CN102921570A - Gas-liquid separator with internal condensation - Google Patents
Gas-liquid separator with internal condensation Download PDFInfo
- Publication number
- CN102921570A CN102921570A CN2011102307472A CN201110230747A CN102921570A CN 102921570 A CN102921570 A CN 102921570A CN 2011102307472 A CN2011102307472 A CN 2011102307472A CN 201110230747 A CN201110230747 A CN 201110230747A CN 102921570 A CN102921570 A CN 102921570A
- Authority
- CN
- China
- Prior art keywords
- gas
- cyclone separator
- condenser
- condensation
- liquid separator
- 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.)
- Pending
Links
Images
Landscapes
- Cyclones (AREA)
Abstract
The invention relates to the chemical engineering field, and discloses a gas-liquid separator with internal condensation. The structure of the gas-liquid separator comprises a cyclone separator and an internal condenser fixed in the cyclone separator, wherein the internal condenser is cylindrical in shape, and the surface of the external cylinder of the internal condenser is fixed with spiral fins; the cylinder of the internal condenser is provided with a cooling water inlet and a cooling water return outlet; the upper portion of the cylinder of the cyclone separator is provided with a gas inlet; the top of the cyclone separator is provided with a gas outlet communicated with the inner chamber of the condenser; and the bottom of the cyclone separator is provided with a tapered baffle plate. The uncondensed gas tangentially enters the cyclone separator along the pipeline of the gas inlet and undergoes surface heat exchange by the spiral fins welded on the surface of the external cylinder of the internal condenser, and condensed components having low dew points flow in the direction of the rotary gas flow, and are enriched on the internal surface of the cylinder of the cyclone separator. The gas-liquid separator has a simple structure, and can be used for the condensing separation of gases which contain a tiny amount of liquid drops or can be condensed into drops.
Description
Technical field
The present invention relates to chemical field, be specially a kind of gas-liquid separator, especially with the gas-liquid separator of internal condensation, be specially adapted to the gas-liquid separation of vacuum tail gas.
Background technology
Be negative-pressure operation at petrochemical industry and coal tar chemical field considerable part destilling tower, evaporimeter, top gaseous phase vacuumizes through vavuum pump and reaches the desired pressure condition of technique.The whereabouts of vacuum tail gas mainly contains following two kinds at present: arrange atmosphere and advance the heating furnace burning.The discharging atmosphere will improve the concentration of device periphery volatile organic matter VOCs, to environment; Advance heating furnace then as in recent years using more a kind of technological means, can be when eliminating or reducing vacuum tail gas and pollute Substitute For Partial coal gas or other fuel, have environmental protection and energy-conservation double meaning, have widely promotional value.
But; vacuum tail gas generally behind cat head, condenser or backflash tail gas bleed; since the general temperature of the process gas of extracting out higher; cooling can make portion gas be condensed into drop from vavuum pump toward the heating furnace course of conveying; to cause the problems such as heating furnace is unstable, over-emitting black exhaust after entering heating furnace, all unfavorable to device production and environmental protection.
Therefore, if a kind of gas-liquid separator with internal condensation function can be arranged, can be before vacuum tail gas enters heating furnace to composition condensation that wherein dew point is lower and reclaim condensate liquid, problem has good effect to solving as above.
Gas-liquid separation equipment, Cyclonic separating apparatus all are widely used, but have no at present cyclone separating and with the gas-liquid separation device of internal condensation device.
Summary of the invention
The present invention aims to provide a kind of gas-liquid separator, can be used for drop or easily is condensed into the condensation separation of the gas that drips.
Structure comprises cyclone separator and is fixed on the interior inner condenser of cyclone separator; Inner condenser can be connected with the cyclone separator housing by welding or flange;
Cyclone separator cylindrical shell top connects gas feed, and the cyclone separator bottom is provided with conical baffled; Conical baffledly be fixed on cyclone separator bottom by conical baffled support bar;
Inner condenser is tubular, fixing helical fin on the surface of the outside cylindrical shell of inner condenser, and helical fin is fixed on the outside cylindrical shell of inner condenser by the mode of welding, and the angle of helical fin backspin is consistent with the inclination angle of tangential admission;
Be respectively equipped with the outlet of cooling water inlet and cooling water backwater on the cylindrical shell of inner condenser; Looping cooling water flow circulation passage between the inner and outer wall of inner condenser; Deflection plate is fixed in the inner condenser circular passage, leaves the space between lower end and the condenser bottom; Deflection plate separates the annular cooling water circulation passage, prevents that cooling water is at the passage internal short-circuit; Cooling water inlet and cooling backwater outlet lay respectively at the two ends of deflection plate line;
The cyclone separator top arranges gas vent, and gas vent is communicated with the condenser inner chamber.
The cyclone separator bottom is the inverted U fluid-tight.
Gas feed is connected to the import of heating furnace vacuum tail gas burning pipeline, and the inverted U fluid-tight is connected to device waste oil groove or corresponding waste oil reclaimer.
