CN208279571U - A kind of viscous crude defoaming separator - Google Patents
A kind of viscous crude defoaming separator Download PDFInfo
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- CN208279571U CN208279571U CN201820747180.3U CN201820747180U CN208279571U CN 208279571 U CN208279571 U CN 208279571U CN 201820747180 U CN201820747180 U CN 201820747180U CN 208279571 U CN208279571 U CN 208279571U
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Abstract
The utility model discloses a kind of viscous crude to defoam separator, and in an implementation mode, which may include shell, Y type vane type liquid knockout, eddy flow pre-separation component, brokenly bubble component, the first brokenly bubble hole board group, the second brokenly bubble hole board group.The separator optimizes separator size from structure design, to achieve the effect that reduce cost and realize efficiently defoaming, separation.Conventional Gravity Separation mode is changed, efficient pre-separation component is increased in separator interior, defoams component, first separation component, secondary separation component.These components utilize fluid mechanics principle to realize defoaming, separation using mechanical forced separated structure.Bubble can be efficiently abolished, oil is realized, gas, efficiently separates.Conventional way is changed on cyclone separator arrangement, and using vertical structure, the volume of separator is greatly reduced compared with typical separators.And vertical structure also significantly reduces the occupied area of yard, while also reducing the construction cost of civil engineering.
Description
Technical field
The utility model relates to viscous crude defoaming equipment technical fields, defoam separator more particularly to a kind of viscous crude.
Background technique
Viscous crude is had in recovery process much at nuclei air bubble, and the bubble of these nucleation separates the oil of viscous crude, gas and water
Sizable difficulty is caused, the separating effect of viscous crude is influenced.Viscous crude defoaming is the difficult point of viscous crude separation, is all difficult to all the time
To good solution.
The separation principle of typical separators: sedimentation theory is utilized, by the filtering of separation assembly, in the residence time one
In the case where fixed, foam is isolated in separation assembly side, viscous crude is brought out from another, due to the extraction technique of viscous crude, in viscous crude
Can not be eliminated at nuclei air bubble, still containing many bubbles in the crude oil after causing separation, can not completely remove, to influence
The measuring accuracy of viscous crude flowmeter, causes economic loss.Meanwhile viscous crude separator conventional at present, most of is Gravity Separation,
Using the residence time of viscous crude, sedimentation time and increase Oil-gas Separation component, to realize the separation of oil, gas, can not preferably divide
From bubbles viscous crude.Conventional viscous crude separator is usually horizontal type structure simultaneously and volume is larger.
Utility model content
The utility model provides a kind of viscous crude defoaming separator.
The utility model provides following scheme:
A kind of viscous crude defoaming separator, comprising:
Shell, the shell from top to bottom successively include gas outlet, inlet and liquid outlet；
Y type vane type liquid knockout, the Y type vane type liquid knockout are located at the enclosure interior and are connected with its top；Institute
State Y type vane type liquid knockout for will enter its internal gas entrainment drop removal and by the gas for removing drop guide to
The gas outlet；
Eddy flow pre-separation component, the eddy flow pre-separation component are located at Y type vane type liquid knockout lower part；The eddy flow
Pre-separation component is connected by pipeline with the inlet；The eddy flow pre-separation component by the inlet for that will be entered
Its internal material becomes circular motion from moving along a straight line, so that the nucleation bubble destruction in material is completed first time gas-liquid point
From；
Brokenly bubble component, the brokenly bubble component are located at the eddy flow pre-separation component lower part, and the brokenly bubble component will be for that will connect
The material for completing first time gas-liquid separation by the eddy flow pre-separation component received carries out brokenly bubble processing and completes second of gas
Liquid separation；
First brokenly bubble hole board group, first brokenly bubble hole board group are located at below the brokenly bubble component and lateral along the shell
Leveling, which is covered with, is set to the enclosure interior；First brokenly bubble hole board group be used to receive by the brokenly bubble component the
The material of secondary gas-liquid separation, which carries out droplet settling, makes gas stay in upper layer；
Second brokenly bubble hole board group, second brokenly bubble hole board group are located at below the board group of first brokenly bubble hole and along the shell
Body transverse direction leveling, which is covered with, is set to the enclosure interior；Second brokenly bubble hole board group is for removing the sedimentation of the first brokenly bubble hole board group
Drop in gas.
