CN106368669B - Oil vapor treatment method - Google Patents
Oil vapor treatment method Download PDFInfo
- Publication number
- CN106368669B CN106368669B CN201610769425.8A CN201610769425A CN106368669B CN 106368669 B CN106368669 B CN 106368669B CN 201610769425 A CN201610769425 A CN 201610769425A CN 106368669 B CN106368669 B CN 106368669B
- Authority
- CN
- China
- Prior art keywords
- liquid
- gas
- primary
- outlet
- treatment method
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000000034 method Methods 0.000 title claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 215
- 239000000203 mixture Substances 0.000 claims abstract description 94
- 238000000926 separation method Methods 0.000 claims abstract description 42
- 230000000630 rising effect Effects 0.000 claims description 13
- 230000005484 gravity Effects 0.000 claims description 11
- 238000001914 filtration Methods 0.000 claims description 7
- 230000005855 radiation Effects 0.000 claims description 6
- 241000219422 Urtica Species 0.000 claims description 2
- 235000009108 Urtica dioica Nutrition 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 170
- 239000003921 oil Substances 0.000 description 25
- 230000000694 effects Effects 0.000 description 16
- 238000003756 stirring Methods 0.000 description 8
- 238000005452 bending Methods 0.000 description 7
- 239000010410 layer Substances 0.000 description 6
- 239000003129 oil well Substances 0.000 description 6
- 230000017525 heat dissipation Effects 0.000 description 5
- 238000001816 cooling Methods 0.000 description 3
- 239000011229 interlayer Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/34—Arrangements for separating materials produced by the well
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
- B01D46/62—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
- C10L2290/547—Filtration for separating fractions, components or impurities during preparation or upgrading of a fuel
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mining & Mineral Resources (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- Physics & Mathematics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
The present invention relates to a kind of oil vapor treatment methods comprising following steps: primary separating step, and gas mixture is separated into primary liquid and primary gas liquid mixture；Primary gas liquid mixture is separated into secondary liquid and secondary gas liquid mixture by main body separating step；Secondary gas liquid mixture is separated into gas and final stage liquid using filter type by final stage separating step；Step is released, liquid and gas are released, wherein the liquid includes the primary liquid, the secondary liquid and the final stage liquid.Above-mentioned oil vapor treatment method releases after gas mixture can be divided into liquid and gas by using filter type and using classification separating step, has preferable oil gas separation, and widely applicable, application value is high.
Description
Technical field
The present invention relates to Oil-gas Separations, more particularly to oil vapor treatment method.
Background technique
Oil-gas Separation is to be blended with oily and gas gas mixture to separate, and is all very important in many fields
Technology, especially in Petroleum Production, the crude oil and associated natural gas that oil well production is come out are separated.
Therefore, how to optimize Oil-gas Separation, be the technical issues that need to address.
Summary of the invention
Based on this, it is necessary to provide a kind of oil vapor treatment method.
A kind of oil vapor treatment method comprising following steps: gas mixture is separated into primary liquid by primary separating step
Body and primary gas liquid mixture；Primary gas liquid mixture is separated into secondary liquid and secondary gas-liquid mixed by main body separating step
Body；Secondary gas liquid mixture is separated into gas and final stage liquid using filter type by final stage separating step；Step is released, is released
Liquid and gas out, wherein the liquid includes the primary liquid, the secondary liquid and the final stage liquid.
The filter type in one of the embodiments, is realized using filter device.
In one of the embodiments, in final stage separating step, using multistage filtering mode, secondary gas liquid mixture point
From at gas and final stage liquid.
The multistage filtering mode in one of the embodiments, is realized using filter device.
The filter device includes strainer in one of the embodiments,.
The filter device includes several stacked strainers in one of the embodiments,.
The filter device includes filter plate in one of the embodiments,.
The filter plate is vane type filter plate in one of the embodiments,.
The filter device includes several stacked filter plates in one of the embodiments,.
Each filter plate is staggeredly stacked in one of the embodiments,.
Above-mentioned oil vapor treatment method can be by gas mixture by using filter type and using classification separating step
It is released after being divided into liquid and gas, there is preferable oil gas separation, and widely applicable, application value is high.
Detailed description of the invention
Fig. 1 is the flow diagram of one embodiment of the invention.
