CN201988302U - Air water separating device - Google Patents
Air water separating device Download PDFInfo
- Publication number
- CN201988302U CN201988302U CN2011200230880U CN201120023088U CN201988302U CN 201988302 U CN201988302 U CN 201988302U CN 2011200230880 U CN2011200230880 U CN 2011200230880U CN 201120023088 U CN201120023088 U CN 201120023088U CN 201988302 U CN201988302 U CN 201988302U
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- air
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Abstract
The utility model relates to an air water separating device, in particular to an air water separating device of compressed air, which comprises a sealed or detachable pressure vessel casing. The air water separating device is characterized in that an air inlet pipe, an air outlet pipe, a reversed cone-shaped whirlwind blocking plate, an ellipsoid apron, an air rising pipe, an orifice plate, a screen mesh layer and a water outlet are installed in the casing. The air inlet pipe, the air outlet pipe, the whirlwind blocking plate and the water outlet are all welded to the casing, the ellipsoid apron is welded to the air rising pipe, the air rising pipe and the orifice plate are welded to the upper plane of the whirlwind blocking plate, the screen mesh layer is arranged between the orifice plate and the air outlet pipe, the air inlet pipe penetrates into the side wall in the middle of the casing close to the whirlwind blocking plate in a tangential direction, the air outlet pipe is positioned on the top of the casing or on the upper portion, and the water outlet is arranged at the bottom of the casing. The water separating device has reasonable structural design, low installation height, long service life, low airflow resistance and capability of completely separating liquid water and avoiding the phenomenon that the air outlet pipe carries water.
Description
Technical field
The utility model relates to a kind of gas and water separator, especially a kind of compressed air gas and water separator, and it mainly is applicable to compressed air separating through cooled liquid moisture and oil content.
Background technology
In the existing mature technology, be used for compressed air and remove the moisture trap that the gas and water separator of liquid moisture mainly contains cyclone separating, baffle plate silk screen combined type and the micron filter core is housed.For cyclone separating, compressed air tangentially enters separator from the pressure vessel upper pipe, and the centrifugal force that utilizes high-speed rotational to produce is realized the centrifugation of air water, but the less mist pearl of quality in can not separation bubble, separating effect is relatively poor; For baffle plate silk screen combined type separator, compressed air enters separator along air inlet pipe, be subjected to the collision of the baffle plate of inner walls direction setting earlier, be mixed in airborne water droplet viscous at baffle surface and be accumulated into the bigger drop of particle diameter at baffle edge and fall into separator bottom, a filter screen that is formed by stacking by the multilayer stainless steel cloth is passed in the air-flow rising then, and small droplet cohesion is grown up and further separated, though separating effect increases, but gas-flow resistance is big, installs highly high; For the moisture trap that the micron filter core is housed,, cost of manufacture height, service life lack, need periodic replacement (in the general 8000h), operating cost height though separating effect is better.
Summary of the invention
The purpose of this utility model be to overcome the gas-water separation that exists in the present technology not thoroughly, the air-flow resistance decreases deficiencies such as big, that production cost is high, service life is short, provide that a kind of structure is simple relatively, gas-water separation thoroughly, resistance decrease less, cost reasonable, the compressed air gas and water separator of long service life.
The utility model solves the problems of the technologies described above the technical scheme that is adopted: a kind of compressed air gas and water separator, it comprises housing, housing is a sealing or removable pressure vessel, it is characterized in that: air inlet pipe is housed on the housing, escape pipe, discharge outlet, turbination whirlwind baffle plate is housed in the housing, the ellipsoid shirt rim, riser, homogenizing plate, silk screen layer, silk screen layer, the whirlwind baffle plate welds with inner walls respectively, ellipsoid shirt rim and riser welding, riser, plane welding on homogenizing plate and the whirlwind baffle plate, silk screen layer is located between homogenizing plate and the escape pipe, air inlet pipe tangentially enters housing middle part sidewall near whirlwind baffle plate place, escape pipe is located at case top or top, and discharge outlet is located at housing bottom.
The compressed air of carrying a large amount of drop liquid mists secretly tangentially enters gas-liquid separator along air inlet pipe, produce the high speed swirling eddy in the interlayer between turbination whirlwind baffle plate, riser, ellipsoid shirt rim and inner walls, fine droplet be accumulated into bigger drop along inner walls and ellipsoid shirt rim outer surface to falling into housing bottom, have only the less drop of fraction particle diameter to be taken away by air-flow.This part remaining small particle diameter water droplet then with air communication cross riser, homogenizing plate enters silk screen layer, under the descending centrifugation layer by layer of the silk screen of different meshes, drop is grown up and is overcome airflow lifting force, falls into housing bottom along housing, whirlwind baffle plate and riser inwall.Dried compressed air after the separation enters escape pipe by case top or top after leaving silk screen layer again, and big water gaging, oil and the impurity separated are then discharged by discharge outlet.
