CN206121403U - Distributing type gas -liquid pre -separation device - Google Patents
Distributing type gas -liquid pre -separation device Download PDFInfo
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- CN206121403U CN206121403U CN201621134447.9U CN201621134447U CN206121403U CN 206121403 U CN206121403 U CN 206121403U CN 201621134447 U CN201621134447 U CN 201621134447U CN 206121403 U CN206121403 U CN 206121403U
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- pipe
- inlet tube
- radian
- liquid pre
- angle steel
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Abstract
The utility model relates to a technical field of gravity type vapour and liquid separator part discloses a distributing type gas -liquid pre -separation device, including the inlet tube of taking the horn mouth, horn mouth jointing equipment inlet tube, the other end of inlet tube and the one end of shrimps pipe are connected, the other end of shrimps pipe is connected through the one end of first flange and connecting pipe, the other end of connecting pipe passes through second flange and apron surface connections, and a plurality of support angle steel become the circumference to be fixed in the unoccupied place between even class between apron lower surface and the bottom plate upper surface, a plurality of supporting beam fix the bottom plate lower surface is just placed in equipment barrel bottom, every supporting beam's both ends all are fixed with the circular arc board, the radian of circular arc board is the same with the radian of equipment barrel. The device simple structure, and reduce turbulent kinetic energy, reduce the breakup of drop, further improve the efficiency of separator.
Description
Technical field
This utility model is related to the technical field of gas-liquid gravity separator part, more particularly to a kind of distributed gas-liquid is pre-
Segregation apparatuss.
Background technology
In gas-liquid separator design, we often separate the hydrocarbon under specified temp and pressure using Gravity separate method
The gas-liquid component of fluid.Generally as separator is the initial management container of all devices, so separator is accurate
Design is extremely important.If this processing unit design is inaccurate, " bottleneck " effect will be formed, causes complete equipment to process
The decline of efficiency.And the separation efficiency of gravitational separator is heavily dependent on pre-separate device.Separator inlet fluid
Usually typical high viscous turbulent flow gas-liquid mixture.As fluid is presented high viscosity and high coagulant state, thus its when entering separator with compared with
High kinetic energy.Entrance pre-separate device by absorbing liquid kinetic energy and can change its flow direction, so that gas-liquid separation, the dress
Put mainly solve the gas-liquid pre-separation of gas-liquid separator entrance fluid not exclusively and liquid splash, it is broken after a large amount of formation foams
Technical problem.For gravitational separator, inlet device commonly use in current engineering and maturation is half-open tubular type and vane type
Two kinds of pre-separate devices.Half-open tubular type pre-separate device is applied to absorption kinetic energy and is less than 2100Pa, and vane type pre-separate device is fitted
For absorbing kinetic energy less than 6000Pa.During for entrance fluid dynamic energy more than 6000Pa, there is provided go out an efficient, compact, price
Cheap and practicable pre-separation inlet device is eager needs.
Utility model content
In order to solve the deficiencies in the prior art, this utility model provides a kind of distributed gas-liquid pre-separate device, reduces dynamic
Can, the breakup of drop is reduced, the efficiency of separator is further improved.
This utility model can be achieved through the following technical solutions:
A kind of distributed gas-liquid pre-separate device, including with bell-mouthed inlet tube, the horn mouth connects equipment entrance
Pipe, one end connection of the other end and dried shrimps pipe of the inlet tube, the other end of the dried shrimps pipe pass through first flange and connection
One end connection of pipe, the other end of the connecting tube pass through second flange and the connection of cover plate upper surface, multiple support angle steels Cheng Yuan
All uniform grades are fixed between the cover plate lower surface and plate upper surface with gap, and multiple support beams are fixed on the base plate
Lower surface and equipment barrel bottom is placed on, the two ends of each support beam are respectively and fixedly provided with steel plate, the radian of the steel plate
It is identical with the radian of equipment barrel.
Further, the opening of the support angle steel is outwardly;The interior circular diameter of multiple support angle steel compositions is not less than company
The diameter of adapter, outside diameter are not more than the diameter of tube sheet and base plate;The support beam is channel-section steel, perpendicular to equipment barrel axle
The diameter of line direction and length more than base plate.
Further, the gap between multiple support angle steels is 30-50mm.
This utility model is beneficial to be had technical effect that:
The pre-separate device simple structure, low cost of manufacture, and the change of fluid parameter can be well adapted to, can be right
Substantial amounts of air-liquid or solid carry out pre-separation, and insensitive to corrosive medium.Can be connected with any entry nozzle, can subtract
Small inlet fluid dynamic potential energy, reduce to greatest extent drop crush and foam generation, be uniformly distributed medium, pressure drop ratio compared with
It is little.Different rate of flow of fluids and liquid level can be passed through during concrete practical operation, the connecting tube and base plate of different length is selected
The inlet device of size, it is to avoid the phenomenon of fluid splash occur.