Specific embodiment
In order to make the foregoing objectives, features and advantages of the present invention clearer and more comprehensible, with reference to the accompanying drawing to the present invention
Specific embodiment be described in detail.Many details are explained in the following description in order to fully understand this hair
It is bright.But the invention can be embodied in many other ways as described herein, those skilled in the art can be not
Similar improvement is done in the case where violating intension of the present invention, therefore the present invention is not limited by the specific embodiments disclosed below.
It should be noted that it can be directly another when element is referred to as " being fixed on " or " being set to " another element
On one element or there may also be elements placed in the middle.When an element is considered as " connection " another element, it can be with
It is directly to another element or may be simultaneously present centering elements.Term as used herein " vertically ", " level
", "left", "right" and similar statement for illustrative purposes only, be not meant to be the only embodiment.
Unless otherwise defined, all technical and scientific terms used herein and belong to technical field of the invention
The normally understood meaning of technical staff is identical.Term as used herein in the specification of the present invention is intended merely to description tool
The purpose of the embodiment of body, it is not intended that in the limitation present invention.Term as used herein "and/or" includes one or more
Any and all combinations of relevant listed item.
As shown in Figure 1, an example of the invention is a kind of oil vapor treatment method comprising following steps: primary separation
Gas mixture is separated into primary liquid and primary gas liquid mixture by step；Main body separating step, primary gas liquid mixture
It is separated into secondary liquid and secondary gas liquid mixture；Final stage separating step, using filter type, secondary gas liquid mixture separation
At gas and final stage liquid；Step is released, liquid and gas are released, wherein the liquid includes the primary liquid, described time
Grade liquid and the final stage liquid.Above-mentioned oil vapor treatment method can by using filter type and using classification separating step
It is released after gas mixture is divided into liquid and gas, there is preferable oil gas separation, and widely applicable, application value
It is high.
For example, a kind of oil vapor treatment method comprising following steps.For example, the oil vapor treatment method is using oil gas point
It is realized from device such as Oil-gas Separation tank body.
Primary separating step comprising gas mixture is separated into primary liquid and primary gas liquid mixture；That is, primary
Gas mixture the following steps are included: be separated into primary liquid and primary gas liquid mixture by separating step；The rest may be inferred.Example
Such as, gas mixture is separated by collision effect by primary liquid and primary gas liquid mixture；For another example, by gravity,
I.e. heavier substance flows down naturally under the effect of gravity, and gas mixture is separated into primary liquid and primary gas liquid mixture；
For another example, gas mixture is separated by cyclone mode by primary liquid and primary gas liquid mixture；For another example, using filter type
Gas mixture is separated into primary liquid and primary gas liquid mixture；For another example, under rotating environment, gas mixture is separated
At primary liquid and primary gas liquid mixture；For another example, under hyperbaric environment, gas mixture is separated into primary liquid and primary
Gas liquid mixture；For another example, at low ambient temperatures, gas mixture is separated into primary liquid and primary gas liquid mixture.
For example, under dissipating-heat environment, gas mixture is separated into primary liquid and primary in the primary separating step
Gas liquid mixture.For example, the dissipating-heat environment includes hot channel.For example, in gas and oil separating plant such as Oil-gas Separation tank body
The primary separating step of execution position at described for example described hot channel of dissipating-heat environment of setting etc..For example, the heat dissipating ring
Border further includes several sink bodies being arranged in outside hot channel.For example, end of the sink body far from hot channel
It interconnects, the outer tube structure with a large amount of holes is integrally formed.For example, the hot channel is provided with interlayer, it is primary
In separating step, the gas mixture is separated into primary liquid and primary gas liquid mixture from the interlayer.For example, the folder
Layer setting liquid collection opening and escape pipe are respectively used to output primary liquid and primary gas liquid mixture.For example, the interlayer is with outer
Expand shape end, the liquid collection opening is arranged in its underpart.For example, extending out shape end is truncated cone-shaped or horn shape.In this way, in first fraction
Certain cooling effect can be reached from step, be conducive to the security performance for improving Oil-gas Separation, and reduced intermolecular mutual
Function and effect are conducive to gas mixture is separated into primary liquid and primary gas liquid mixture and subsequent Oil-gas Separation.