The utility model compared with prior art, have the following advantages: 1, reasonable in design, the setting of ellipsoid shirt rim further improves the effect of cyclonic separation, being used in combination of whirlwind baffle plate and homogenizing plate, air-flow is uniformly dispersed, and the effect that silk screen separates gets a promotion, and can prevent that the escape pipe water phenomenon from taking place, comprehensive separating effect is better, and has controlled height of devices; 2, device integral body is a center steering body structure, and the air-flow resistance is decreased less; 3, simple in structure, cost is lower, and no operating cost is easy to maintenance.
Description of drawings
Accompanying drawing 1 is a kind of structural representation of the present utility model.
The specific embodiment
Below by embodiment, and in conjunction with the accompanying drawings, the technical solution of the utility model is described in further detail.
Embodiment: accompanying drawing 1 is a kind of structural representation of the present utility model.
A kind of compressed air gas and water separator, it comprises housing 8, housing 8 is a sealing or removable pressure vessel, it is characterized in that: air inlet pipe 5 is housed on the housing 8, escape pipe 1, discharge outlet 9, turbination whirlwind baffle plate 4 is housed in the housing 8, ellipsoid shirt rim 7, riser 6, homogenizing plate 3, silk screen layer 2, silk screen layer 2, whirlwind baffle plate 4 welds with housing 8 inwalls respectively, ellipsoid shirt rim 7 and riser 6 welding, riser 6, plane welding on homogenizing plate 3 and the whirlwind baffle plate 4, silk screen layer 2 is located between homogenizing plate 3 and the escape pipe 1, air inlet pipe 5 tangentially enters housing 8 middle part sidewalls near whirlwind baffle plate 4 places, escape pipe 1 is located at housing 8 tops or top, and discharge outlet 9 is located at housing 8 bottoms.
The compressed air of carrying a large amount of drop liquid mists secretly tangentially enters gas-liquid separator along air inlet pipe 5, produce the high speed swirling eddy in the interlayer between turbination whirlwind baffle plate 4, riser 6, ellipsoid shirt rim 7 and housing 8 inwalls, fine droplet be accumulated into bigger drop along housing 8 inwalls and ellipsoid shirt rim 7 outer surfaces to falling into housing 8 bottoms, have only the less drop of fraction particle diameter to be taken away by air-flow.This part remaining small particle diameter water droplet then with air communication cross riser 6, homogenizing plate 3 enters silk screen layer 2, under the descending centrifugation layer by layer of the silk screen of different meshes, drop is grown up and is overcome airflow lifting force, falls into housing 8 bottoms along housing 8, whirlwind baffle plate 4 and riser 6 inwalls.Dried compressed air after the separation enters escape pipe 1 by housing 8 tops or top after leaving silk screen layer 2 again, and big water gaging, oil and the impurity of separating is then discharged by discharge outlet 9.
This novel gas and water separator can separate liquid moisture fully, and air-flow resistance is decreased little, simple in structure, and cost is lower and do not have operating cost.
Claims (1)
1. compressed air gas and water separator, it comprises housing, housing is a sealing or removable pressure vessel, it is characterized in that: air inlet pipe is housed on the housing, escape pipe, discharge outlet, turbination whirlwind baffle plate is housed in the housing, the ellipsoid shirt rim, riser, homogenizing plate, silk screen layer, silk screen layer, the whirlwind baffle plate welds with inner walls respectively, ellipsoid shirt rim and riser welding, riser, plane welding on homogenizing plate and the whirlwind baffle plate, silk screen layer is located between homogenizing plate and the escape pipe, air inlet pipe tangentially enters housing middle part sidewall near whirlwind baffle plate place, and escape pipe is located at case top or top, and discharge outlet is located at housing bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200230880U CN201988302U (en) | 2011-01-25 | 2011-01-25 | Air water separating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200230880U CN201988302U (en) | 2011-01-25 | 2011-01-25 | Air water separating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201988302U true CN201988302U (en) | 2011-09-28 |
Family
ID=44664807
