CN201394406Y - High-efficiency combined-type gas-liquid separator - Google Patents
High-efficiency combined-type gas-liquid separator Download PDFInfo
- Publication number
- CN201394406Y CN201394406Y CN2009200848053U CN200920084805U CN201394406Y CN 201394406 Y CN201394406 Y CN 201394406Y CN 2009200848053 U CN2009200848053 U CN 2009200848053U CN 200920084805 U CN200920084805 U CN 200920084805U CN 201394406 Y CN201394406 Y CN 201394406Y
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- Prior art keywords
- gas
- liquid separator
- air
- cyclone type
- type gas
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- Expired - Fee Related
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Separating Particles In Gases By Inertia (AREA)
- Cyclones (AREA)
Abstract
A high-efficiency combined-type gas-liquid separator is characterized in that a whirlwind-type gas-liquid separator (17), a tubebank-type air water charge air cooler (18) and a high-efficiency anti-foam spray catcher (19); an air inlet (1) is directly communicated into a spiral gas-guide tube (7) of the whirlwind-type gas-liquid separator (17); and gas circuits of the whirlwind-type gas-liquid separator (17), the tubebank-type air water charge air cooler (18) and the high-efficiency anti-foam spray catcher (19) are communicated in sequence. The utility model relates to a high-efficiency fuel gas purifying treatment device, which has the advantages of polyfunctional functions of cooling, dust removal, dehydration, voltage stabilization, gas storage and the like, low cost and convenient installation, is suitable for purifying various fuel gas and compressed air such as biomass gasification gas, marsh gas, landfill gas, methane gas, coke oven gas, natural gas and the like, and can remove95 to 99 percent of dust and moisture in the fuel gas and the compressed air; moreover, the particle size of dust in the finished gas is less than or equal to 5um, and the moisture content thereof isless than or equal to 10ppm.
Description
Technical field
The utility model relates to a kind of gas-liquid separator, is the integrated efficient composite gas-liquid separator of a kind of height specifically.
Background technology
Gas-liquid separator has following several from the principle branch at present: 1, rotational flow separation; 2, baffling separates; 3, silk screen separates; 4, filler separates; 5, gravity settling separation; 6, ultra-filtration and separation.What usually run in the industry is to use monotechnics, or several isolation technics successively connects, makes up by different equipment, and function singleness, cost height, separative efficiency is low, volume is big, the installation and maintenance complexity.
Summary of the invention
The purpose of this utility model provides a kind of efficient composite gas-liquid separator that collects cooling, dedusting, dehydration, voltage stabilizing, gas storage one.
Described efficient composite gas-liquid separator, the gas-liquid separation treating column that comprises belt supporting frame, in the gas-liquid separation treating column, establish the cyclone type gas-liquid separator, it is characterized in that: shell and tube air water charge air cooler also is installed in the gas-liquid separation treating column, efficient broken foam mist eliminator, this tertiary treatment device erection sequence from the bottom to top is: the cyclone type gas-liquid separator, shell and tube air water charge air cooler, efficient broken foam mist eliminator, air inlet directly is communicated in the spiral air-conducting pipe of cyclone type gas-liquid separator, the cyclone type gas-liquid separator, shell and tube air water charge air cooler, the gas circuit of efficient broken foam mist eliminator is communicated with successively, and air-flow is finally discharged from the gas outlet at top through the pressure stabilizing chamber of gas-liquid separation treating column.
Body of the tower at the gas-liquid separation treating column also is provided with cooling water inlet pipe and cooling water outlet pipe, cooling water inlet pipe and cooling water outlet pipe be communicated to the gas-liquid separation shell with in cold heat exchanger tube surround in the shell and tube air water charge air cooler cavity that forms.
The anti-rotating plate in spiral air-conducting road is housed in the spiral air-conducting pipe of described cyclone type gas-liquid separator, establishes condensate draining pipe in the lower end of described cyclone type gas-liquid separator.
Described cyclone type gas-liquid separator, shell and tube air water charge air cooler, efficiently broken foam mist eliminator, pressure stabilizing chamber adopt the modularization splicing structure.
The utlity model has multi-functional, low costs such as cooling, dedusting, dehydration, voltage stabilizing, gas storage, high efficiency burnt gas purification apparatus easily is installed, be applicable to multiple fuel gas and compressed-air actuated purifications such as biomass gasified gas, biogas, rubbish landfill gas, Device in Gas, coke-stove gas, natural gas, can remove in combustion gas and the compressed air 95～99% dust and moisture, dust particle diameter≤5um in the finished product gas, water content≤10ppm.