Main body separating step comprising primary gas liquid mixture is separated into secondary liquid and secondary gas liquid mixture；Example
Such as, primary gas liquid mixture is separated by gravity by secondary liquid and secondary gas liquid mixture；For another example, by eddy flow side
Primary gas liquid mixture is separated into secondary liquid and secondary gas liquid mixture by formula；For another example, using filter type primary gas-liquid
Mixture is separated into secondary liquid and secondary gas liquid mixture；For another example, under rotating environment, primary gas liquid mixture is separated into
Secondary liquid and secondary gas liquid mixture；For another example, under hyperbaric environment, primary gas liquid mixture be separated into secondary liquid and time
Grade gas liquid mixture；For another example, at low ambient temperatures, primary gas liquid mixture is separated into secondary liquid and secondary gas-liquid mixed
Body.
For example, main body separating step, comprising the following steps: under rotating environment, primary gas liquid mixture is separated into secondary
Grade liquid and secondary gas liquid mixture；For example, in the rotating environment, in output port horizontal output primary gas liquid mixture.
Alternatively, in output port inclined output primary gas liquid mixture, the inclination port is inclined with upward in the rotating environment
Angle.For example, the inclination angle is 1 to 6 degree.Preferably, the tilt adjustable setting.In this way, it is different to be adapted to hydrocarbon content
Raw material is treated with a certain discrimination, so that having preferable section speed when output port exports primary gas liquid mixture, and in primary
When gas liquid mixture gas content is lower inclined output be conducive to be promoted a primary gas liquid mixture be separated into secondary liquid with
The effect of secondary gas liquid mixture.For example, the output port has semicircular output end face.For example, the output port
Output end face with round or ellipse；Alternatively, the output port has trapezoidal output end face；Alternatively, the output
Valve is arranged in port, for the output size of the output port to be arranged.For example, pressure sensing is arranged in the output port
Device connects the valve, for controlling the switch degree of the valve according to the pressure of primary gas liquid mixture to adjust
State the output size of output port.Primary gas-liquid mixed is exported in output port with adjustment in this way, can preferably control
The speed of body, so that control and promotion are separated into primary gas liquid mixture the effect of secondary liquid and secondary gas liquid mixture.
Further to promote separating effect, for another example, main body separating step is the following steps are included: at low ambient temperatures, at the beginning of
Grade gas liquid mixture is separated into secondary liquid and secondary gas liquid mixture；For example, the low temperature environment, including environment temperature are lower than
40 degrees Celsius.Preferably, the low temperature environment, including environment temperature are lower than 30 degrees Celsius.In low temperature environment, intermolecular work
With less, be conducive to gas mixture separation.For example, being realized by all or part of cooling to gas and oil separating plant described low
Warm environment.
Final stage separating step comprising secondary gas liquid mixture is separated into gas and final stage liquid；For example, using filtering
Secondary gas liquid mixture is separated into gas and final stage liquid by mode；For example, the filter type, is realized using filter device.
For example, secondary gas liquid mixture is separated into gas and final stage liquid by filter device in final stage separating step；Class according to this
It pushes away.For another example, secondary gas liquid mixture is separated by gravity by gas and final stage liquid；For another example, pass through cyclone mode handle
Secondary gas liquid mixture is separated into gas and final stage liquid；For another example, under rotating environment, secondary gas liquid mixture is separated into gas
Body and final stage liquid；For another example, at low ambient temperatures, secondary gas liquid mixture is separated into gas and final stage liquid；For another example, in height
Under pressure ring border, secondary gas liquid mixture is separated into gas and final stage liquid.
