20 to the oil in fuel tank 10
Gas carries out the purpose of Oil-gas Separation.
With continued reference to Fig. 1 and Fig. 2, preferred embodiment according to the present utility model, in order to improve the drainage of the utility model
The drainage device 30 of the drainage effect of equipment 30, the utility model is connected with compressor 32, compressor 32 in the first pipeline 336
Air inlet be connected to air source 31, the exhaust outlet of compressor 32 is connected to the second end of the first pipeline 336.Therefore, compressor 32
Can be high-speed flow by the drainage gas compression in air source 31, high-speed flow can not only improve gas in the first pipeline 336
Flowing velocity, the gas stream in oil pipe 14 between 10 oil gas vent of 20 oil and gas import of gs-oil separator and fuel tank can also be improved
The speed for entering gs-oil separator 20, to improve the drainage effect of drainage device 30.
With continued reference to Fig. 1 and Fig. 2, preferred embodiment according to the present utility model, in order to further increase the utility model
Drainage device 30 drainage effect, the drainage device 30 of the utility model further includes drainage component 33, and drainage component 33 is connected to
In the second end of the first pipeline 336, and drainage component 33 respectively with the oil gas of the oil gas vent of fuel tank 11 and gs-oil separator into
Mouth 21 is connected to.Drainage component 33 is set by the second end in the first pipeline 336, is the drainage gas band in the first pipeline 336
Oil gas in dynamic oil pipe 14 provides drainage environment, i.e. drainage gas in the first pipeline 336 can drive in drainage component 33
Oil gas enter gs-oil separator 20, to improve the drainage effect of drainage device 30, meanwhile, drainage component 33 also be the first pipeline
Drainage gas in 336 provides flow direction, reduces the phenomenon that the drainage gas in the first pipeline 336 flows into fuel tank 10.
Specifically, drainage component 33 includes injection pipe 331, reception pipe 333 and receiving pipe 335, wherein the jet port 332 of injection pipe 331
Internal diameter is less than the second end internal diameter of the first pipeline 336, one end opposite with jet port 332 of injection pipe 331 and the first pipeline 336
Second end connection, 334 internal diameter of receiving port of reception pipe 333 is more than 332 internal diameter of jet port, and receiving port 334 and jet port 332
Relative gap is arranged, and the one end opposite with receiving port 334 of reception pipe 333 is connected to the oil and gas import 21 of gs-oil separator, accommodates
Pipe 335 is sheathed on receiving port 334 with outside jet port 332, and receiving port 334 is made to be located at the accommodating chamber for accommodating pipe 335 with jet port 332
It is interior, and accommodate oil pipe 14 perforation of gap location of the pipe 335 between receiving port 334 and jet port 332 with fuel tank 10.This practicality is new
Type can make first by the way that 332 internal diameter of jet port of injection pipe 331 to be set smaller than to the second end internal diameter of the first pipeline 336
Drainage gas in pipeline 336 flows to the receiving port 334 of reception pipe 333, drawing in the first pipeline 336 in such a way that high speed is sprayed
Gas body drives the oil gas accommodated in pipe 335 to be flowed into gs-oil separator 20 by reception pipe 333 during high speed is sprayed,
At this point, the air pressure accommodated in pipe 335 reduces, and in order to compensate for the air pressure accommodated in pipe 335, the fuel tank 10 being connected to receiving pipe 335
Oil gas is conveyed into receiving pipe 335 by oil pipe 14, the drainage gas in the first pipeline 336 will accommodate the oil gas in pipe 335 again
It brings into gs-oil separator 20, gs-oil separator 20 carries out Oil-gas Separation, cycle to the oil gas flowed into gs-oil separator 20 again
This flow process realizes that gs-oil separator 20 carries out the oil gas in fuel tank 10 purpose of Oil-gas Separation.
