CN202270430U - Gas-liquid separator - Google Patents
Gas-liquid separator Download PDFInfo
- Publication number
- CN202270430U CN202270430U CN2011203472241U CN201120347224U CN202270430U CN 202270430 U CN202270430 U CN 202270430U CN 2011203472241 U CN2011203472241 U CN 2011203472241U CN 201120347224 U CN201120347224 U CN 201120347224U CN 202270430 U CN202270430 U CN 202270430U
- Authority
- CN
- China
- Prior art keywords
- gas
- separator
- liquid
- shell
- flow guiding
- 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.)
- Expired - Lifetime
Links
Images
Landscapes
- Separating Particles In Gases By Inertia (AREA)
- Cyclones (AREA)
Abstract
The utility model discloses a gas-liquid separator. The gas-liquid separator is characterized in that one side of the separator is provided with a gas inlet; the other side of a separator shell is provided with a liquid outlet; the top part of the separator shell is provided with a gas outlet connecting pipe; the top part of the gas outlet connecting pipe is provided with a gas outlet; the inner side of the separator shell is provided with a baffling box, a flow guiding cover, a flow guiding barrel, a baffling plate, a liquid collecting part and a streamline baffle plate; gas enters the separator shell through the baffling box at one side of the gas inlet; the upper part of the flow guiding barrel in the separator shell is provided with the flow guiding cover; the upper part of the flow guiding cover is provided with the streamline baffle plate; the lower part of the flow guiding barrel is provided with the baffling plate and the lower part of the flow guiding barrel is provided with a liquid collecting part; and one side of the liquid collecting part is provided with a liquid outlet. According to the gas-liquid separator, the resistance and the equipment investment are reduced as much as possible under the condition that liquid drops and the gas are separated efficiently.
Description
Technical field
The utility model relates to a kind of gas-liquid separator.
Background technology
In the process gas compressor operation,, inevitably can contain saturated steam and lubricating oil because of the reason of technology; Because process gas after compressing through each level, need cool off rear entering next stage and compress, and high-temperature gas is after cooling; Saturation water in the gas and lubricating oil can be changed liquid by gaseous state, if these water and oil do not separate when compressing along with gas entering next stage cylinder, can make the damage of next stage air valve and piston ring; Can cause decreasing the generation of machine accident when situation is serious; Separating efficiently is a difficult problem, if but only require separating effect efficiently, investment is increased; And can increase air resistance, increase power consumption.
The utility model content
The utility model purpose: the purpose of the utility model is in order to solve the deficiency of prior art, a kind of gas-liquid separator to be provided, make gas and liquid guarantee that drop and gas carry out reducing equipment investment under the situation of high efficiency separation as far as possible.
Technical scheme: in order to realize above purpose, the described a kind of gas-liquid separator of the utility model is characterized in that; Side from device is provided with the gas inlet port, and the side in addition of shell separator is provided with liquid outlet, and the top of shell separator is provided with outgoing gas connection tube; The top of outgoing gas connection tube is a gas vent, and the inboard of shell separator is provided with baffling box, kuppe; Guide shell, deflection plate, liquid collection portion and fairshaped baffle plate; Gas gets into shell separator through the baffling box of gas inlet port one side, and the top of the guide shell in the shell separator is provided with kuppe, and the top of kuppe is provided with fairshaped baffle plate; The bottom of guide shell is provided with deflection plate, and the bottom of guide shell is provided with liquid collection portion, and a side of liquid collection portion is provided with liquid outlet.
Liquid outlet and shell separator are fixing for welding in the utility model, take over shell separator also fixing for welding.
The operation principle of the utility model: according to centrifugal separation technology, gas gets into shell separator through the baffling box of air inlet, and gas flow rate improves; And flow along cylinder inboard wall; Drop in the gas is because centrifugal action is separated from the gas, and drop flows down along cylinder inboard wall, and after gas collides with the deflection plate of container bottom again; After the fine droplet that carried secretly itself separates, carry out next stage after coming out along outgoing gas connection tube from shell separator and compress.