Description of the drawings
Fig. 1 is structural front view of the present utility model;
Fig. 2 is structure left view of the present utility model;
Fig. 3 is operation principle structural representation of the present utility model;
Fig. 4 is support angle steel arrangement schematic diagram of the present utility model, and the gap A in figure between support angle steel is 30-
50mm;
Wherein, 1- equipment entrances pipe, 2- inlet tubes, 3- dried shrimps pipes, 4- first flanges, 5- connecting tubes, 6- second flanges, 7-
Cover plate, 8- support angle steels, 9- base plates, 10- support beams, 11- steel plates.
Specific embodiment
Below in conjunction with the accompanying drawings and preferred embodiment describes specific embodiment of the present utility model in detail.
As Figure 1-3, equipment entrance pipe 1 is inserted in the horn mouth of inlet tube 2, the other end and the dried shrimps pipe 3 of inlet tube 2
Using being welded to connect;3 other end of dried shrimps pipe is connected with connecting tube 5 by first flange 4, and the first flange 4 includes two flanges,
One is welded on dried shrimps pipe 4, and another is welded in connecting tube 5;The other end of connecting tube 5 is by second flange 6 and cover plate 7
Connected with securing member;Multiple support angle steels 8 are welded to connect with cover plate and base plate 9, and angle steel opening outwardly, is arranged in into even circumferential
Between cover plate 7 and base plate 9, the gap between general support angle steel 8 is maintained between 30~50mm and is preferred.9 bottom welding of base plate
Two support beams 10, support beam 10 are channel-section steel, and two pieces of arc plates 11 are welded at channel-section steel two ends, in 11 radian of arc plate and cylinder
Wall radian is identical.
Whole inlet device is integrated, and is easy to integral demounting to install.The quantity of support angle steel is with gap according to practical situation
Depending on.During work, after fluid-mixing enters pre-separate device, after support angle steel is shunted, as kinetic energy is reduced, medium delays
Slowly by support angle steel gap, water droplet rises to that surface time is elongated, is thus provided that bigger chance and other droplet coalescences
Bigger water droplet is formed, separation process is assisted.
Although the foregoing describing specific embodiment of the present utility model, it will be appreciated by those of skill in the art that
These are merely illustrative of, and on the premise of without departing substantially from principle of the present utility model and essence, these embodiments can be done
Go out various changes or modifications, therefore, protection domain of the present utility model is defined by the appended claims.
Claims (3)
1. a kind of distributed gas-liquid pre-separate device, it is characterised in that:Including with bell-mouthed inlet tube, the horn mouth connection
Equipment entrance pipe, one end connection of the other end and dried shrimps pipe of the inlet tube, the other end of the dried shrimps pipe pass through the first method
One end of blue and connecting tube connects, and the other end of the connecting tube passes through second flange and the connection of cover plate upper surface, multiple supports
Angle steel is fixed between the cover plate lower surface and plate upper surface with gap into even circumferential etc., and multiple support beams are fixed on
The base plate lower surface and equipment barrel bottom is placed on, the two ends of each support beam are respectively and fixedly provided with arc plate, described
The radian of arc plate is identical with the radian of equipment barrel.
2. the distributed gas-liquid pre-separate device described in claim 1, it is characterised in that:The opening of the support angle steel is outwardly;
The interior circular diameter of multiple support angle steel compositions is not less than the straight of the diameter of connecting tube, outside diameter no more than tube sheet and base plate
Footpath;The support beam be channel-section steel, perpendicular to equipment barrel axis direction and length more than base plate diameter.
3. the distributed gas-liquid pre-separate device described in claim 1 or 2, it is characterised in that:Between multiple support angle steels
Gap be 30-50mm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621134447.9U CN206121403U (en) | 2016-10-18 | 2016-10-18 | Distributing type gas -liquid pre -separation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621134447.9U CN206121403U (en) | 2016-10-18 | 2016-10-18 | Distributing type gas -liquid pre -separation device |
Publications (1)
Publication Number | Publication Date |
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CN206121403U true CN206121403U (en) | 2017-04-26 |
Family
ID=58573927
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201621134447.9U Active CN206121403U (en) | 2016-10-18 | 2016-10-18 | Distributing type gas -liquid pre -separation device |
Country Status (1)
Country | Link |
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CN (1) | CN206121403U (en) |
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2016
- 2016-10-18 CN CN201621134447.9U patent/CN206121403U/en active Active
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