For example, using multistage filtering mode, secondary gas liquid mixture is separated into gas and final stage in final stage separating step
Liquid.For example, the multistage filtering mode, is realized using filter device.For example, the filter device includes strainer.Preferably,
The filter device includes several stacked strainers.And/or the filter device includes filter plate.Preferably, the filter plate is leaf
Chip filter plate.For example, the filter device includes several stacked filter plates.For example, each filter plate is staggeredly stacked.In this way, can
To obtain preferable filter effect, the collision of secondary gas liquid mixture and strainer or filter plate is increased, so that secondary gas-liquid mixed
Gas and final stage liquid separation degree in body is higher.For example, the filter device includes the stacked strainer of several layers, every layer of institute
It states strainer and is provided with several mesh units, and be provided with several strainer connection structures between adjacent layer strainer, each strainer
Connection structure is provided at least one mesh unit.For example, the mesh unit include it is several gang up with part and several bending members,
The part of ganging up with includes first ganging up with part and second and ganging up with part；Wherein, described first gangs up with part with helical structure, is similar to
Spring shape；Described second gangs up with part with rectilinear structure, and has turned around several circles, such as one in the rectilinear structure
Root itself turns around the line-like of several " Q " or " R " shape；For another example several circles are arranged in winding on a straight line；Also, institute
It states first and gangs up with part and described second and gang up with and connected between part by the bending member；For example, the bending member is butterfly, again
Such as, the bending member is butterfly grade separation bridge shape；For another example, the bending member is fold-line-shaped or the bending member is four circles
With the compound shape of " well " word, four circles are located at the four corners of " well " word.In this way, largely being touched with relatively firm
Micro-structure is hit, droplet collision probability can be further increased, so that secondary gas liquid mixture is separated into gas and final stage liquid
Better effect.For the ease of manufacturing, for another example, the mesh unit is integrally formed setting, i.e., each described to gang up with part and each institute
It states bending member and is integrally formed setting.
In order to obtain preferable oil gas separation, for example, main body separating step is the following steps are included: in hyperbaric environment
Under, primary gas liquid mixture is separated into secondary liquid and secondary gas liquid mixture, and so on；For example, the hyperbaric environment
Pressure be higher than 7MPa.For another example, the pressure of the hyperbaric environment is higher than 6MPa.For another example, the pressure of the hyperbaric environment is higher than
5MPa.For another example, the pressure of the hyperbaric environment is higher than 4MPa.For high pressure oil wells, pressure is often beyond 10MPa, i.e., 1,000
Ten thousand pas；Under hyperbaric environment, primary gas liquid mixture is separated into secondary liquid and secondary gas liquid mixture, is applicable not only to height
Pressure oil well is also applied for mesolow oil well；High pressure oil wells need to only be depressurized by equipment such as valve, for mesolow
Oil well can suitably be pumped into safe gas such as nitrogen or the primary gas liquid mixture of lasting input and control releases step and releases gas
The speed of body.On the basis of this embodiment, for example, in final stage separating step, under mesohigh environment, secondary gas-liquid
Mixture is separated into gas and final stage liquid.For example, the pressure of the mesohigh environment is higher than 1.5MPa.For example, the middle height
The pressure in pressure ring border is higher than 1.5MPa and is lower than 6MPa.For another example, the pressure of the mesohigh environment is higher than 1.5MPa and is lower than
5MPa.Such as, the pressure of the mesohigh environment is higher than 1.5MPa and is lower than 4MPa.
Release step comprising release liquid and gas, wherein the liquid includes the primary liquid, the secondary
Liquid and the final stage liquid.For example, releasing in step, before releasing liquid, the liquid is also passed through into stirring region；That is,
By the liquid by being released again after stirring region；For example, the top half setting of the stirring region is slowly stirred structure,
The lower half portion setting of the stirring region stands area, for example, passing through in the middle and lower part region and/or bottom section for standing area defeated
Structure releases liquid out；For example, the structure that is slowly stirred includes the rotary agitator paddle that revolving speed is lower than 5rpm, i.e. its revolving speed is small
In or be lower than 5 turns per minute, can be promoted in this way stirring remove gas remnants effect and avoid stirring when additionally introduce newly
Gas；Preferably, the rotary agitator paddle has several triangle through hole, and each triangle through hole edge extends
It is convexly equipped with triangular pyramid tongue, for cutting liquid in stirring to promote the effect that stirring removes gas remnants.For another example, described defeated
Structure includes output channel and its output control valve door out.In this way, it is possible to reduce the bubble or gas content in liquid released.
