CN204656168U - A kind of swirl flow gas-liquid separator - Google Patents
A kind of swirl flow gas-liquid separator Download PDFInfo
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- CN204656168U CN204656168U CN201520332096.1U CN201520332096U CN204656168U CN 204656168 U CN204656168 U CN 204656168U CN 201520332096 U CN201520332096 U CN 201520332096U CN 204656168 U CN204656168 U CN 204656168U
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Abstract
The utility model relates to a kind of swirl flow gas-liquid separator, comprises separable cartridge, blast pipe, dividing plate, riser, spin-ended, return duct and deflection plate; The top of separable cartridge arranges blast pipe, and blast pipe upper end is communicated with outside, and lower end extends in separable cartridge; Separable cartridge top arranges dividing plate, forms transition chamber between separable cartridge top and dividing plate, and the center of dividing plate wears fixing riser, the axis of riser and the dead in line of separable cartridge; Draft tube diameter is greater than air slit diameter, and the top of riser, just to the top of blast pipe, exists a discharge opeing annular space between riser and blast pipe; The bottom of separable cartridge is fixedly installed spin-ended, forms a main disengagement chamber between spin-ended and dividing plate, and the main disengagement chamber axle center place of spin-ended top arranges deflection plate; Spin-ended forms liquid pool with separable cartridge bottom, and the bottom of separable cartridge arranges a liquid-phase outlet; Return duct is arranged on the outside of separable cartridge, and upper port is communicated with transition chamber, and lower port is fixedly connected with deflection plate.
Description
Technical field
The utility model relates to a kind of separator, particularly about a kind of swirl flow gas-liquid separator.
Background technology
In the different phase that oil gas field is produced, the output of produce hydrocarbons and ratio all can change, this just has higher requirement to the adaptability for working condition of gas-liquid separation device, existing gas and oil separating plant often under high speed mist flow condition separating effect poor, drop with high velocity air from separator blast pipe escape and can not get reclaim.Prior art discloses a kind of secondary that carried out by escape drop and catch the cyclone separator be separated, it is in running, and gas-liquid mixed phase enters separator via tangential inlet, and most free liquid film can enter bottom liquid pool along separator inwall under gravity; The drop that Action of Gravity Field fails to be separated in time produces rotary motion in the main disengagement chamber formed by the annular space between separator inwall and riser and the separated space between riser entrance and deflection plate, is completed the separation of droplet by centrifugal force; Through main disengagement chamber except the air-flow of liquid is when entering riser and moving upward, because flow area diminishes, eddy flow more at a high speed and stronger centrifugal force is formed in riser, drop less for residue particle diameter is thrown to riser inwall, form liquid film at riser inwall, and migrate under the effect of riser inwall axial shearing stress and climb, the discharge opeing annular space through being arranged in riser upper end enters separator transition chamber, flow back to bottom liquid pond through return duct again, complete the separation again of escape drop.The key that the above-mentioned type separator can realize excellent separating property is: first, and the secondary separation liquid phase entering transition chamber is wanted can smoothly from return duct backflow, forms a good cyclic process by return duct; Secondly, Lourver position has the radial flow velocity in larger sensing axle center, and the liquid film that prevent this place from being formed again is entrainmented under larger radial flow velocity promotes enters into inward eddy; 3rd, prevent High Rotation Speed air-flow from producing disturbance to the liquid phase being separated to liquid pool, even carry secretly.
And in above-mentioned technology, the dividing plate of separator transition chamber is slab construction, in practical application, transition chamber dividing plate is difficult to accomplish complete level, if flat board exists the gradient contrary with refluxing opening direction in installation process, then can cause transition chamber hydrops and affect backflow.Meanwhile, although the plane deflection plate of employing can control swirl strength, isolation separated space and liquid pool, can not effectively stop drop carry due to the Radial Flow drag force of gas phase at Lourver position and enter the secondary that central gas core produces drop and escape.
Summary of the invention
For the problems referred to above, the purpose of this utility model is to provide a kind of swirl flow gas-liquid separator that can obtain better separating effect.