Preferred: the inlet end of the Y type vane type liquid knockout is connected with the enclosure interior space, the Y type blade
The outlet side of formula liquid knockout is located in the independent outlet chamber formed by partition；It is led with the independent outlet chamber gas outlet
It is logical.
Preferred: the eddy flow pre-separation component includes the first tubular body being fixedly linked and the first cone body；
The first tubular body side wall offers tangential inlet, and top is connected with outlet pipe；It opens first cone body lower part
Equipped with the first liquid outlet；Wherein, the pipeline is connected with the tangential inlet.
Preferred: the brokenly bubble component includes the second tubular body being fixedly linked and the second cone body；Described
Two taper body upper surfaces are provided with first band and puncture bubble plate；Second cone body, which is connected on bracket described in bracket, to be arranged
There is the second barbed brokenly bubble plate.
Preferred: first brokenly bubble hole board group includes the first orifice plate of multiple-layer stacked；According to one on first orifice plate
Fixed distance is uniformly provided with multiple first through hole；First through hole interlaced arrangement between every layer of first orifice plate.
Preferred: second brokenly bubble hole board group includes the second orifice plate of multiple-layer stacked；According to one on second orifice plate
Fixed distance is uniformly provided with multiple second through-holes；Between every layer of second orifice plate and through-hole interlaced arrangement.
It is preferred: to offer the first liquid level between the inlet and first brokenly bubble hole board group on the shell
Count mouth.
It is preferred: to be located at second brokenly bubble hole board group lower part on the shell and offer second liquid level gauge mouth.
It is preferred: to be connected with sewage draining exit at the liquid outlet.
According to specific embodiment provided by the utility model, the utility model discloses following technical effects:
By the utility model, a kind of viscous crude defoaming separator may be implemented, in an implementation mode, which can
To include shell, the shell from top to bottom successively includes gas outlet, inlet and liquid outlet；Y type vane type liquid knockout, institute
Y type vane type liquid knockout is stated to be located at the enclosure interior and be connected with its top；The Y type vane type liquid knockout will be for that will enter
The drop of its internal gas entrainment removes and guides the gas for removing drop to the gas outlet；Eddy flow pre-separation component,
The eddy flow pre-separation component is located at Y type vane type liquid knockout lower part；The eddy flow pre-separation component passes through pipeline and institute
Inlet is stated to be connected；The eddy flow pre-separation component is used to that its internal material will to be entered by moving along a straight line by the inlet
Become circular motion, so that the nucleation bubble destruction in material is completed first time gas-liquid separation；Brokenly bubble component, the brokenly bubble group
Part is located at the eddy flow pre-separation component lower part, and the brokenly bubble component will be for that will receive through the eddy flow pre-separation component
The material for completing first time gas-liquid separation carries out brokenly bubble processing and completes second of gas-liquid separation；First brokenly bubble hole board group, described
One brokenly bubble hole board group, which is located at below the brokenly bubble component and is covered with along the shell transverse direction leveling, is set to the enclosure interior；Institute
The first brokenly bubble hole board group is stated to sink for the material by second of gas-liquid separation of brokenly bubble component received to be carried out drop
Drop makes gas stay in upper layer；Second brokenly bubble hole board group, second brokenly bubble hole board group are located at below the board group of first brokenly bubble hole
And it is covered with along the shell transverse direction leveling and is set to the enclosure interior；Second brokenly bubble hole board group is for removing the first brokenly bubble
Gas in the drop of hole board group sedimentation.Viscous crude provided by the present application defoams separator, optimizes separator from structure design
Size, to achieve the effect that reduce cost and realize efficiently defoaming, separation.Conventional Gravity Separation mode is changed, in separator
Inside increases efficient pre-separation component, defoams component, first separation component, secondary separation component.These components utilize
Fluid mechanics principle realizes defoaming, separation using mechanical forced separated structure.Viscous crude defoaming separator can be abolished efficiently
Bubble realizes oil, gas, efficiently separates.Conventional way is changed on cyclone separator arrangement, using vertical structure, with conventional point
The volume for greatly reducing separator is compared from device.And vertical structure also significantly reduces the occupied area of yard, while
Reduce the construction cost of civil engineering.