During use, respectively cooling water pipeline and CWR road are connected to cooling water inlet and the outlet of cooling water backwater, for equipment provides cold; Vavuum pump or other gas are connected to gas feed, make tangential and downward-sloping the entering of gas; Gas vent is connected to the import of heating furnace vacuum tail gas burning pipeline, and the inverted U fluid-tight is connected to device waste oil groove or corresponding waste oil reclaimer.
After each interface all connects complete and comes into operation, uncondensed gas is along the pipeline cutting of gas feed to entering in the cyclone separator, helical fin surface heat exchanging through the welding of inner condenser outer barrel surface, after the lower composition condensation of dew point, along with the swirling eddy direction downwards in the enrichment of cyclone separator shell inner surface, and drop to the liquid collection zone of cyclone separator bottom along wall; Conical baffled gradient can make conical baffled upper liquid flow into liquid collection zone along the gradient, can prevent also that simultaneously the liquid that has accumulated in the liquid collection zone from being taken out of by uprising gas again; Condensation has also been removed the gas behind the drop and has been separated through cyclone separator, leaves from gas vent.External inverted U fluid-tight prevents that liquid is from the bottom short circuit.
Modern design of the present invention is reasonable, simple in structure, is convenient to settle.Can effectively solve vacuum tail gas and in course of conveying, lower the temperature so that portion gas is condensed into drop, so gas enters the stokehold and contain drop, can will cause the problems such as heating furnace is unstable, over-emitting black exhaust after entering heating furnace.Simultaneously the present invention also can be used for other condensation separation that contains micro-drop or easily be condensed into the gas that drips.
Description of drawings
The structural representation of Fig. 1 gas-liquid separator;
Fig. 2 is that air-flow moves towards schematic diagram;
Fig. 3 is the top view of gas-liquid separator;
Fig. 4 is conical baffled structure;
Fig. 5 is inner condenser surface helical fin schematic diagram;
Fig. 6 is inner condenser cross-sectional structure schematic diagram;
Fig. 7 is Fig. 6 profile on A-A and B-B direction;
Fig. 8 is the inner condenser structural representation;
The 1-gas feed, 2-cyclone separator, the fluid-tight of 3-inverted U, 4-gas vent, 5-cooling water (CW) import, 6-cooling water backwater (CWR) outlet, the 7-inner condenser, 8-is conical baffled, the 9-deflection plate, the conical baffled support bar of 10-, the outside cylindrical shell of 11-inner condenser, 12-helical fin.
Specific implementation method
A kind of gas-liquid separator with internal condensation, such as Fig. 1, shown in Figure 3, structure comprises cyclone separator 2 and is fixed on the interior inner condenser 7 of cyclone separator; Inner condenser can be connected with the cyclone separator housing by welding or flange;
Inner condenser is tubular, fixing helical fin 12 on the surface of the outside cylindrical shell of inner condenser, helical fin is fixed on the outside cylindrical shell of inner condenser by the mode of welding, and the angle of helical fin backspin is consistent with the inclination angle of gas feed tangential admission, as shown in Figure 5;
Be respectively equipped with cooling water inlet 5 and cooling backwater outlet 6 on the cylindrical shell of inner condenser, looping cooling water (CW) circulation passage between the inner and outer wall of inner condenser; Be fixed with deflection plate 9 between the inner and outer wall of inner condenser, such as Fig. 6, Fig. 7 and shown in Figure 8; Deflection plate is fixed in the inner condenser annular cooling water circulation passage, and its purpose is to prevent cooling water short circuit between importing and exporting; The deflection plate upper end is fixed on the inner condenser top, between deflection plate lower end and the condenser bottom space is arranged; Deflection plate is separated the cooling water flow circulation passage; Cooling water inlet and cooling backwater outlet lay respectively at the two ends of deflection plate line;
Cyclone separator cylindrical shell top is provided with gas feed 1;
The cyclone separator top arranges gas vent 4, and gas vent is communicated with the condenser inner chamber.
The cyclone separator bottom is provided with conical baffled 8; Conical baffledly be fixed on cyclone separator bottom by conical baffled support bar, as shown in Figure 4.The cyclone separator bottom is inverted U fluid-tight 3.
Respectively cooling water inlet pipe road and CWR road are connected to cooling water inlet 5 and cooling water backwater outlet 6 during use, for equipment provides cold; Deflection plate can increase the flow process of cooling water; Gas feed 4 is connected to the import of heating furnace vacuum tail gas burning pipeline, and the inverted U fluid-tight is connected to device waste oil groove or corresponding waste oil reclaimer; Vavuum pump or other gas are connected to gas feed 1.