It is in order to realize that the oil in the liquid is separated from the water, it for another example, releases in step, classification releases liquid.For example,
It releases in step, liquid is released using gravity classification structure rating.In this way, can be by water-oil separating.For example, in the standing area
Liquid is released using gravity classification structure rating.For example, releasing portion by the first export structure in the middle and lower part region for standing area
Liquid separation body, and partially liq is released by the second export structure in the bottom section for standing area；Standing area has output knot
Structure, export structure include the first export structure and the second export structure, and the first export structure and/or the second export structure include
Output channel and its output control valve door；For example, oil is released by the first export structure in the middle and lower part region for standing area, and
Water is released by the second export structure in the bottom section for standing area.For another example, each export structure is equipped with unhurried current structure, uses
Whirlpool is avoided in unhurried current, for example, unhurried current structure is convex block, barrier and/or filter device etc..For example, the gravity classification structure
There are two liquid outlets of pre-determined distance including height.For example, the gravity classification structure further includes several unhurried current plates.For example,
Each unhurried current plate is not in contact with each other, and descends circulation road naturally to form liquid；For another example, projection of each unhurried current plate in bottom plane
At least partly it is overlapped；For example, each unhurried current plate is divided into two groups, the unhurried current plate in every group is arranged in parallel, the unhurried current in different groups
The extended line of plate is arranged in a crossed manner, and the projection at least portion of the bottom plane of each unhurried current plate device used by Oil-gas Separation
Divide and is overlapped.In this way, can achieve preferable oil-water separation.
For another example, it releases in step, using lift structure evolved gas.For example, the top of the Oil-gas Separation tank body is arranged
There is lift structure, the oil vapor treatment method is released in step, using lift structure evolved gas.For example, the rising knot
Structure includes ventilation tube body, for example, ventilation tube body is set to the top of the Oil-gas Separation tank body.For example, the lift structure is suitable
Sequence, which is equipped with, rises entrance, gas passage and air exit.For example, ventilation tube body is sequentially with and rises entrance, gas passage and row
Gas outlet, wherein the prominent Oil-gas Separation tank body of air exit.For example, the Oil-gas Separation tank body has inner cavity, above rise up into
Mouth is located at the inner cavity of the Oil-gas Separation tank body with gas passage, and air exit is located at the outside of the Oil-gas Separation tank body and leads to
It crosses gas passage and rises the inner cavity that entrance is connected to the Oil-gas Separation tank body；For another example, gas passage portion quartile is in the oil gas
It separates the inner cavity of tank body and part and is located at the outside of the Oil-gas Separation tank body.
For example, the rising entrance is in up-small and down-big horn shape；In this way, being conducive to pass through gas before releasing
Gravity is further separated out liquid therein.For another example, the rising entrance is funnel shaped.For another example, the rising entrance
In up big and down small horn shape；In this way, being conducive to collect the separation liquid to flow down from gas passage.For another example, it is risen up on described
Mouth is truncated conical shape；For example, the rising entrance is up big and down small truncated conical shape；In this way, being conducive to collect from gas passage
Dirty separation liquid.
For example, the lower edge for rising entrance is provided with unhurried current slot, the separating liquid for flowing down the lift structure
Body passes through unhurried current slot and the primary liquid, the secondary liquid, the final stage liquid pools.For example, the unhurried current slot has
Ring structure or funnel shaped structure, around the lower edge setting for rising entrance, so that flow down from gas passage
Separation liquid is unlikely to directly largely to fall.For example, the lower edge for rising entrance is additionally provided with several hanging nets, the unhurried current slot
The nettle being connected on each hanging net or each hanging net, so that the separation liquid that the lift structure flows down passes through unhurried current slot
And hanging net, it then falls and the primary liquid, the secondary liquid, the final stage liquid pools.Preferably, the hanging net is set
It is equipped with guide groove, the propensity to export of the guide groove is in the primary liquid or the secondary liquid position, so that the rising
The separation liquid that structure flows down falls into the primary liquid or the secondary liquid position, in this way, being conducive to make the final stage
Liquid regions are more gentle, to be conducive to later period separation and collect waste liquid and oil liquid.For example, the separation to flow down from gas passage
Liquid is flowed out from the unhurried current slot for rising entrance.
In order to which lift gas is further separated out the ability of liquid therein before releasing, for example, the gas passage
It is with spiral shape.For example, the gas passage has double screw shape；By using spiral-shaped or double screw shape, one
Aspect slows down the speed of gas, on the other hand increases molecular collision, is conducive to make drop to be easier from taking guttiferous gas
Separation forms separation liquid in body.For example, described spiral-shaped or double screw shape inner wall has several projective structures, to increase
Strong collision effect.Preferably, described spiral-shaped or double screw shape inner wall has several fin bodies, and each fin body
Groove downward is collectively formed, can preferably slow down the speed of gas in this way and increases collision, is also beneficial to separate
Lift structure described in liquid flows down.For example, being provided with radiator structure outside the gas passage.For example, the heat dissipation knot
Structure includes several extended heat radiation conduits and/or heat dissipation branch；For another example, the radiator structure includes several extended
Several heat dissipation branches of intersection are stretched on heat radiation conduit and heat radiation conduit；It is later to obtain better heat dissipation effect.For another example, the heat dissipation
Structure includes water-cooling heat radiating system.In this way, by effectively radiating, so that gas passage internal temperature is lower, to make drop
More easily from take in guttiferous gas coagulate, better gas-liquid separation effect can be reached.