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200230880U Expired - Fee Related CN201988302U (en) | 2011-01-25 | 2011-01-25 | Air water separating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201988302U (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103157332A (en) * | 2013-03-27 | 2013-06-19 | 中国石油天然气集团公司 | Filter |
| CN103240192A (en) * | 2013-04-23 | 2013-08-14 | 华东理工大学 | Combined structure type efficient hydrocyclone used for potassium fertilizer production |
| CN103331069A (en) * | 2013-01-23 | 2013-10-02 | 厦门美时美克空气净化有限公司 | An efficient air filtration and dehumidification device |
| 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 |
| CN104524798A (en) * | 2015-01-18 | 2015-04-22 | 丁武轩 | Continuous evaporation and crystallization device and method capable of saving energy by mechanical steam recompression |
| CN104548651A (en) * | 2015-01-19 | 2015-04-29 | 陈式好 | Industrial grade energy-saving and water-saving type MVR (mechanical vapor recompression) continuous evaporative crystallization system |
| CN105435564A (en) * | 2015-11-16 | 2016-03-30 | 滁州市博康模具塑料有限公司 | Oil-water separation device special for portable injection molding machine |
| CN105972575A (en) * | 2016-06-30 | 2016-09-28 | 无锡太湖锅炉有限公司 | Vertical type end cover type steam separator of once-through boiler |
| CN110327746A (en) * | 2019-08-15 | 2019-10-15 | 安徽铜冠有色金属（池州）有限责任公司 | A kind of compressed air de-watering apparatus |
| CN111249236A (en) * | 2020-01-20 | 2020-06-09 | 长沙一加一生物科技有限公司 | Preparation method and preparation device of insoluble special medical food powder for reducing high blood pressure, high blood sugar and high blood sugar |
| CN114288794A (en) * | 2021-12-31 | 2022-04-08 | 深圳市家家分类环保技术开发有限公司 | Garbage vacuum evaporation steam dust removal device |
-
2011
- 2011-01-25 CN CN2011200230880U patent/CN201988302U/en not_active Expired - Fee Related
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103331069A (en) * | 2013-01-23 | 2013-10-02 | 厦门美时美克空气净化有限公司 | An efficient air filtration and dehumidification device |
| CN103331069B (en) * | 2013-01-23 | 2016-05-04 | 厦门美时美克空气净化有限公司 | A kind of high-efficiency air filtering dehydrating unit |
| CN103157332A (en) * | 2013-03-27 | 2013-06-19 | 中国石油天然气集团公司 | Filter |
| CN103240192B (en) * | 2013-04-23 | 2016-03-16 | 华东理工大学 | A kind of high-efficiency hydraulic swirler for combining structure in potash fertilizer production |
| CN103240192A (en) * | 2013-04-23 | 2013-08-14 | 华东理工大学 | Combined structure type efficient hydrocyclone used for potassium fertilizer production |
| 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 |
| 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 |
| CN104524798A (en) * | 2015-01-18 | 2015-04-22 | 丁武轩 | Continuous evaporation and crystallization device and method capable of saving energy by mechanical steam recompression |
| CN104524798B (en) * | 2015-01-18 | 2016-06-08 | 丁武轩 | The continuous evaporative crystallization device of function of mechanical steam recompression and continuous evaporative crystallization method |
| CN104548651A (en) * | 2015-01-19 | 2015-04-29 | 陈式好 | Industrial grade energy-saving and water-saving type MVR (mechanical vapor recompression) continuous evaporative crystallization system |
| CN105435564A (en) * | 2015-11-16 | 2016-03-30 | 滁州市博康模具塑料有限公司 | Oil-water separation device special for portable injection molding machine |
| CN105972575A (en) * | 2016-06-30 | 2016-09-28 | 无锡太湖锅炉有限公司 | Vertical type end cover type steam separator of once-through boiler |
| CN110327746A (en) * | 2019-08-15 | 2019-10-15 | 安徽铜冠有色金属（池州）有限责任公司 | A kind of compressed air de-watering apparatus |
| CN111249236A (en) * | 2020-01-20 | 2020-06-09 | 长沙一加一生物科技有限公司 | Preparation method and preparation device of insoluble special medical food powder for reducing high blood pressure, high blood sugar and high blood sugar |
| CN114288794A (en) * | 2021-12-31 | 2022-04-08 | 深圳市家家分类环保技术开发有限公司 | Garbage vacuum evaporation steam dust removal device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: HANGZHOU ULTRAFILTRATION INDUSTRY CO., LTD. Free format text: FORMER OWNER: HANGZHOU UNION ULTRAFILTRATION PURIFICATION EQUIPMENT CO., LTD. Effective date: 20131104 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20131104 Address after: Hangzhou City, Zhejiang province 311122 Yuhang District Xianlin Street Xian Xing Road No. 10-3 Patentee after: Hangzhou ultrafiltration Industry Co Ltd Address before: Yuhang District of Hangzhou City, Zhejiang Province, 311122 enterprises Zhenjia Xian Lin Road No. 19 Patentee before: Hangzhou United Ultrafiltration Purification Equipment Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110928 Termination date: 20150125 |
|
| EXPY | Termination of patent right or utility model |