CN204107190U - Self-rotary gas-liquid separator - Google Patents
Self-rotary gas-liquid separator Download PDFInfo
- Publication number
- CN204107190U CN204107190U CN201420549752.9U CN201420549752U CN204107190U CN 204107190 U CN204107190 U CN 204107190U CN 201420549752 U CN201420549752 U CN 201420549752U CN 204107190 U CN204107190 U CN 204107190U
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- Prior art keywords
- inner barrel
- cylinder body
- outer cylinder
- gas
- spin
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- Expired - Lifetime
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 35
- 239000012530 fluid Substances 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 238000000926 separation method Methods 0.000 abstract description 11
- 230000000903 blocking effect Effects 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 235000014653 Carica parviflora Nutrition 0.000 description 2
- 241000243321 Cnidaria Species 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
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- Centrifugal Separators (AREA)
Abstract
The utility model belongs to chemical industry equipment gas-liquid separation technical field, is specifically related to a kind of self-rotary gas-liquid separator; Comprise outer cylinder body, the center at outer cylinder body top is provided with outer cylinder body air inlet, the side on outer cylinder body top is provided with gas outlet, the inside of outer cylinder body is provided with spin inner barrel, the position that outer cylinder body air inlet bottom is corresponding with spin inner barrel top offers the inner barrel air inlet that spins, and gas inlet duct passes vertically through outer cylinder body air inlet and spin inner barrel air inlet; The side direction inclined tube of described gas inlet duct is 35 ° ~ 40 ° angles with spin inner barrel center line; The barrel of described spin inner barrel offers several rectangular grid gate hole, the outer surface of described spin inner barrel is provided with rotating vane, rotating vane to be radian the be arc of 75 ° ~ 110 °; There is reasonable in design, structure simple, gas-liquid separation efficiency can be improved and avoid occurring the advantage of blocking.
Description
Technical field
The utility model belongs to chemical industry equipment gas-liquid separation technical field, is specifically related to a kind of self-rotary gas-liquid separator.
Background technology
The gas-liquid separation of process gas is unit operations comparatively general and important in the Chemical Manufacture such as synthetic ammonia.Existing gas-liquid separation equipment is mainly divided into gravity type and screen type separator, separator normally in tower equipment close to exit, gas-liquid separator is set and carries out simple gas-liquid separation, simultaneously set up special gas-liquid separation equipment to carry out precipitation of liquid droplets later.But in actual production, this method is not because have guiding device, and separating effect is very poor, also easily blocking, increases SR.Many producers are the frequent parking maintenance of having to because of separator blocking all, and cleaning separator, what have even removes separator.So just greatly have impact on normally carrying out of production, gas-liquid cannot be separated, reduce the quality of gas, great harm is caused to lower workshop section.
Utility model content
The purpose of this utility model is to overcome defect of the prior art, and provide a kind of reasonable in design, structure simple, gas-liquid separation efficiency can be improved and avoid occurring the self-rotary gas-liquid separator of blocking.
The purpose of this utility model be achieved in that comprise outer cylinder body, the center at outer cylinder body top is provided with outer cylinder body air inlet, the side on outer cylinder body top is provided with gas outlet, the inside of outer cylinder body is provided with spin inner barrel, the position that outer cylinder body air inlet bottom is corresponding with spin inner barrel top offers the inner barrel air inlet that spins, and gas inlet duct passes vertically through outer cylinder body air inlet and spin inner barrel air inlet; The side direction inclined tube of described gas inlet duct is 35 ° ~ 40 ° angles with spin inner barrel center line; The barrel of described spin inner barrel offers several rectangular grid gate hole, the outer surface of described spin inner barrel is provided with rotating vane, rotating vane to be radian the be arc of 75 ° ~ 110 °; The inner bottom part of described spin inner barrel is provided with liquid-seal type liquid-leaking nozzle; The bottom centre position of described spin inner barrel is provided with the inner cylinder rotating axle be connected with electric rotating machine; The top of described electric rotating machine is provided with the baffle plate be connected with outer cylinder body inner surface, and the bottom of baffle plate and inner cylinder rotating shaft connection place is provided with water seal, and the side at baffle plate top is provided with fluid collection chamber; Described fluid collection chamber is connected with discharging tube.The side direction inclined tube of described gas inlet duct is 40 ° of angles with spin inner barrel center line.Described rotating vane to be radian the be arc of 80 °.The bottom of described electric rotating machine is provided with electric machine support.The area of several rectangular grid gate hole described is identical.Distance between described two adjacent rectangular grid gate hole is identical.Described rotating vane is arranged between two adjacent rectangular grid gate hole.Described liquid-seal type liquid-leaking nozzle is four.