Can prolong the time between overhauls(TBO) (normally not having more than three times of supporting this cleaning system) of fuel gas generation unit and other gas equipment when being used for gas electricity generator greatly; reduce and shut down the maintenance number of times; alleviate power plant operation attendant's labour intensity; reduce the replacing quantity of accessories such as spark plug, thereby improve power station integrated economic benefit greatly.
Description of drawings
Fig. 1 is the utility model structural representation.
Among the figure: 1-air inlet, 2-gas outlet, 3-pressure stabilizing chamber, 4-gas barrier, the 5-support, 6-condensate draining pipe, 7-spiral air-conducting pipe, the efficient demister filter core assembly of 8-, 9-cooling water inlet pipe, 10-cooling water outlet pipe, cold heat exchanger tube among the 11-, liner plate under the 12-spiral air-conducting road, liner plate on the 13-spiral air-conducting road, the 14-ring flange, 15-spiral air-conducting road central tube, rotating plate is prevented in 16-spiral air-conducting road, the efficiently broken foam mist eliminator of 17-cyclone type gas-liquid separator, 18-shell and tube air water charge air cooler, 19-.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is further specified: efficient composite gas-liquid separator as shown in fig. 1, the gas-liquid separation treating column that comprises belt supporting frame 5, in the gas-liquid separation treating column, establish cyclone type gas-liquid separator 17, shell and tube air water charge air cooler 18 also is installed in the gas-liquid separation treating column, efficient broken foam mist eliminator 19, this tertiary treatment device erection sequence from the bottom to top is: cyclone type gas-liquid separator 17, shell and tube air water charge air cooler 18, efficient broken foam mist eliminator 19, air inlet 1 directly is communicated in the spiral air-conducting pipe 7 of cyclone type gas-liquid separator 17, cyclone type gas-liquid separator 17, shell and tube air water charge air cooler 18, the gas circuit of efficient broken foam mist eliminator 19 is communicated with successively, and air-flow is finally discharged from the gas outlet 2 at top through the pressure stabilizing chamber 3 of gas-liquid separation treating column.
As we can see from the figure, pending gas enters spiral air-conducting pipe 7 from air inlet 1 with high pressure, and around spiral air-conducting road central tube 15 formation eddy flows, with in the gas with moisture because action of centrifugal force is thrown to the moisture collecting net of spiral air-conducting pipe 7 inwalls, the anti-rotating plate 16 in spiral air-conducting road is housed in the spiral air-conducting pipe 7 of described cyclone type gas-liquid separator 17, part moisture when the anti-rotating plate 16 in spiral air-conducting road slows down for air-flow in the interception air-flow, establish condensate draining pipe 6 in the lower end of described cyclone type gas-liquid separator 17, moisture is in time discharged from the condensate draining pipe 6 of cyclone type gas-liquid separator 17 lower ends, air-flow is through reduction of speed, centrifugal, collision, slow down, processes such as cohesion, remove the liquid moisture content in the Compressed Gas, reach the effect of purification.
Air-flow is from the cyclone type gas-liquid separator 17 laggard shell and tube air water charge air cooler 18 of going into that comes out, body of the tower at the gas-liquid separation treating column is provided with cooling water inlet pipe 9 and cooling water outlet pipe 10, cooling water the gas-liquid separation shell with in cold heat exchanger tube 11 surround in shell and tube air water charge air cooler 18 cavitys that form from bottom to top and flow, the gas that contains vaporous water is met condensation during cold heat exchanger tube 11 and is formed liquid water droplets in flowing through, fall under gravity into the gas-liquid separation tower bottom, air-flow is therein through fully cooling, it is further dry that gas after the cooling enters the efficient demister filter core assembly 8 of efficient broken foam mist eliminator 19, and wherein minute water vapour particle is filtered.
Last gas is by the clean gas of pressure stabilizing chamber 3 back formation pressure stabilitys, drying, and 2 discharge from the gas outlet, enter next step operation.Finish multiple functions such as the utility model cooling, dedusting, dehydration, voltage stabilizing, gas storage.