Certainly, any product for implementing the utility model does not necessarily require achieving all the advantages described above at the same time.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Needed in attached drawing be briefly described, it should be apparent that, the accompanying drawings in the following description is only the utility model
Some embodiments for those of ordinary skill in the art without creative efforts, can also be according to this
A little attached drawings obtain other attached drawings.
Fig. 1 is a kind of structural schematic diagram of viscous crude defoaming separator provided by the embodiment of the utility model.
In figure: shell 1, gas outlet 101, inlet 102, liquid outlet 103, first liquid level gauge mouth 104, second liquid level gauge mouth
105, sewage draining exit 106, Y type vane type liquid knockout 2, eddy flow pre-separation component 3, brokenly bubble component 4, first band puncture bubble plate 401, the
Two barbed brokenly bubble plates 402, the first brokenly bubble hole board group 5, the second brokenly bubble hole board group 6.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art's every other embodiment obtained, all belongs to
In the range of the utility model protection.
Embodiment
It is that a kind of viscous crude provided by the embodiment of the utility model defoams separator, as shown in Figure 1, the separator referring to Fig. 1
Including shell 1, the shell 1 from top to bottom successively includes gas outlet 101, inlet 102 and liquid outlet 103；
Y type vane type liquid knockout 2, the Y type vane type liquid knockout 2 are located at 1 inside of shell and are connected with its top；
The Y type vane type liquid knockout 2 is used to remove the drop for entering its internal gas entrainment and draw the gas for removing drop
It is directed at the gas outlet；The inlet end of the Y type vane type liquid knockout 2 is connected with the enclosure interior space, the Y type blade
The outlet side of formula liquid knockout is located in the independent outlet chamber formed by partition；The gas outlet 101 and the independent outlet
Chamber conducting.
Eddy flow pre-separation component 3, the eddy flow pre-separation component 3 are located at 2 lower part of Y type vane type liquid knockout；It is described
Eddy flow pre-separation component 3 is connected by pipeline with the inlet 102；The eddy flow pre-separation component 3 is used for will be by described
Inlet, which enters its internal material, becomes circular motion from moving along a straight line, so that the nucleation bubble destruction in material is completed the
Gas-liquid separation；The eddy flow pre-separation component 3 includes the first tubular body being fixedly linked and the first cone body；Institute
It states the first tubular body side wall and offers tangential inlet, top is connected with outlet pipe；First cone body lower part opens up
There is the first liquid outlet；Wherein, the pipeline is connected with the tangential inlet.
Brokenly bubble component 4, the brokenly bubble component 4 are located at 3 lower part of eddy flow pre-separation component, and the brokenly bubble component 4 is used for
The material for completing first time gas-liquid separation by the eddy flow pre-separation component 3 received is subjected to brokenly bubble processing and completes second
Secondary gas-liquid separation；The brokenly bubble component 4 includes the second tubular body being fixedly linked and the second cone body；Second cone
Shape body upper surface is provided with first band and punctures bubble plate 401；Second cone body, which is connected on bracket described in bracket, to be arranged
There is the second barbed brokenly bubble plate 402.
First brokenly bubble hole board group 5, first brokenly bubble hole board group 5 are located at 4 lower section of brokenly bubble component and along the shells
Lateral leveling, which is covered with, to be set to inside the shell 1；First brokenly bubble hole board group 5 will be for that will receive through the brokenly bubble
The material of second of gas-liquid separation of component, which carries out droplet settling, makes gas stay in upper layer；First brokenly bubble hole board group includes multilayer
First orifice plate of superposition；Multiple first through hole are uniformly provided with according to a certain distance on first orifice plate；Every layer of first hole
First through hole interlaced arrangement between plate.