For example, the air exit has one or more labyrinth type exhaust outlets, wherein the labyrinth type exhaust outlet also may be used
Referred to as be interconnected duct type exhaust outlet；Wherein, the labyrinth type exhaust outlet has several interconnected exhaust passages, each to arrange
Gas channel is interconnected, that is, each exhaust passage is connected with other one or more exhaust passages, so that the labyrinth type is arranged
The exhaust of gas in port is like to walk labyrinth, but each channel can walk out labyrinth, is particularly conducive to increase
Add collision and/or precession, to obtain preferable gas-liquid separation effect；For example, the air exit is vented with multiple labyrinth types
Mouthful, and each labyrinth type exhaust outlet is arranged in series, and forms series connection labyrinth type exhaust outlet queue；For example, the labyrinth type exhaust
Mouth includes one and enters gas outlet, an outlet outlet and multiple interconnected exhaust passages, each exhaust passage
Respectively with it is described enter gas outlet, the outlet outlet be connected to.In series connection labyrinth type exhaust outlet queue, in addition to the labyrinth of end
Except formula exhaust outlet, the outlet outlet for entering gas outlet and connecting another labyrinth type exhaust outlet of each labyrinth type exhaust outlet.It is excellent
Choosing, each roughly vertical setting of exhaust passage in the labyrinth type exhaust outlet, for example, each exhaust passage
The angle of each Duan Junyu vertical line is less than 20 degree；In this way, the drop for being conducive to collect by gravity in gas flows down naturally.
Preferably, the gas outlet that enters of each labyrinth type exhaust outlet is vertically arranged, for collecting the drop in gas and sequentially passing through
Gas passage and rising entrance, with the primary liquid, the secondary liquid, the final stage liquid pools.In this way, using labyrinth
Formula exhaust outlet is conducive to collect the drop in gas as much as possible.Further, heat sink clip is arranged in the labyrinth type exhaust outlet
Layer, wherein being equipped with radiator liquid, the heat radiation sandwich layer does not connect mutually with each exhaust passage in the labyrinth type exhaust outlet
It is logical, cool down for the convection action by radiator liquid to each exhaust passage, so that gas is further separated out it
In liquid, obtain better oil gas separation.
For example, the air exit is equipped with exhaust screen.For example, the labyrinth type exhaust outlet is equipped with the exhaust screen.
For another example, the outlet outlet of the labyrinth type exhaust outlet is equipped with the exhaust screen.It, can be into one by the setting of exhaust screen
Step increases droplet collision probability, preferably isolates the remaining droplet in gas.For another example, each labyrinth type exhaust outlet series connection
Setting forms series connection labyrinth type exhaust outlet queue, is equipped in the outlet outlet of the labyrinth type exhaust outlet of the queue end described
Exhaust screen.And/or the air exit is equipped with exhaust pipe and air discharge duct, the exhaust pipe is passed through in the air discharge duct, is used for
By air discharge duct evolved gas, in order to collect.For example, air discharge duct is provided with partial pressure gas collecting equipment.In this way, can achieve preferably
Safety exhaust and collecting effect.
It should be noted that other embodiments of the invention further include, the mutually group of the technical characteristic in the various embodiments described above
Close the oil vapor treatment method that is formed by, can implement, also known as oil and gas separation method or oil gas hierarchical processing method.
Each technical characteristic of embodiment described above can be combined arbitrarily, for simplicity of description, not to above-mentioned reality
It applies all possible combination of each technical characteristic in example to be all described, as long as however, the combination of these technical characteristics is not deposited
In contradiction, all should be considered as described in this specification.
The embodiments described above only express several embodiments of the present invention, and the description thereof is more specific and detailed, but simultaneously
It cannot therefore be construed as limiting the scope of the patent.It should be pointed out that coming for those of ordinary skill in the art
It says, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to protection of the invention
Range.Therefore, the scope of protection of the patent of the invention shall be subject to the appended claims.