With continued reference to Fig. 1 and Fig. 2, preferred embodiment according to the present utility model, the oil and gas separating system of the utility model
01 is additionally provided with air-extractor 40, and the bleeding point of air-extractor 40 is connected to the exhaust outlet 23 of gs-oil separator, for extracting oil
Gas in gas separating device 20.Wherein, air-extractor 40 be the common aspiration pump in this field be either evacuated wind turbine aspiration pump or
Gas in gs-oil separator 20 can be extracted out and is emitted into air by pumping wind turbine, make to keep centainly in gs-oil separator 20
Vacuum degree automatically flows into gs-oil separator 20 to make the high-pressure oil gas in fuel tank 10 pass through oil pipe 14, makes gs-oil separator 20
Complete the purpose to the high-pressure oil gas progress Oil-gas Separation in fuel tank 10, it should be noted that the utility model drainage device 30
In air source 31, compressor 32 and drainage component 33 be opposite 40 independent equipment of air-extractor, therefore, when air-extractor 40
When failure, the drainage device 30 of the utility model remains to work normally, and the oil gas in fuel tank 10 is introduced in gs-oil separator 20
It is discharged from the exhaust outlet of gs-oil separator 23 after the filtering of gs-oil separator 20, by relatively independent drainage device 30 and takes out
Gas equipment 40 can improve the stability of the utility model oil and gas separating system 01.
With continued reference to Fig. 1 and Fig. 2, preferred embodiment according to the present utility model, in order to make the utility model Oil-gas Separation
Device 20 still is able to the gas in gs-oil separator 20 gs-oil separator 20, the utility model is discharged in 40 failure of air-extractor
Oil and gas separating system 01 be provided with connection 20 exhaust outlet of gs-oil separator and 40 exhaust outlet of air-extractor second pipe, second
By-passing valve 51 is provided in pipeline 50.Therefore, when 40 failure of air-extractor, the high pressure gas of 20 exhaust ports of gs-oil separator without
When method is discharged from air-extractor 40, high pressure gas is opened and is provided with by-passing valve 51 in the second pipeline 50, and gs-oil separator 20 is vented
The exhaust outlet that high pressure gas at mouthful drains into air-extractor 40 by by-passing valve 51 flows into air again.
With continued reference to Fig. 1 and Fig. 2, preferred embodiment according to the present utility model, in order to make the drainage of the utility model set
Standby 30 can in time react to the failure of air-extractor 40, and control is additionally provided in the oil and gas separating system 01 of the utility model
Device 60 processed, controller 60 are connect with air-extractor 40 and compressor 32 respectively, for controlling air-extractor 40 and compressor 32
It opens.Wherein, controller 60 can detect the working condition of air-extractor 40 in real time, when air-extractor 40 is in normal work shape
When state, controller 60 controls 32 low-power operation of compressor in air-extractor 40 or is not turned on compressor 32, when pumping is set
When being stopped due to failure for 40, controller 60 controls compressor 32 plus high power work in drainage device 30, so as to draw
Oil gas in fuel tank 10 can be introduced into gs-oil separator 20 by flow device 30, to reduce the oil pressure in fuel tank 10, make industry
Lubricating oil in oxygen generation system can be to 10 normal oil return of fuel tank.
Finally, second aspect according to the present utility model, the utility model also proposed a kind of industrial oxygenerating system,
In, industrial oxygenerating system includes：Oxygen compressor processed；Fuel tank 10, fuel tank 10 connect with oxygen compressor processed and are supplied to oxygen compressor processed
Oil and the oil return for receiving oxygen compressor processed；Oil and gas separating system 01, oil and gas separating system 01 are connect with fuel tank 10, and being used for will be oily
Gas discharge in oil return in case 10, wherein oil and gas separating system 01 is the Oil-gas Separation system of the utility model first aspect
System 01.Therefore, the industrial oxygenerating system of the utility model has the incision technology effect of the oil and gas separating system 01 of the utility model
Fruit, details are not described herein.
The preferable specific implementation mode of the above, only the utility model, but the scope of protection of the utility model is not
It is confined to this, any one skilled in the art within the technical scope disclosed by the utility model, can readily occur in
Change or replacement, should be covered within the scope of the utility model.Therefore, the scope of protection of the utility model should be with
Subject to the scope of the claims.
Claims (9)
1. a kind of oil and gas separating system for fuel tank, which is characterized in that the oil and gas separating system includes：
Gs-oil separator, the oil and gas import of the gs-oil separator are connected to the oil gas vent of the fuel tank；
Drainage device, the drainage device connect with the oil and gas import of the oil gas vent of the fuel tank and the gs-oil separator respectively
It is logical, for the oil gas in the fuel tank to be introduced in the gs-oil separator.