The self-rotary gas-liquid separator made according to such scheme, gas to be entered to spin inner barrel by inlet line, because inner/outer tube inside and outside exists pressure reduction, gas enters outer cylinder body fast from lattice coral hole, and rotating vane is subject to gas and impacts drive spin inner barrel fast rotational; Droplet in gas, under the effect of centrifugal force and self gravitation, collides on rotating vane, and accumulation forms liquid film gradually, flows automatically to bottom outer cylinder body; In outer cylinder body, gas is discharged by side direction gas outlet simultaneously.The utility model utilizes gas self power to drive inward turning cylindrical shell to rotate, gas realizes being separated under self centrifugal force with the effect of gravity with liquid, power consumption is little, separative efficiency is high, without clogging, practicality is comparatively strong, when there is situation about being short of power, by electric rotating machine, spin inner barrel being rotated and realizing gas-liquid separator; There is reasonable in design, structure simple, gas-liquid separation efficiency can be improved and avoid occurring the advantage of blocking.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model;
Fig. 2 is the top view of spin inner barrel.
Detailed description of the invention
As shown in Figure 1, 2, the utility model comprises outer cylinder body 3, the center at outer cylinder body 3 top is provided with outer cylinder body air inlet, the side on outer cylinder body 3 top is provided with gas outlet 2, the inside of outer cylinder body 3 is provided with spin inner barrel 4, the position that outer cylinder body air inlet bottom is corresponding with spin inner barrel 4 top offers the inner barrel air inlet that spins, and gas inlet duct 1 passes vertically through outer cylinder body air inlet and spin inner barrel air inlet; The side direction inclined tube of described gas inlet duct 1 is 35 ° ~ 40 ° angles with spin inner barrel 4 center line; The barrel of described spin inner barrel 4 offers several rectangular grid gate hole 7, the outer surface of described spin inner barrel 4 is provided with rotating vane 5, rotating vane 5 for radian be the arc of 75 ° ~ 110 °; The inner bottom part of described spin inner barrel 4 is provided with liquid-seal type liquid-leaking nozzle 6; The bottom centre position of described spin inner barrel 4 is provided with the inner cylinder rotating axle 8 be connected with electric rotating machine 10; The top of described electric rotating machine 10 is provided with the baffle plate 14 be connected with outer cylinder body 3 inner surface, and baffle plate 14 is provided with water seal 9 with the bottom of inner cylinder rotating axle 8 junction, and the side at baffle plate 14 top is provided with fluid collection chamber 12; Described fluid collection chamber 12 is connected with discharging tube 13.The side direction inclined tube of described gas inlet duct 1 is 40 ° of angles with spin inner barrel 4 center line.Described rotating vane 5 for radian be the arc of 80 °.The bottom of described electric rotating machine 10 is provided with electric machine support 11.The area of several rectangular grid gate hole 7 described is identical.Distance between described two adjacent rectangular grid gate hole 7 is identical.Described rotating vane 5 is arranged between two adjacent rectangular grid gate hole 7.Described liquid-seal type liquid-leaking nozzle 6 is four.On the barrel of described spin inner barrel 4, radial direction offers several rectangular grid gate hole 7 uniformly, and rectangular grid gate hole 7 specification size is identical; The rotating vane 5 arranged between two adjacent rectangular grid gate hole 7 is for turning clockwise.Described four liquid-seal type liquid-leaking nozzles 6 adopt symmetrical mode to install.