Described cyclone type gas-liquid separator 17, shell and tube air water charge air cooler 18, efficiently broken foam mist eliminator 19, pressure stabilizing chamber 3 adopt the modularization splicing structure.Maintenance, assembly unit is simple and efficient.
Claims (4)
1. efficient composite gas-liquid separator, the gas-liquid separation treating column that comprises belt supporting frame, in the gas-liquid separation treating column, establish the cyclone type gas-liquid separator, it is characterized in that: shell and tube air water charge air cooler (18) also is installed in the gas-liquid separation treating column, efficient broken foam mist eliminator (19), this tertiary treatment device erection sequence from the bottom to top is: cyclone type gas-liquid separator (17), shell and tube air water charge air cooler (18), efficient broken foam mist eliminator (19), air inlet (1) directly is communicated in the spiral air-conducting pipe (7) of cyclone type gas-liquid separator (17), cyclone type gas-liquid separator (17), shell and tube air water charge air cooler (18), the gas circuit of efficient broken foam mist eliminator (19) is communicated with successively, and air-flow finally passes through the pressure stabilizing chamber (3) of gas-liquid separation treating column and discharges from the gas outlet (2) at top.
2. efficient composite gas-liquid separator according to claim 1, it is characterized in that: the body of the tower at the gas-liquid separation treating column also is provided with cooling water inlet pipe (9) and cooling water outlet pipe (10), cooling water inlet pipe (9) and cooling water outlet pipe (10) be communicated to the gas-liquid separation shell with in cold heat exchanger tube (11) surround in shell and tube air water charge air cooler (18) cavity that forms.
3. efficient composite gas-liquid separator according to claim 1, it is characterized in that: the anti-rotating plate (16) in spiral air-conducting road is housed in the spiral air-conducting pipe (7) of described cyclone type gas-liquid separator (17), establishes condensate draining pipe (6) in the lower end of described cyclone type gas-liquid separator (17).
4. efficient composite gas-liquid separator according to claim 1 is characterized in that: described cyclone type gas-liquid separator (17), shell and tube air water charge air cooler (18), efficiently broken foam mist eliminator (19), pressure stabilizing chamber (3) adopt the modularization splicing structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200848053U CN201394406Y (en) | 2009-04-09 | 2009-04-09 | High-efficiency combined-type gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200848053U CN201394406Y (en) | 2009-04-09 | 2009-04-09 | High-efficiency combined-type gas-liquid separator |
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| Publication Number | Publication Date |
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| CN201394406Y true CN201394406Y (en) | 2010-02-03 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2009200848053U Expired - Fee Related CN201394406Y (en) | 2009-04-09 | 2009-04-09 | High-efficiency combined-type gas-liquid separator |
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| CN (1) | CN201394406Y (en) |
Cited By (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102296979A (en) * | 2010-06-22 | 2011-12-28 | 武汉高科佳诚动力科技有限公司 | Dedusting and dehydrating process of deep condensation to gas by utilizing natural cold source |
| CN102489101A (en) * | 2011-12-23 | 2012-06-13 | 青岛京润石化设计研究院有限公司 | Gas-liquid separator |
| CN102517091A (en) * | 2011-12-15 | 2012-06-27 | 洛阳骏腾能源科技有限公司 | Counter combustion-type pyrolysis gasification equipment for biomass waste resources |