For achieving the above object, the utility model takes following technical scheme: a kind of swirl flow gas-liquid separator, is characterized in that: it comprise separable cartridge, blast pipe, dividing plate, riser, spin-ended, mixed phase inlet tube, return duct and deflection plate; The top of described separable cartridge arranges described blast pipe, and the upper end of described blast pipe is communicated with outside, and the lower end of described blast pipe extends to described separable cartridge inside; Described separable cartridge internal upper part arranges described dividing plate, forms a transition chamber between described separable cartridge top and described dividing plate; The center of described dividing plate wears fixing described riser, the axis of described riser and the dead in line of described separable cartridge; Described draft tube diameter is greater than described air slit diameter, and the top of described riser, just to the bottom of described blast pipe, exists a discharge opeing annular space between described riser and described blast pipe; The bottom of described separable cartridge is fixedly installed described spin-ended, and form a main disengagement chamber between described spin-ended and described dividing plate, the described main disengagement chamber axle center place being positioned at described spin-ended top arranges described deflection plate; Described spin-ended forms a liquid pool with described separable cartridge bottom, and the bottom of described separable cartridge arranges a liquid-phase outlet; The described mixed phase inlet tube that the top and one of described main disengagement chamber is arranged on the outside of described separable cartridge is communicated with; Described return duct is arranged on the outside of described separable cartridge, and the upper port of described return duct is communicated with described transition chamber, and the lower port of described return duct is fixedly connected with described deflection plate.
Described separator face adopts inclined plane to the end face of described transition chamber, and described inclined plane points to the upper port of described return duct.
The mode that the upper port of described return duct adopts dislocation to connect is communicated with described transition chamber, and namely the lower edge of the upper port of described return duct is lower than the upper edge of dividing plate.
Described deflection plate adopts conical plate, and the cone angle of described conical plate is towards the lower port of described riser, and the basal diameter of described conical plate is less than the internal diameter of described separable cartridge.
The rectangular tab of described spin-ended employing right-angled intersection, rectangular tab and the described separable cartridge inwall of described right-angled intersection are fixed.
The utility model is owing to taking above technical scheme, it has the following advantages: 1, the utility model is owing to comprising main disengagement chamber, liquid pool, discharge opeing annular space, transition chamber, riser, spin-ended, deflection plate and return duct, major part in gas-liquid mixed phase stream dissociate liquid film under gravity along main disengagement chamber inwall enter bottom liquid pool, Action of Gravity Field fails the drop that is separated in time producing rotary motion by the annular space between main disengagement chamber inwall and riser outer wall and the space between riser lower port and deflection plate, the separation of droplet is completed by centrifugal force, thus complete first time separation, through main disengagement chamber except the air-flow after liquid is entering riser, eddy flow more at a high speed and stronger centrifugal force is formed in riser, riser inwall formation liquid film is thrown to by remaining the less drop of particle diameter in air-flow, liquid film enters transition chamber by discharge opeing annular space, thus realize second time separation, twice separation can improve the separating property of separator, obtains good separating effect.2, separator face of the present utility model adopts inclined plane to the end face of transition chamber, and inclined plane points to the upper port of return duct, therefore enables the liquid in transition chamber flow into return duct smoothly, ensure that separator is separated the smooth backflow of liquid phase again.3, return duct upper port of the present utility model with adopt the mode misplacing and be communicated with between transition chamber, therefore avoid in transition chamber and produce hydrops.4, deflection plate of the present utility model adopts conical plate, the conical surface of conical plate provides a radially outer weight component to drop attached to it, in order to balance the drag force impetus of this place's radial air flow, avoid the liquid film be separated by secondary droplets, reduce the back-mixing degree that Lourver position is separated liquid film.5, the rectangular tab of spin-ended employing right-angled intersection of the present utility model, is fixed on separable cartridge inwall, further stablizes the liquid entering liquid pool, prevent fluctuation and high-speed rotational the entrainmenting liquid of liquid level.The utility model can be widely used in the process of gas-liquid separation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of the utility model dividing plate;
Fig. 3 is the relative position relation schematic diagram of the utility model dividing plate and return duct upper port;
Fig. 4 is the structural representation of the utility model deflection plate;
Fig. 5 is the cut-away view of Fig. 4;
Fig. 6 is the spin-ended chip architecture schematic diagram of the utility model.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is described in detail.