Second brokenly bubble hole board group 6, second brokenly bubble hole board group 6 are located at first brokenly bubble hole board group, 5 lower section and along institutes
It states the lateral leveling of shell 1 and is covered with and be set to the enclosure interior；Second brokenly bubble hole board group 6 is for removing the first brokenly bubble orifice plate
Gas in the drop of group sedimentation.Second brokenly bubble hole board group includes the second orifice plate of multiple-layer stacked；On second orifice plate
Multiple second through-holes are uniformly provided with according to a certain distance；Between every layer of second orifice plate and through-hole interlaced arrangement.
Further, it is offered between the inlet 102 and first brokenly bubble hole board group 3 on the shell 1
First liquid level gauge mouth 104.It is located at described second brokenly bubble orifice plate, 6 groups of lower parts on the shell 1 and offers second liquid level gauge mouth 105.
Sewage draining exit 106 is connected at the liquid outlet 103.
The separation principle of separator provided by the present application are as follows:
1, eddy flow pre-separation part
Bubbles viscous crude (hereinafter referred to as material) enters eddy flow component by gas-liquid import with certain speed, and material is by straight line
Movement becomes circular motion, and the overwhelming majority for rotating material is twist flowed downwardly toward cone along wall.At nuclei air bubble from
Under the action of mental and physical efforts, be thrown toward wall, in collision process, be destroyed at nuclei air bubble and be separated into gas and drop, drop with
Wall contact, just loses inertia force, and the momentum of the speed axially downwards near wall falls along wall surface, flows to brokenly bubble component.
The outer rotational gas flow for rotating decline constantly flows into the central part of separator during decline, forms centripetal radial air flow,
This fraction, which just constitutes, rotates upward inward eddy.Eddy flow pre-separation component is discharged.
2, brokenly bubble component
Since air bubble content is more in viscous crude, eddy flow pre-separation component can only tentatively be broken to nuclei air bubble, in eddy flow process
In there are still not in contact with eddy flow wall at nuclei air bubble.Need brokenly bubble component that will further puncture at nuclei air bubble at this time, thus
Realize gas-liquid separation.
The structure of brokenly bubble component is hangnail pattern, and the size and arrangement of hangnail are summarized by various test datas
A set of optimal mechanism size layout out.Bubble can be efficiently abolished, realizes gas-liquid separation.
3, level-one brokenly bubble orifice plate (purpose: by droplet settling, gas stays in upper layer)
The hardened structure of level-one brokenly bubble is the orifice plate of multiple-layer stacked, and hole is uniformly distributed according to a fixed spacing certain size, between every laminate
Hole interlaced arrangement.So that material is staggeredly fallen at a slow speed, to increase the residence time of material, the gas in material can be made to fill
Divide discharge.And orifice plate can effectively stop omit be not punctured at nuclei air bubble enter separation after material in.
4, second level brokenly bubble orifice plate (purpose: gas in removal liquid rises the gas in liquid from gas vent and is discharged)
The structure of second level brokenly bubble orifice plate is similar with level-one brokenly bubble orifice plate, only different according to effect, the spacing in hole and aperture
It is different from level-one brokenly bubble orifice plate.
5, Y type vane type liquid knockout
The purpose of Y type blade liquid knockout: the drop carried secretly in gas is effectively removed.
For Y type blade liquid knockout compared with common blade, Y type blade liquid storage device makes gas in the circulation process, constantly changes
The flow direction of gas, makes gas and plate collides condensation, the partial drop carried secretly in removing gas.
Table 1 is the Structure Comparison of typical separators and separator provided by the present application
Table 2 be same environment, with operating condition in the case where separator size and separation effect comparison
| Reduced parameter | Typical separators | New Type of Separator | Remarks |
| Diameter | 1.5D | D | |
| Length | 1.5L | L | |
| Separating effect | De-bubble rate in viscous crude: 70% | De-bubble rate in viscous crude: 98% |
In short, viscous crude provided by the present application defoams separator, separator size is optimized from structure design, to reach drop
Low cost simultaneously realizes the effect for efficiently defoaming, separating.Conventional Gravity Separation mode is changed, is increased efficiently in separator interior
Pre-separation component, defoam component, first separation component, secondary separation component.These components are adopted using fluid mechanics principle
Defoaming, separation are realized with mechanical forced separated structure.The viscous crude defoaming separator can efficiently abolish bubble, realize oil, gas,
Efficiently separate.Conventional way is changed on cyclone separator arrangement, using vertical structure, is substantially reduced compared with typical separators
The volume of separator.And vertical structure also significantly reduces the occupied area of yard, while also reducing the construction of civil engineering
Cost.