Beneficial effect: the utility model compared with prior art has the following advantages:
1, make gas get into shell separator after because circulating face narrows down, flow velocity improves, and centrifugal force is increased, and has strengthened separating effect;
2, because the airflow design of the plate washer of shell separator inside makes gas when getting into shell separator,, reach optimal separating efficiency near mobile in the do rotation along wall;
3, gas flows along the liquid/gas separator housing wall, can not produce outgoing gas connection tube and impact;
4, after gas enters into the top of shell separator,, after colliding with the bottom kuppe again, make separation more thorough through centrifugation;
5, through the gas of kuppe after colliding, get into the shell separator interface of giving vent to anger, flow out shell separator, can not produce disturbance to lower liquid, guaranteed separating effect.
Description of drawings
Fig. 1 is the structural representation of the utility model.
The specific embodiment:
Below in conjunction with accompanying drawing, further illustrate the utility model.
Be illustrated in figure 1 as the structural representation of the utility model, a side of shell separator 10 is provided with gas inlet port 1, and the side in addition of shell separator 10 is provided with liquid outlet 5, and the top of shell separator 10 is provided with outgoing gas connection tube 7; The top of outgoing gas connection tube 7 is a gas vent 8, and the inboard of shell separator 10 is provided with baffling box 2, kuppe 3, guide shell 4; Deflection plate 6, liquid collection portion 9 and baffle plate 11 are behind the baffling box 2 entering shell separators 10 of gas through gas inlet port 1 one sides, because circulating face narrows down; Flow velocity improves, and centrifugal force is increased, and gas flows along the inwall that separates housing 10, and the drop in the gas is because centrifugal action is separated from the gas; Drop flows down along the inwall of guide shell 4, after gas enters into the top of shell separator 10, through centrifugation, after colliding with bottom kuppe 3 again; Make separation more thorough, streamlined because of being shaped as of the plate washer 11 of separator shell, make gas when getting into shell separator 10; Near flowing doing rotation along wall, reach optimal separating efficiency, and after gas collides with the deflection plate 6 of separator bottom again; Get into the interface 8 of giving vent to anger of shell separator 10, flow out shell separator 10, can not produce disturbance lower liquid; After having guaranteed that fine droplet that separating effect carries secretly itself separates, discharge, carry out the compression of next stage along outgoing gas connection tube 7 from shell separator.
The utility model provides a kind of gas-liquid separator, and the drop separation in the gas is effective, and is simple to operate, and cost is low, and is easy to maintenance, under the effect of high efficiency gas-liquid separation, has reduced cost greatly.
Claims (4)
1. gas-liquid separator, it is characterized in that: a side of shell separator (10) is provided with gas inlet port (1), and the side in addition of shell separator (10) is provided with liquid outlet (5); The top of shell separator (10) is provided with outgoing gas connection tube (7), and the top of outgoing gas connection tube (7) is gas vent (8), and the inboard of shell separator (10) is provided with baffling box (2); Kuppe (3); Guide shell (4), deflection plate (6), liquid collection portion (9) and baffle plate (11); Gas gets into shell separator (10) through the baffling box (2) of gas inlet port (1) one side; The top of the guide shell (4) in the shell separator (10) is provided with kuppe (3), and the top of kuppe (3) is provided with baffle plate (11), and the bottom of guide shell (4) is provided with deflection plate (6); The bottom of guide shell (4) is provided with liquid collection portion (9), and a side of liquid collection portion (9) is provided with liquid outlet (5).
2. a kind of gas-liquid separator according to claim 1 is characterized in that: described liquid outlet (5) and shell separator (10) be for being fixedly connected, and outgoing gas connection tube (7) and shell separator (10) are also for being fixedly connected.
3.
According toThe described a kind of gas-liquid separator of claim 2 is characterized in that: described liquid outlet (5) is fixing for welding with shell separator (10), and it is also fixing for welding with shell separator (10) to take over (7).