2. oil and gas separating system according to claim 1, which is characterized in that the drainage device includes：
Air source stores drainage gas in the air source；
The first end of first pipeline, first pipeline is connected to the gas outlet of the air source, the second end point of first pipeline
It is not connected to the oil and gas import of the oil gas vent and the gs-oil separator of the fuel tank.
3. oil and gas separating system according to claim 2, which is characterized in that the drainage device further includes：
Compressor, the compressor are connected in first pipeline, and the air inlet of the compressor is connected to the air source, institute
The exhaust outlet for stating compressor is connected to the second end of first pipeline.
4. oil and gas separating system according to claim 3, which is characterized in that the drainage device further includes：
Drainage component, the drainage component are communicated in the second end of first pipeline, and the drainage component respectively with it is described
The oil gas vent of fuel tank is connected to the oil and gas import of the gs-oil separator.
5. oil and gas separating system according to claim 4, which is characterized in that the drainage component includes：
Injection pipe, the jet port internal diameter of the injection pipe are less than the internal diameter of the second end of first pipeline, the injection pipe with
The second end of first pipeline is connected to；
The receiving port internal diameter of reception pipe, the reception pipe is more than the jet port internal diameter, and the receiving port and the jet port
Relative gap is arranged, and the reception pipe is connected to the oil and gas import of the gs-oil separator；
Pipe is accommodated, the receiving pipe sleeve is set to outside the receiving port and the jet port, the receiving port and the jet port position
In in the accommodating chamber for accommodating pipe, and it is described accommodate gap location of the pipe between the receiving port and the jet port with it is described
The oil gas vent of fuel tank penetrates through.
6. oil and gas separating system according to claim 5, which is characterized in that the oil and gas separating system further includes：
Air-extractor, the bleeding point of the air-extractor are connected to the exhaust outlet of the gs-oil separator, for extracting the oil
Gas in gas separating device.
7. oil and gas separating system according to claim 6, which is characterized in that the oil and gas separating system further includes：
Second pipeline, one end of second pipeline are connected to the exhaust outlet of the gs-oil separator, second pipeline it is another
End is connected to the exhaust outlet of the air-extractor；
By-passing valve, the by-passing valve are connected in second pipeline, and respectively with the exhaust outlet of the gs-oil separator and institute
The exhaust outlet for stating air-extractor communicates.
8. oil and gas separating system according to claim 7, which is characterized in that the oil and gas separating system further includes：
Controller, the controller are connect with the air-extractor and the compressor respectively, for controlling the air-extractor
With the unlatching of the compressor.
9. a kind of industrial oxygenerating system, which is characterized in that the industrial oxygenerating system includes：
Oxygen compressor processed；
Fuel tank, the fuel tank connect with the oxygen compressor processed and to the oxygen compressor fuel feeding processed and receive the oxygen pressure processed
The oil return of contracting machine；
Oil and gas separating system, the oil and gas separating system are connect with the fuel tank, and being used for will be in the oil return in the fuel tank
Gas discharge, wherein the oil and gas separating system be oil and gas separating system described in any item of the claim 1 to 8.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820113093.2U CN208065963U (en) | 2018-01-23 | 2018-01-23 | Oil and gas separating system and industrial oxygenerating system including the oil and gas separating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820113093.2U CN208065963U (en) | 2018-01-23 | 2018-01-23 | Oil and gas separating system and industrial oxygenerating system including the oil and gas separating system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208065963U true CN208065963U (en) | 2018-11-09 |
Family
ID=64035879
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820113093.2U Expired - Fee Related CN208065963U (en) | 2018-01-23 | 2018-01-23 | Oil and gas separating system and industrial oxygenerating system including the oil and gas separating system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208065963U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115247100A (en) * | 2021-04-27 | 2022-10-28 | 广州市洁科不锈钢设备有限公司 | Castor oil micro-water removal system |
-
2018
- 2018-01-23 CN CN201820113093.2U patent/CN208065963U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115247100A (en) * | 2021-04-27 | 2022-10-28 | 广州市洁科不锈钢设备有限公司 | Castor oil micro-water removal system |
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