| CN102671470A (en) * | 2012-05-23 | 2012-09-19 | 浙江大学 | Efficient gas-liquid separator |
| CN102690689A (en) * | 2012-06-08 | 2012-09-26 | 神华集团有限责任公司 | Device and method for scrubbing and purifying coal gas |
| CN103275761A (en) * | 2013-06-25 | 2013-09-04 | 朱清敏 | Method and device for manufacturing chemical virgin gas with solid organic materials |
| CN103410495A (en) * | 2013-07-15 | 2013-11-27 | 淮南矿业(集团)有限责任公司 | Gas-water separator with automatic cooling function |
| CN103861428A (en) * | 2014-01-01 | 2014-06-18 | 施健 | Tubular absorption tower plate |
| CN104034103A (en) * | 2014-07-01 | 2014-09-10 | 吉首大学 | Novel ammonia refrigeration intercooler |
| CN104492177A (en) * | 2014-12-25 | 2015-04-08 | 江阴中南重工股份有限公司 | Separator |
| CN104587805A (en) * | 2015-01-08 | 2015-05-06 | 张文良 | Cyclone gas drier |
| CN104989383A (en) * | 2015-07-08 | 2015-10-21 | 淮南矿业(集团)有限责任公司 | Gas pressure measuring device and gas pressure measuring system |
| CN105038888A (en) * | 2015-08-15 | 2015-11-11 | 重庆联合机器制造有限公司 | Natural gas second-stage gas-liquid separator |
| CN106492544A (en) * | 2016-11-28 | 2017-03-15 | 西安长庆科技工程有限责任公司 | A kind of spiral-flow type combines gas liquid high-efficiency segregation apparatuss |
| CN109442434A (en) * | 2018-10-22 | 2019-03-08 | 广州顺途信息科技有限公司 | For incineration firing tail gas de-watering apparatus |
| CN110005614A (en) * | 2019-04-02 | 2019-07-12 | 章玉妹 | A kind of vacuum equipment moisture separator |
| CN110575738A (en) * | 2019-10-14 | 2019-12-17 | 中国沈阳晶鑫环保科技有限公司 | comprehensive dehydration method for wet flue gas |
| CN110614015A (en) * | 2018-06-19 | 2019-12-27 | 英格索尔-兰德公司 | Gas-water separation system and method |
| CN110846084A (en) * | 2019-11-29 | 2020-02-28 | 北京航天迈未科技有限公司 | Dust separation and recovery equipment and method |
| CN110923027A (en) * | 2019-12-19 | 2020-03-27 | 珠海巨涛海洋石油服务有限公司 | Natural gas dehydration device |
| CN112807926A (en) * | 2021-01-05 | 2021-05-18 | 长沙有色冶金设计研究院有限公司 | Hydrometallurgy tail gas washing device and method |
| CN112870901A (en) * | 2021-01-28 | 2021-06-01 | 福建德尔科技有限公司 | Novel aqueous vapor autosegregation device |
| CN113617182A (en) * | 2021-08-27 | 2021-11-09 | 浙江新创兴科技有限公司 | Waste gas treatment equipment and method |
| WO2022017183A1 (en) * | 2020-07-20 | 2022-01-27 | 约克（无锡）空调冷冻设备有限公司 | Gas-liquid separator |
| CN116654469A (en) * | 2023-05-08 | 2023-08-29 | 江苏立业环境科技有限公司 | Buffer tank with self-cleaning function for pressure container |
-
2009
- 2009-04-09 CN CN2009200848053U patent/CN201394406Y/en not_active Expired - Fee Related
Cited By (36)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102296979B (en) * | 2010-06-22 | 2013-09-25 | 武汉高科佳诚动力科技有限公司 | Dedusting and dehydrating process of deep condensation to gas by utilizing natural cold source |
| CN102296979A (en) * | 2010-06-22 | 2011-12-28 | 武汉高科佳诚动力科技有限公司 | Dedusting and dehydrating process of deep condensation to gas by utilizing natural cold source |
| CN102517091B (en) * | 2011-12-15 | 2014-09-24 | 洛阳骏腾能源科技有限公司 | Counter combustion-type pyrolysis gasification equipment for biomass waste resources |
| CN102517091A (en) * | 2011-12-15 | 2012-06-27 | 洛阳骏腾能源科技有限公司 | Counter combustion-type pyrolysis gasification equipment for biomass waste resources |
| CN102489101A (en) * | 2011-12-23 | 2012-06-13 | 青岛京润石化设计研究院有限公司 | Gas-liquid separator |
| CN102489101B (en) * | 2011-12-23 | 2013-12-25 | 青岛京润石化设计研究院有限公司 | Gas-liquid separator |
| CN102671470A (en) * | 2012-05-23 | 2012-09-19 | 浙江大学 | Efficient gas-liquid separator |
| CN102690689A (en) * | 2012-06-08 | 2012-09-26 | 神华集团有限责任公司 | Device and method for scrubbing and purifying coal gas |