When using the utility model, band liquid gas from gas inlet pipeline 1 side direction enters in inward turning cylindrical shell 4, because inner/outer tube inside and outside exists pressure reduction, gas enters outer cylinder body fast from lattice coral hole, and now rotating vane is subject to gas impact and drives spin inner barrel fast rotational; Drop in gas, under the effect of centrifugal force and self gravitation, collides on rotating vane, and accumulation forms liquid film gradually, flows automatically to bottom outer cylinder body; In outer cylinder body, gas is discharged by side direction gas outlet under the effect of pressure reduction simultaneously.Liquid gas is with to achieve gas-liquid separation by the mode of eddy flow thus; Bottom inward turning cylindrical shell 4, four liquid-seal type liquid-leaking nozzles 6 are installed simultaneously, ensure that inside and outside cylindrical shell does not occur phenomenon of collaborating, make the liquid of inward turning cylindrical shell 4 be discharged to outside cylindrical shell 3 simultaneously; The utility model does not need power-equipment under normal circumstances, but when inward turning cylindrical shell 4 turn up requires less than gas-liquid separation rotation, can open electric rotating machine 10 and drive inward turning cylindrical shell 4 to rotate, thus obtain higher separative efficiency.
Claims (8)
1. a self-rotary gas-liquid separator, comprise outer cylinder body (3), the center at outer cylinder body (3) top is provided with outer cylinder body air inlet, the side on outer cylinder body (3) top is provided with gas outlet (2), it is characterized in that: the inside of outer cylinder body (3) is provided with spin inner barrel (4), the position that outer cylinder body air inlet bottom is corresponding with spin inner barrel (4) top offers the inner barrel air inlet that spins, and gas inlet duct (1) passes vertically through outer cylinder body air inlet and spin inner barrel air inlet; The side direction inclined tube of described gas inlet duct (1) is 35 ° ~ 40 ° angles with spin inner barrel (4) center line; The barrel of described spin inner barrel (4) offers several rectangular grid gate hole (7), the outer surface of described spin inner barrel (4) is provided with rotating vane (5), rotating vane (5) for radian be the arc of 75 ° ~ 110 °; The inner bottom part of described spin inner barrel (4) is provided with liquid-seal type liquid-leaking nozzle (6); The bottom centre position of described spin inner barrel (4) is provided with the inner cylinder rotating axle (8) be connected with electric rotating machine (10); The top of described electric rotating machine (10) is provided with the baffle plate (14) be connected with outer cylinder body (3) inner surface, baffle plate (14) is provided with water seal (9) with the bottom of inner cylinder rotating axle (8) junction, and the side at baffle plate (14) top is provided with fluid collection chamber (12); Described fluid collection chamber (12) is connected with discharging tube (13).
2. self-rotary gas-liquid separator according to claim 1, is characterized in that: the side direction inclined tube of described gas inlet duct (1) is 40 ° of angles with spin inner barrel (4) center line.
3. self-rotary gas-liquid separator according to claim 1, is characterized in that: described rotating vane (5) for radian be the arc of 80 °.
4. self-rotary gas-liquid separator according to claim 1, is characterized in that: the bottom of described electric rotating machine (10) is provided with electric machine support (11).
5. self-rotary gas-liquid separator according to claim 1, is characterized in that: the area of several rectangular grid gate hole (7) described is identical.
6. self-rotary gas-liquid separator according to claim 1, is characterized in that: the distance between described two adjacent rectangular grid gate hole (7) is identical.
7. self-rotary gas-liquid separator according to claim 1, is characterized in that: described rotating vane (5) is arranged between two adjacent rectangular grid gate hole (7).