As shown in Figure 1, the swirl flow gas-liquid separator that the utility model provides, it comprise separable cartridge 1, blast pipe 2, dividing plate 3, transition chamber 4, riser 5, discharge opeing annular space 6, spin-ended 7, main disengagement chamber 8, liquid pool 9, liquid-phase outlet 10, mixed phase inlet tube 11, return duct 12 and deflection plate 13.The top of separable cartridge 1 arranges blast pipe 2, and the upper end of blast pipe 2 is communicated with outside, and the lower end of blast pipe 2 extends to separable cartridge 1 inside.Separable cartridge 1 internal upper part arranges dividing plate 3, forms transition chamber 4 between separable cartridge 1 top and dividing plate 3, and the center of dividing plate 3 wears fixing riser 5, the axis of riser 5 and the dead in line of separable cartridge 1.Riser 5 diameter is greater than blast pipe 2 diameter, and the top of riser 5, just to the bottom of blast pipe 2, exists discharge opeing annular space 6 between riser 5 and blast pipe 2.The bottom of separable cartridge 1 is fixedly installed spin-ended 7, main disengagement chamber 8 is formed between spin-ended 7 and dividing plate 3, the main disengagement chamber 8 axle center place be positioned at above spin-ended 7 arranges deflection plate 13, and spin-ended 7 forms liquid pool 9 with the bottom of separable cartridge 1, and the bottom of separable cartridge 1 arranges liquid-phase outlet 10.The top of separable cartridge 1 is communicated with the mixed phase inlet tube 11 being arranged on separable cartridge 1 outside.Return duct 12 is arranged on the outside of separable cartridge 1, and the upper port of return duct 12 is communicated with transition chamber 4, and the lower port of return duct 12 is fixedly connected with deflection plate 13.Return duct 12 is arranged on the outside of separable cartridge 1, and the upper port of return duct 12 is communicated with transition chamber 4, and the lower port of return duct 12 is fixedly connected with deflection plate 13.
In a preferred embodiment, as shown in Figure 2, dividing plate 3 can adopt inclined plane towards the end face of transition chamber 4, and inclined plane points to the upper port of return duct 12, thus ensure the liquid being entered transition chamber 4 in riser 5 by discharge opeing annular space 6, return duct 12 can be flowed into smoothly.
In a preferred embodiment, as shown in Figure 3, when the upper port of return duct 12 is communicated with transition chamber 4, the mode that dislocation connects can be adopted, namely the lower edge of the upper port of return duct 12 is a little less than the upper edge of dividing plate 3, once have liquid to produce in transition chamber 4, liquid just can flow to return duct 12 smoothly, thus avoids producing hydrops in transition chamber 4.
In a preferred embodiment, as shown in Figures 4 and 5, deflection plate 13 can adopt conical plate, and the cone angle of conical plate is towards the lower port of riser 5, and the basal diameter of conical plate is less than the internal diameter of separable cartridge 1.The conical surface of conical plate provides a radially outer weight component to drop attached to it, in order to balance the drag force impetus of this place's radial air flow, avoids the liquid film be separated by secondary droplets.During work, due to cyclonic action, between transition chamber 4 and deflection plate 13, form positive pressure difference, thus the liquid be forced through in riser 5 enters transition chamber 4 from discharge opeing annular space 6.Enter liquid in transition chamber 4 by after return duct 12, be discharged on main disengagement chamber 8 inwall by the port of deflection plate 13, and flow back to liquid pool 9.
In a preferred embodiment, as shown in Figure 6, spin-ended 7, for further stablizing the liquid entering liquid pool 9, prevents fluctuation and high-speed rotational the entrainmenting liquid of liquid level, it can adopt the rectangular tab of right-angled intersection, and right-angled intersection rectangular tab and separable cartridge 1 inwall are fixed.
The concrete use procedure of the swirl flow gas-liquid separator that the utility model provides is:
Gas-liquid mixed phase flows through and enters separable cartridge 1 by mixed phase inlet tube 11, the major part in gas-liquid mixed phase stream dissociate liquid film can under gravity along main disengagement chamber 8 inwall enter bottom liquid pool 9.The drop that Action of Gravity Field fails to be separated in time, producing rotary motion by the annular space between main disengagement chamber 8 inwall and riser 5 outer wall and the space between riser 5 lower port and deflection plate 13, is completed the separation of droplet by centrifugal force.