| CN102690689B (en) * | 2012-06-08 | 2013-12-04 | 神华集团有限责任公司 | Device and method for scrubbing and purifying coal gas |
| CN103275761A (en) * | 2013-06-25 | 2013-09-04 | 朱清敏 | Method and device for manufacturing chemical virgin gas with solid organic materials |
| CN103410495B (en) * | 2013-07-15 | 2016-08-10 | 淮南矿业(集团)有限责任公司 | There is the moisture trap from cooling function |
| CN103410495A (en) * | 2013-07-15 | 2013-11-27 | 淮南矿业(集团)有限责任公司 | Gas-water separator with automatic cooling function |
| CN103861428A (en) * | 2014-01-01 | 2014-06-18 | 施健 | Tubular absorption tower plate |
| CN104034103A (en) * | 2014-07-01 | 2014-09-10 | 吉首大学 | Novel ammonia refrigeration intercooler |
| CN104034103B (en) * | 2014-07-01 | 2016-07-13 | 吉首大学 | Ammonia refrigeration intercooler |
| CN104492177A (en) * | 2014-12-25 | 2015-04-08 | 江阴中南重工股份有限公司 | Separator |
| CN104587805A (en) * | 2015-01-08 | 2015-05-06 | 张文良 | Cyclone gas drier |
| CN104989383A (en) * | 2015-07-08 | 2015-10-21 | 淮南矿业(集团)有限责任公司 | Gas pressure measuring device and gas pressure measuring system |
| CN105038888A (en) * | 2015-08-15 | 2015-11-11 | 重庆联合机器制造有限公司 | Natural gas second-stage gas-liquid separator |
| CN106492544A (en) * | 2016-11-28 | 2017-03-15 | 西安长庆科技工程有限责任公司 | A kind of spiral-flow type combines gas liquid high-efficiency segregation apparatuss |
| CN110614015A (en) * | 2018-06-19 | 2019-12-27 | 英格索尔-兰德公司 | Gas-water separation system and method |
| CN109442434A (en) * | 2018-10-22 | 2019-03-08 | 广州顺途信息科技有限公司 | For incineration firing tail gas de-watering apparatus |
| 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 |
| CN110575738B (en) * | 2019-10-14 | 2021-12-03 | 中国沈阳晶鑫环保科技有限公司 | Comprehensive dehydration method for wet flue gas |
| CN110575738A (en) * | 2019-10-14 | 2019-12-17 | 中国沈阳晶鑫环保科技有限公司 | comprehensive dehydration method for wet flue gas |
| CN110846084A (en) * | 2019-11-29 | 2020-02-28 | 北京航天迈未科技有限公司 | Dust separation and recovery equipment and method |
| CN110846084B (en) * | 2019-11-29 | 2024-03-12 | 北京航天迈未科技有限公司 | Dust separation and recovery equipment and method |
| CN110923027B (en) * | 2019-12-19 | 2021-01-19 | 珠海巨涛海洋石油服务有限公司 | Natural gas dehydration device |
| CN110923027A (en) * | 2019-12-19 | 2020-03-27 | 珠海巨涛海洋石油服务有限公司 | Natural gas dehydration device |
| WO2022017183A1 (en) * | 2020-07-20 | 2022-01-27 | 约克（无锡）空调冷冻设备有限公司 | Gas-liquid separator |
| CN112807926A (en) * | 2021-01-05 | 2021-05-18 | 长沙有色冶金设计研究院有限公司 | Hydrometallurgy tail gas washing device and method |
| CN112870901A (en) * | 2021-01-28 | 2021-06-01 | 福建德尔科技有限公司 | Novel aqueous vapor autosegregation device |
| CN113617182A (en) * | 2021-08-27 | 2021-11-09 | 浙江新创兴科技有限公司 | Waste gas treatment equipment and method |
| CN116654469A (en) * | 2023-05-08 | 2023-08-29 | 江苏立业环境科技有限公司 | Buffer tank with self-cleaning function for pressure container |
| CN116654469B (en) * | 2023-05-08 | 2023-10-20 | 江苏立业环境科技有限公司 | Buffer tank with self-cleaning function for pressure container |
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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: WUHAN GAOKE JIACHENG POWER SCIENCE CO., LTD. Free format text: FORMER OWNER: HUBEI JIACHENG POWER SCIENCE CO., LTD. Effective date: 20100108 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20100108 Address after: Xu Dong Lu Hubei Harbourside city of Wuhan province Wuchang District 1 building room 604, zip code: 430060 Patentee after: Wuhan Gaoke Jiacheng Power Technology Co., Ltd. Address before: Liuhe Industrial Park, hi tech Development Zone, Hubei, Xiaogan Province, China: 432100 Patentee before: Hubei Jiacheng Power Science and Technology Co., Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100203 Termination date: 20180409 |