8. self-rotary gas-liquid separator according to claim 1, is characterized in that: described liquid-seal type liquid-leaking nozzle (6) is four.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420549752.9U CN204107190U (en) | 2014-09-24 | 2014-09-24 | Self-rotary gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420549752.9U CN204107190U (en) | 2014-09-24 | 2014-09-24 | Self-rotary gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204107190U true CN204107190U (en) | 2015-01-21 |
Family
ID=52324553
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420549752.9U Expired - Lifetime CN204107190U (en) | 2014-09-24 | 2014-09-24 | Self-rotary gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204107190U (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105709509A (en) * | 2016-04-22 | 2016-06-29 | 台州龙江化工机械科技有限公司 | Steam-water separation device |
| CN106582120A (en) * | 2016-12-15 | 2017-04-26 | 山东神华山大能源环境有限公司 | Gas-liquid separating drum for flue gas dewatering, dewatering device and system |
| CN107774213A (en) * | 2016-08-30 | 2018-03-09 | 南通鸿志化工有限公司 | A kind of telescopic sodium borohydride agitating device |
| CN108067046A (en) * | 2016-11-11 | 2018-05-25 | 中国石油化工股份有限公司抚顺石油化工研究院 | High efficiency demister |
| CN108067044A (en) * | 2016-11-11 | 2018-05-25 | 中国石油化工股份有限公司抚顺石油化工研究院 | Defogging equipment |
| CN109098952A (en) * | 2018-08-30 | 2018-12-28 | 西安交通大学 | A kind of axial-flow type whizzer and oil and gas separation method |
| CN109297299A (en) * | 2018-10-31 | 2019-02-01 | 上海成界制药设备有限公司 | A kind of device preventing discharging beat |
| CN109806673A (en) * | 2019-03-06 | 2019-05-28 | 中国石油大学(北京) | A kind of gas-liquid separation device for gas defoaming |
| CN110041976A (en) * | 2019-03-15 | 2019-07-23 | 中国煤层气集团有限公司 | Gas-solid-liquid separating apparatus |
| CN115155219A (en) * | 2022-08-22 | 2022-10-11 | 浙江洛森压缩机股份有限公司 | Gas-liquid separation sewage discharging system |
-
2014
- 2014-09-24 CN CN201420549752.9U patent/CN204107190U/en not_active Expired - Lifetime
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105709509A (en) * | 2016-04-22 | 2016-06-29 | 台州龙江化工机械科技有限公司 | Steam-water separation device |
| CN107774213A (en) * | 2016-08-30 | 2018-03-09 | 南通鸿志化工有限公司 | A kind of telescopic sodium borohydride agitating device |
| CN108067046A (en) * | 2016-11-11 | 2018-05-25 | 中国石油化工股份有限公司抚顺石油化工研究院 | High efficiency demister |
| CN108067044A (en) * | 2016-11-11 | 2018-05-25 | 中国石油化工股份有限公司抚顺石油化工研究院 | Defogging equipment |
| CN106582120A (en) * | 2016-12-15 | 2017-04-26 | 山东神华山大能源环境有限公司 | Gas-liquid separating drum for flue gas dewatering, dewatering device and system |
| CN109098952B (en) * | 2018-08-30 | 2019-08-23 | 西安交通大学 | A kind of axial-flow type whizzer and oil and gas separation method |
| CN109098952A (en) * | 2018-08-30 | 2018-12-28 | 西安交通大学 | A kind of axial-flow type whizzer and oil and gas separation method |
| CN109297299A (en) * | 2018-10-31 | 2019-02-01 | 上海成界制药设备有限公司 | A kind of device preventing discharging beat |
| CN109806673A (en) * | 2019-03-06 | 2019-05-28 | 中国石油大学(北京) | A kind of gas-liquid separation device for gas defoaming |
| CN110041976A (en) * | 2019-03-15 | 2019-07-23 | 中国煤层气集团有限公司 | Gas-solid-liquid separating apparatus |
| CN110041976B (en) * | 2019-03-15 | 2021-06-08 | 中国煤层气集团有限公司 | Gas-solid-liquid separation device |
| CN115155219A (en) * | 2022-08-22 | 2022-10-11 | 浙江洛森压缩机股份有限公司 | Gas-liquid separation sewage discharging system |
| CN115155219B (en) * | 2022-08-22 | 2023-09-08 | 浙江洛森压缩机股份有限公司 | Gas-liquid separation sewage disposal system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 453731 Xinxiang Economic Development Zone, Henan Province (Xiaoji Town) Patentee after: Henan Xinlianxin Chemical Industry Group Co.,Ltd. Address before: 453731 Henan Xinxiang Economic Development Zone Xiaoji Town Henan Xinlianxin Chemical Fertilizer Co., Ltd. Patentee before: HENAN XINLIANXIN FERTILIZER Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20150121 |