Claims (10)
1. a kind of oil vapor treatment method, which comprises the following steps:
Gas mixture is separated into primary liquid and primary gas liquid mixture by primary separating step；
Primary gas liquid mixture is separated into secondary liquid and secondary gas liquid mixture by main body separating step；
Secondary gas liquid mixture is separated into gas and final stage liquid using filter type by final stage separating step；
Release step, release liquid and gas, wherein the liquid include the primary liquid, the secondary liquid with it is described
Final stage liquid；
It releases in step, liquid is released using gravity classification structure rating；
It releases in step, using lift structure evolved gas, the lift structure, which is sequentially with, rises entrance, gas passage and row
Gas outlet；
The lower edge for rising entrance is provided with unhurried current slot, and the lower edge for rising entrance is additionally provided with several hanging nets, described slow
Chute is connected to the nettle on each hanging net or each hanging net, so that the separation liquid that the lift structure flows down is by delaying
Then chute and hanging net are fallen and the primary liquid, the secondary liquid, the final stage liquid pools；
The hanging net is provided with guide groove, and the propensity to export of the guide groove is in the primary liquid or the secondary liquid position
It sets, so that the separation liquid that the lift structure flows down falls into the primary liquid or the secondary liquid position；
The gas passage is with spiral shape；
The air exit has multiple interconnected duct type exhaust outlets, and each interconnected duct type exhaust outlet series connection is set
It sets, forms the duct type exhaust outlet queue that is interconnected of connecting；The interconnected duct type exhaust outlet has several be interconnected
Exhaust passage, each exhaust passage is connected with other one or more exhaust passages；The interconnected duct type exhaust
Mouth includes one and enters gas outlet, an outlet outlet and multiple interconnected exhaust passages, each exhaust passage
Respectively with it is described enter gas outlet, the outlet outlet be connected to；The phase of the interconnected duct type exhaust outlet queue end of series connection
The outlet outlet of intercommunicated duct type exhaust outlet is equipped with exhaust screen；
Heat radiation sandwich layer is arranged in the interconnected duct type exhaust outlet, wherein it is equipped with radiator liquid, the heat radiation sandwich layer and institute
Each exhaust passage stated in interconnected duct type exhaust outlet is not connected to mutually.
2. oil vapor treatment method according to claim 1, which is characterized in that the filter type is realized using filter device.
3. oil vapor treatment method according to claim 1, which is characterized in that in final stage separating step, using multistage filtering side
Secondary gas liquid mixture is separated into gas and final stage liquid by formula.
4. oil vapor treatment method according to claim 3, which is characterized in that the multistage filtering mode, using filter device
It realizes.
5. according to the oil vapor treatment method of claim 2 or 4, which is characterized in that the filter device includes strainer.
6. oil vapor treatment method according to claim 5, which is characterized in that the filter device includes several stacked filters
Net.
7. according to the oil vapor treatment method of claim 2 or 4, which is characterized in that the filter device includes filter plate.
8. oil vapor treatment method according to claim 7, which is characterized in that the filter plate is vane type filter plate.
9. oil vapor treatment method according to claim 7, which is characterized in that the filter device includes several stacked filters
Plate.