Through main disengagement chamber 8 except the air-flow after liquid is when entering riser 5 and moving upward, because flow area diminishes, eddy flow more at a high speed and stronger centrifugal force is formed in riser 5, riser 5 inwall is thrown to by remaining the less drop of particle diameter in air-flow, liquid film is formed at riser 5 inwall, and migrate under the effect of riser 5 inwall axial shearing stress and climb, discharge opeing annular space 6 through being arranged in riser 5 top enters separator transition chamber 4, because dividing plate 3 end face is inclined plane, the liquid phase entering transition chamber 4 has flowed to return duct 12 upper port smoothly, the mode adopting dislocation to connect due to return duct 12 upper port is communicated with transition chamber 4, the liquid phase that ensure that in transition chamber 4 is not formed to be gathered, thus enter return duct 12 smoothly.The liquid phase entering return duct 12 sprays to main disengagement chamber 8 inwall from deflection plate 13 port connecting return duct 12 lower end, the conical design of deflection plate 13 provides a radially outer weight component to drop attached to it, in order to balance the drag force impetus of this place's radial air flow, avoid the liquid film be separated by secondary droplets.The liquid phase of main disengagement chamber 8 inwall flows to liquid pool 9 through spin-ended 7 under gravity, complete the separation again of escape drop, adopt the rectangular tab of right-angled intersection for spin-ended 7, the liquid phase being separated to liquid pool 9 is further stablized, prevent high-speed rotational from causing the fluctuation of liquid level and entrainmenting liquid phase, the liquid phase in liquid pool 9 flows out separable cartridge 1 eventually through liquid-phase outlet 10.
The various embodiments described above are only for illustration of the utility model; wherein the structure of each parts, connected mode and manufacture craft etc. all can change to some extent; every equivalents of carrying out on the basis of technical solutions of the utility model and improvement, all should not get rid of outside protection domain of the present utility model.
Claims (6)
1. a swirl flow gas-liquid separator, is characterized in that: it comprise separable cartridge, blast pipe, dividing plate, riser, spin-ended, mixed phase inlet tube, return duct and deflection plate; The top of described separable cartridge arranges described blast pipe, and the upper end of described blast pipe is communicated with outside, and the lower end of described blast pipe extends to described separable cartridge inside; Described separable cartridge internal upper part arranges described dividing plate, forms a transition chamber between described separable cartridge top and described dividing plate; The center of described dividing plate wears fixing described riser, the axis of described riser and the dead in line of described separable cartridge; Described draft tube diameter is greater than described air slit diameter, and the top of described riser, just to the bottom of described blast pipe, exists a discharge opeing annular space between described riser and described blast pipe; The bottom of described separable cartridge is fixedly installed described spin-ended, and form a main disengagement chamber between described spin-ended and described dividing plate, the described main disengagement chamber axle center place being positioned at described spin-ended top arranges described deflection plate; Described spin-ended forms a liquid pool with described separable cartridge bottom, and the bottom of described separable cartridge arranges a liquid-phase outlet; The described mixed phase inlet tube that the top and one of described main disengagement chamber is arranged on the outside of described separable cartridge is communicated with; Described return duct is arranged on the outside of described separable cartridge, and the upper port of described return duct is communicated with described transition chamber, and the lower port of described return duct is fixedly connected with described deflection plate.
2. a kind of swirl flow gas-liquid separator as claimed in claim 1, is characterized in that: described separator face adopts inclined plane to the end face of described transition chamber, and described inclined plane points to the upper port of described return duct.
3. a kind of swirl flow gas-liquid separator as claimed in claim 1, is characterized in that: the mode that the upper port of described return duct adopts dislocation to connect is communicated with described transition chamber, and namely the lower edge of the upper port of described return duct is lower than the upper edge of dividing plate.
4. a kind of swirl flow gas-liquid separator as claimed in claim 2, is characterized in that: the mode that the upper port of described return duct adopts dislocation to connect is communicated with described transition chamber, and namely the lower edge of the upper port of described return duct is lower than the upper edge of dividing plate.
5. a kind of swirl flow gas-liquid separator as claimed in claim 1 or 2 or 3 or 4, it is characterized in that: described deflection plate adopts conical plate, the cone angle of described conical plate is towards the lower port of described riser, and the basal diameter of described conical plate is less than the internal diameter of described separable cartridge.