It should be noted that, in this document, relational terms such as first and second and the like are used merely to a reality
Body or operation are distinguished with another entity or operation, are deposited without necessarily requiring or implying between these entities or operation
In any actual relationship or order or sequence.Moreover, the terms "include", "comprise" or its any other variant are intended to
Non-exclusive inclusion, so that the process, method, article or equipment including a series of elements is not only wanted including those
Element, but also including other elements that are not explicitly listed, or further include for this process, method, article or equipment
Intrinsic element.In the absence of more restrictions, the element limited by sentence "including a ...", it is not excluded that
There is also other identical elements in process, method, article or equipment including the element.
The above is only the preferred embodiment of the utility model only, is not intended to limit the protection model of the utility model
It encloses.Any modification, equivalent substitution, improvement and etc. made within the spirit and principle of the present invention, are all contained in this reality
With in novel protection scope.
Claims (9)
1. a kind of viscous crude defoams separator characterized by comprising shell, the shell from top to bottom successively include gas outlet,
Inlet and liquid outlet；Y type vane type liquid knockout, the Y type vane type liquid knockout are located at the enclosure interior and push up with it
Portion is connected；The Y type vane type liquid knockout is used to remove the drop for entering its internal gas entrainment and will remove drop
Gas is guided to the gas outlet；Eddy flow pre-separation component, the eddy flow pre-separation component are located at the Y type vane type liquid knockout
Lower part；The eddy flow pre-separation component is connected by pipeline with the inlet；The eddy flow pre-separation component will be for that will pass through
The inlet, which enters its internal material, becomes circular motion from moving along a straight line, so that the nucleation bubble destruction in material is complete
At first time gas-liquid separation；Brokenly bubble component, the brokenly bubble component are located at the eddy flow pre-separation component lower part, the brokenly bubble component
The material for completing first time gas-liquid separation by the eddy flow pre-separation component for that will receive carries out brokenly bubble processing and completes
Second of gas-liquid separation；First brokenly bubble hole board group, first brokenly bubble hole board group are located at below the brokenly bubble component and along described
Shell transverse direction leveling, which is covered with, is set to the enclosure interior；What first brokenly bubble hole board group was used to receive is broken by described
The material of bubble second of gas-liquid separation of component, which carries out droplet settling, makes gas stay in upper layer；Second brokenly bubble hole board group, described second
Brokenly bubble hole board group, which is located at below the board group of first brokenly bubble hole and is covered with along the shell transverse direction leveling, to be set in the shell
Portion；Second brokenly bubble hole board group is used to remove the gas in the drop of the first brokenly bubble hole board group sedimentation.
2. viscous crude according to claim 1 defoams separator, which is characterized in that the air inlet of the Y type vane type liquid knockout
End is connected with the enclosure interior space, and the outlet side of the Y type vane type liquid knockout is located at independently to go out by what partition was formed
In air cavity；The gas outlet is connected with the independent outlet chamber.
3. viscous crude according to claim 1 defoams separator, which is characterized in that the eddy flow pre-separation component includes fixing
Connected the first tubular body and the first cone body；The first tubular body side wall offers tangential inlet, and top connects
It is connected to outlet pipe；First cone body lower part offers the first liquid outlet；Wherein, the pipeline tangentially enters with described
Mouth is connected.
4. viscous crude according to claim 1 defoams separator, which is characterized in that the brokenly bubble component includes being fixedly linked
Second tubular body and the second cone body；Second cone body upper surface is provided with first band and punctures bubble plate；It is described
Second cone body, which is connected on bracket described in bracket, is provided with the second barbed brokenly bubble plate.