4. a kind of gas-liquid separator according to claim 1 is characterized in that: being shaped as of described baffle plate is streamlined.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203472241U CN202270430U (en) | 2011-09-16 | 2011-09-16 | Gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203472241U CN202270430U (en) | 2011-09-16 | 2011-09-16 | Gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202270430U true CN202270430U (en) | 2012-06-13 |
Family
ID=46190822
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203472241U Expired - Lifetime CN202270430U (en) | 2011-09-16 | 2011-09-16 | Gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202270430U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103691236A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Dual-layer baffle-type natural gas washing tank |
| CN103691234A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Filler-type natural gas washing tank |
| CN103691233A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Natural gas washing tank with guide plate |
| CN103691235A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Natural gas washing tank |
| CN103706211A (en) * | 2013-12-17 | 2014-04-09 | 成都展望能源机械有限公司 | Cyclone natural gas washing tank |
| CN103949118A (en) * | 2014-05-19 | 2014-07-30 | 西安航空制动科技有限公司 | CVI (chemical vapor infiltration) furnace tail gas treatment device |
| CN106440464A (en) * | 2016-12-14 | 2017-02-22 | 山东超越地源热泵科技有限公司 | Transcritical CO2 water and ground source heat pump refrigerating and heating system and heating method |
| CN110005614A (en) * | 2019-04-02 | 2019-07-12 | 章玉妹 | A kind of vacuum equipment moisture separator |
-
2011
- 2011-09-16 CN CN2011203472241U patent/CN202270430U/en not_active Expired - Lifetime
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103691233B (en) * | 2013-12-17 | 2015-11-11 | 成都展望能源机械有限公司 | There is the natural gas washing tank of deflector |
| CN103691234A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Filler-type natural gas washing tank |
| CN103691233A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Natural gas washing tank with guide plate |
| CN103691235A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Natural gas washing tank |
| CN103706211A (en) * | 2013-12-17 | 2014-04-09 | 成都展望能源机械有限公司 | Cyclone natural gas washing tank |
| CN103691236A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Dual-layer baffle-type natural gas washing tank |
| CN103691234B (en) * | 2013-12-17 | 2015-11-18 | 成都展望能源机械有限公司 | Material filling type natural gas washing tank |
| CN103706211B (en) * | 2013-12-17 | 2015-11-18 | 成都展望能源机械有限公司 | Cyclone type natural gas washing tank |
| CN103949118A (en) * | 2014-05-19 | 2014-07-30 | 西安航空制动科技有限公司 | CVI (chemical vapor infiltration) furnace tail gas treatment device |
| CN103949118B (en) * | 2014-05-19 | 2016-02-03 | 西安航空制动科技有限公司 | A kind of CVI furnace exhaust gas treating apparatus |
| CN106440464A (en) * | 2016-12-14 | 2017-02-22 | 山东超越地源热泵科技有限公司 | Transcritical CO2 water and ground source heat pump refrigerating and heating system and heating method |
| CN110005614A (en) * | 2019-04-02 | 2019-07-12 | 章玉妹 | A kind of vacuum equipment moisture separator |
| CN110005614B (en) * | 2019-04-02 | 2024-01-12 | 贝尔实验室装备江苏有限公司 | Water-gas separation device of vacuum equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202270430U (en) | Gas-liquid separator | |
| CN110747007B (en) | CO (carbon monoxide)2Gas-liquid separation device for produced fluid | |
| CN201983546U (en) | Spiral oil separator | |
| CN108424792B (en) | Integrated cooling separator and working method thereof | |
| CN104697255A (en) | Separator device for separating lubricating oil and in refrigerating system and method for oil separating | |
| CN201164765Y (en) | Wave type gas-liquid separation tank | |
| CN108671638B (en) | Rearmounted gas separator of vehicle air conditioner compressor | |
| CN201978631U (en) | Gas and water separating device | |
| CN201221469Y (en) | Oil and gas separating barrel of air compressor | |
| CN202962136U (en) | Special centrifugal type oil stain separator for compressed natural gas | |
| CN202853219U (en) | Vertical working medium gas-liquid separator | |
| CN108465301B (en) | Combined cyclone deflection large-caliber gas-liquid compound separation device of gas compressor | |
| CN102654336A (en) | Oil separator | |
| CN206988107U (en) | A kind of screw air compressor gas-oil separating cylinder | |
| CN203375773U (en) | Oil separator and air conditioner | |
| CN203175866U (en) | Oil-gas separator for oil injection screw air compressor | |
| CN212700919U (en) | Dewatering separation tank | |
| CN103398519A (en) | Vertical type oil separator | |
| CN208151316U (en) | Integrated cooling separator | |
| CN203908142U (en) | Novel gas-liquid separator for ammonia refrigeration | |
| CN206247721U (en) | Oil eliminator and use its refrigeration system | |
| CN203083226U (en) | High-efficient oil separator | |
| CN101972571A (en) | Spiral-flow type spray catcher | |
| CN201599993U (en) | Novel centrifugal type oil separator | |
| CN202177268U (en) | Oil separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120613 |