10. oil vapor treatment method according to claim 9, which is characterized in that each filter plate is staggeredly stacked.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610769425.8A CN106368669B (en) | 2016-08-30 | 2016-08-30 | Oil vapor treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610769425.8A CN106368669B (en) | 2016-08-30 | 2016-08-30 | Oil vapor treatment method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106368669A CN106368669A (en) | 2017-02-01 |
| CN106368669B true CN106368669B (en) | 2019-08-02 |
Family
ID=57901680
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610769425.8A Active CN106368669B (en) | 2016-08-30 | 2016-08-30 | Oil vapor treatment method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106368669B (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102575677A (en) * | 2009-09-09 | 2012-07-11 | 英格索尔-兰德公司 | Multi-Stage Oil Separation System Including A Cyclonic Separation Stage |
| CN202555095U (en) * | 2012-05-28 | 2012-11-28 | 山东国舜建设集团有限公司 | Reversed and interlaced spiral rising device for direct discharge flue gas |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL1029230C2 (en) * | 2005-06-10 | 2006-12-12 | Fmc Technologies Cv | System and inlet device for separating a mixture. |
| CN201586443U (en) * | 2009-11-30 | 2010-09-22 | 北京北分麦哈克分析仪器有限公司 | Cyclone separation filter |
| CN202417464U (en) * | 2011-12-14 | 2012-09-05 | 扬州利达科技有限公司 | Oil-gas separation automatic control device |
| CN105233575B (en) * | 2015-10-14 | 2017-10-27 | 中国科学院广州能源研究所 | MVR system gas-liquid separation devices |
-
2016
- 2016-08-30 CN CN201610769425.8A patent/CN106368669B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102575677A (en) * | 2009-09-09 | 2012-07-11 | 英格索尔-兰德公司 | Multi-Stage Oil Separation System Including A Cyclonic Separation Stage |
| CN202555095U (en) * | 2012-05-28 | 2012-11-28 | 山东国舜建设集团有限公司 | Reversed and interlaced spiral rising device for direct discharge flue gas |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106368669A (en) | 2017-02-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5555160B2 (en) | Separator tank | |
| CN106215534B (en) | Multistage oil gas partition method | |
| CN106368670B (en) | Oil-gas Separation pressure application | |
| CN102671502A (en) | Gas-liquid inertia separation and distribution coupling unit and separator adopting same | |
| CN106434304A (en) | Micro-device capable of removing low-temperature cell protective agent | |
| CN106368669B (en) | Oil vapor treatment method | |
| CN106215536B (en) | Rotate oil and gas separation method | |
| CN106321058B (en) | Oil gas cold treatment method | |
| BR112018002309B1 (en) | IMMERSION EXTRACTOR AND METHOD | |
| US20160008752A1 (en) | Vertical gas/liquid phase separator | |
| CN106085832A (en) | A kind of circulating tumor cell automatic separation system | |
| US9744489B2 (en) | Phase separator using pressure differential | |
| CN206545504U (en) | A kind of multistage natural gas gas-liquid separation device under water | |
| CN105999839A (en) | Oil-liquid separation and recovery treatment system for processing center | |
| CN107050931B (en) | Gas-liquid multistage separation device for pump inflow gas-containing experiment | |
| CN202070491U (en) | Chaff and rice separator | |
| CN206304484U (en) | A kind of gas collector and delivery pipe filter net type desander | |
| NO861183L (en) | METHOD EXTRACTION METHOD AND APPARATUS. | |
| CN106659997A (en) | Interaction chambers with reduced cavitation | |
| González-Esparza et al. | Design and modeling of a microfluidic device with potential application for isolation of circulating tumor cells | |
| US9434790B2 (en) | Process for the extraction of wood | |
| CN207324177U (en) | A kind of combined inclined plate sedimentation pond | |
| US1693849A (en) | Oil and gas separator | |
| CN207406299U (en) | A kind of mud purification desanding circulator of flat-bottomed boat | |
| CN205048821U (en) | Efficient multicavity oil separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20190703 Address after: 321200 No. 67, Matsu Hill Road, Wuyi County, Jinhua, Zhejiang. Applicant after: Jin Miaoying Address before: 516000 Huizhou County, Guangdong province Boluo county Luo Yang nine Village neighborhood committee B trust garden two phase Applicant before: Huizhou City Curtis Technology Co. Ltd. |
|
| TA01 | Transfer of patent application right | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201201 Address after: The first room from the north of 4th floor, No.47 qiaoganglang, Liangqiao village, Weitang street, Jiashan County, Jiashan City, Zhejiang Province Patentee after: Jiashan Xianming New Material Co., Ltd Address before: 321200 No. 67 Shuxi North Road, Hushan Street, Wuyi County, Jinhua City, Zhejiang Province Patentee before: Jin Miaoying |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201214 Address after: No.84 Fuqian Road, Chengbei Park, Jingjiang Economic and Technological Development Zone, Taizhou City, Jiangsu Province, 214500 Patentee after: Jiangsu Qingrun solid waste disposal Co., Ltd Address before: The first room from the north of 4th floor, No.47 qiaoganglang, Liangqiao village, Weitang street, Jiashan County, Jiashan City, Zhejiang Province Patentee before: Jiashan Xianming New Material Co., Ltd |
|
| TR01 | Transfer of patent right |