5. viscous crude according to claim 1 defoams separator, which is characterized in that first brokenly bubble hole board group includes multilayer
First orifice plate of superposition；Multiple first through hole are uniformly provided with according to a certain distance on first orifice plate；Every layer of first hole
First through hole interlaced arrangement between plate.
6. viscous crude according to claim 1 defoams separator, which is characterized in that second brokenly bubble hole board group includes multilayer
Second orifice plate of superposition；Multiple second through-holes are uniformly provided with according to a certain distance on second orifice plate；Every layer of second hole
Between plate and through-hole interlaced arrangement.
7. defoaming separator to viscous crude described in 6 any one according to claim 1, which is characterized in that be located on the shell
First liquid level gauge mouth is offered between the inlet and first brokenly bubble hole board group.
8. defoaming separator to viscous crude described in 6 any one according to claim 1, which is characterized in that be located on the shell
Second brokenly bubble hole board group lower part offers second liquid level gauge mouth.
9. defoaming separator to viscous crude described in 6 any one according to claim 1, which is characterized in that connect at the liquid outlet
It is connected to sewage draining exit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820747180.3U CN208279571U (en) | 2018-05-18 | 2018-05-18 | A kind of viscous crude defoaming separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820747180.3U CN208279571U (en) | 2018-05-18 | 2018-05-18 | A kind of viscous crude defoaming separator |
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| Publication Number | Publication Date |
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| CN208279571U true CN208279571U (en) | 2018-12-25 |
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| CN201820747180.3U Active CN208279571U (en) | 2018-05-18 | 2018-05-18 | A kind of viscous crude defoaming separator |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111089282A (en) * | 2019-12-31 | 2020-05-01 | 广东美的厨房电器制造有限公司 | Steam generator of household appliance, control method thereof and steam oven |
| CN111389055A (en) * | 2020-04-03 | 2020-07-10 | 武汉理工大学 | Fire fighting equipment for oil on-line monitoring system |
| CN111841085A (en) * | 2020-07-23 | 2020-10-30 | 招商局金陵船舶(威海)有限公司 | Water wheel centrifugal defoaming device |
| WO2021088828A1 (en) * | 2019-11-04 | 2021-05-14 | 中国石油大学(华东) | Co 2 flooding produced fluid gas-liquid separation apparatus |
| CN113261851A (en) * | 2020-02-14 | 2021-08-17 | 佛山市顺德区美的电热电器制造有限公司 | Bubble breaking structure, pot cover assembly and cooking utensil |
| CN113996090A (en) * | 2021-09-24 | 2022-02-01 | 深圳市卓宝科技股份有限公司 | Method for eliminating bubbles in asphalt sizing material |
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2018
- 2018-05-18 CN CN201820747180.3U patent/CN208279571U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021088828A1 (en) * | 2019-11-04 | 2021-05-14 | 中国石油大学(华东) | Co 2 flooding produced fluid gas-liquid separation apparatus |
| CN111089282A (en) * | 2019-12-31 | 2020-05-01 | 广东美的厨房电器制造有限公司 | Steam generator of household appliance, control method thereof and steam oven |
| CN113261851A (en) * | 2020-02-14 | 2021-08-17 | 佛山市顺德区美的电热电器制造有限公司 | Bubble breaking structure, pot cover assembly and cooking utensil |
| CN111389055A (en) * | 2020-04-03 | 2020-07-10 | 武汉理工大学 | Fire fighting equipment for oil on-line monitoring system |
| CN111841085A (en) * | 2020-07-23 | 2020-10-30 | 招商局金陵船舶(威海)有限公司 | Water wheel centrifugal defoaming device |
| CN111841085B (en) * | 2020-07-23 | 2022-04-19 | 招商局金陵船舶(威海)有限公司 | Water wheel centrifugal defoaming device |
| CN113996090A (en) * | 2021-09-24 | 2022-02-01 | 深圳市卓宝科技股份有限公司 | Method for eliminating bubbles in asphalt sizing material |
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