6. a kind of swirl flow gas-liquid separator as claimed in claim 1 or 2 or 3 or 4, is characterized in that: the described spin-ended rectangular tab adopting right-angled intersection, rectangular tab and the described separable cartridge inwall of described right-angled intersection are fixed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201520332096.1U CN204656168U (en) | 2015-05-21 | 2015-05-21 | A kind of swirl flow gas-liquid separator |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520332096.1U CN204656168U (en) | 2015-05-21 | 2015-05-21 | A kind of swirl flow gas-liquid separator |
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| CN204656168U true CN204656168U (en) | 2015-09-23 |
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| CN201520332096.1U Active CN204656168U (en) | 2015-05-21 | 2015-05-21 | A kind of swirl flow gas-liquid separator |
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| CN105879501A (en) * | 2016-06-13 | 2016-08-24 | 杭州中能汽轮动力有限公司 | Steam-water separator |
| CN106039774A (en) * | 2016-07-12 | 2016-10-26 | 西南石油大学 | Experimental device for separating gas-liquid mixture and measuring gas volume and liquid volume |
| CN106865673A (en) * | 2017-04-13 | 2017-06-20 | 中国石油大学(华东) | A kind of swirl flow air supporting oil-contained waste water treatment device |
| CN107519693A (en) * | 2017-10-16 | 2017-12-29 | 陕西航天泵阀科技集团有限公司 | A kind of gas-liquid separation device |
| CN107557087A (en) * | 2017-09-05 | 2018-01-09 | 中石化广州工程有限公司 | A kind of spiral-flow type gas-liquid separation device and method |
| CN107648888A (en) * | 2017-10-13 | 2018-02-02 | 中石化广州工程有限公司 | Air separator and gas-liquid separating method for gas-liquid separation |
| CN107670338A (en) * | 2017-09-21 | 2018-02-09 | 中石化广州工程有限公司 | A kind of outer-flowing type air separator |
| CN107882547A (en) * | 2016-09-29 | 2018-04-06 | 中国石油化工股份有限公司 | Duct type high-water-cut oil-producing well produces liquid three-phase metering mechanism and method |
| CN108237023A (en) * | 2016-12-25 | 2018-07-03 | 况保宗 | Eddy flow low speed deduster |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN105879501A (en) * | 2016-06-13 | 2016-08-24 | 杭州中能汽轮动力有限公司 | Steam-water separator |
| CN106039774A (en) * | 2016-07-12 | 2016-10-26 | 西南石油大学 | Experimental device for separating gas-liquid mixture and measuring gas volume and liquid volume |
| CN107882547B (en) * | 2016-09-29 | 2023-08-04 | 中国石油化工股份有限公司 | Pipeline type high-water-content oil well liquid production three-phase metering device and method |
| CN107882547A (en) * | 2016-09-29 | 2018-04-06 | 中国石油化工股份有限公司 | Duct type high-water-cut oil-producing well produces liquid three-phase metering mechanism and method |
| CN108237023A (en) * | 2016-12-25 | 2018-07-03 | 况保宗 | Eddy flow low speed deduster |
| CN108237023B (en) * | 2016-12-25 | 2021-07-27 | 况保宗 | Cyclone low-speed dust remover |
| CN106865673A (en) * | 2017-04-13 | 2017-06-20 | 中国石油大学(华东) | A kind of swirl flow air supporting oil-contained waste water treatment device |
| CN107557087A (en) * | 2017-09-05 | 2018-01-09 | 中石化广州工程有限公司 | A kind of spiral-flow type gas-liquid separation device and method |
| CN107557087B (en) * | 2017-09-05 | 2020-06-23 | 中石化广州工程有限公司 | Spiral-flow type gas-liquid separation device and method |
| CN107670338A (en) * | 2017-09-21 | 2018-02-09 | 中石化广州工程有限公司 | A kind of outer-flowing type air separator |
| CN107670338B (en) * | 2017-09-21 | 2020-04-14 | 中石化广州工程有限公司 | Outward flow type air eliminator |
| CN107648888A (en) * | 2017-10-13 | 2018-02-02 | 中石化广州工程有限公司 | Air separator and gas-liquid separating method for gas-liquid separation |
| CN107648888B (en) * | 2017-10-13 | 2019-10-22 | 中石化广州工程有限公司 | Air separator and gas-liquid separating method for gas-liquid separation |
| CN107519693A (en) * | 2017-10-16 | 2017-12-29 | 陕西航天泵阀科技集团有限公司 | A kind of gas-liquid separation device |
| CN108339789A (en) * | 2018-03-01 | 2018-07-31 | 上海毓风机电设备有限公司 | A kind of cooling tower water-collecting tray automatic cleaning system and its cleaning method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 100010 Beijing, Chaoyangmen, North Street, No. 25, No. Co-patentee after: CNOOC research institute limited liability company Patentee after: China Offshore Oil Group Co., Ltd. Address before: 100010 Beijing, Chaoyangmen, North Street, No. 25, No. Co-patentee before: CNOOC Research Institute Patentee before: China National Offshore Oil Corporation |
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| CP01 | Change in the name or title of a patent holder |