After each interface all connects complete and comes into operation, vavuum pump or other gas are connected to gas feed 1, make tangential and downward-sloping the entering of gas; Uncondensed gas tangentially enters the cyclone separator internal cyclone along inlet line and separates, helical fin 12 surface heat exchangings through the welding of inner condenser 8 outer barrel surfaces, after the lower composition condensation of dew point, along with the swirling eddy direction downwards in the enrichment of cyclone separator shell inner surface, and drop to the liquid collection zone of cyclone separator bottom along wall, conical baffled gradient can make conical baffled upper liquid flow into liquid collection zone along the gradient, can prevent also that simultaneously the liquid that has accumulated in the liquid collection zone from being taken out of by uprising gas again; Condensation has also been removed the gas behind the drop and has been separated through cyclone separator, leaves from gas vent.As shown in Figure 2.Cooling water (CW) import, cooling water backwater (CWR) outlet, gas feed, gas vent with inverted U fluid-tight be connected flange and be connected with exterior tubing.
External inverted U fluid-tight 3 can prevent that liquid is from the bottom short circuit.
Claims (7)
1. the gas-liquid separator of condensation in the band, structure comprise cyclone separator and are fixed on inner condenser in the cyclone separator;
Inner condenser is tubular, fixing helical fin on the surface of the outside cylindrical shell of inner condenser;
Be respectively equipped with the outlet of cooling water inlet and cooling water backwater on the cylindrical shell of inner condenser;
Cyclone separator cylindrical shell top is provided with gas feed;
The cyclone separator top arranges gas vent, and gas vent is communicated with the condenser inner chamber;
The cyclone separator bottom is provided with conical baffled.
2. the gas-liquid separator of condensation in the described band of claim 1 is characterized in that, described inner condenser is connected with the housing of cyclone separator by welding or flange.
3. the gas-liquid separator of condensation in the described band of claim 1 is characterized in that, described shape baffle plate is fixed on the cyclone separator bottom by conical baffled support bar.
4. the gas-liquid separator of condensation in the described band of claim 1 is characterized in that, the angle of described helical fin backspin is consistent with the inclination angle of gas feed tangential admission.
5. the gas-liquid separator of condensation in the described band of claim 1 is characterized in that, described helical fin is fixed on the outside cylindrical shell of inner condenser by the mode of welding.
6. the gas-liquid separator of condensation in the described band of claim 1 is characterized in that, described cyclone separator bottom connects the inverted U fluid-tight.
7. the gas-liquid separator of condensation in the described band of claim 1 is characterized in that, the inside of described inner condenser is provided with deflection plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011102307472A CN102921570A (en) | 2011-08-12 | 2011-08-12 | Gas-liquid separator with internal condensation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011102307472A CN102921570A (en) | 2011-08-12 | 2011-08-12 | Gas-liquid separator with internal condensation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102921570A true CN102921570A (en) | 2013-02-13 |
Family
ID=47636578
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011102307472A Pending CN102921570A (en) | 2011-08-12 | 2011-08-12 | Gas-liquid separator with internal condensation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102921570A (en) |
Cited By (27)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104128267A (en) * | 2014-07-15 | 2014-11-05 | 山东博润工业技术股份有限公司 | High efficiency cyclone separator having lower exhaust structure |
| CN104548854A (en) * | 2015-01-27 | 2015-04-29 | 苏州巨联科技有限公司 | Waste gas humidity adjusting device for recovering solvent |
| CN104654823A (en) * | 2014-12-02 | 2015-05-27 | 成都聚智工业设计有限公司 | Industrial waste steam condensing device |
| CN104740964A (en) * | 2015-03-05 | 2015-07-01 | 鲁西化工集团股份有限公司硅化工分公司 | Recycling system containing 'Si-O' link body and recycling method |
| CN104888982A (en) * | 2015-04-27 | 2015-09-09 | 上海遨提新材料技术咨询有限公司 | Asphalt flue gas processing cyclone separator |
| CN107234010A (en) * | 2017-06-20 | 2017-10-10 | 大连理工大学 | From ejection circulation backflow supersonic cyclone separator and its separation method |
| CN110384981A (en) * | 2019-08-29 | 2019-10-29 | 湖北襄化机械设备有限公司 | A kind of moisture trap of enhancing water recycling |
| CN110685892A (en) * | 2019-10-31 | 2020-01-14 | 汤业禧 | Diaphragm vacuum pump |
| CN111804116A (en) * | 2020-07-31 | 2020-10-23 | 宁波巨化化工科技有限公司 | Trichloroethylene quenching coarse separation tower |
| US10987443B1 (en) | 2020-07-03 | 2021-04-27 | Chio Kang Medical, Inc. | Container sterilization device and system, assembling method thereof, and use thereof |
| US11085016B1 (en) | 2020-01-20 | 2021-08-10 | Chio Kang Medical, Inc. | Method for screening bacteria capable of degrading ethylene oxide |
| CN113244733A (en) * | 2021-06-16 | 2021-08-13 | 韩松 | Water-gas separator with dual separation |
| US11103608B1 (en) | 2020-07-03 | 2021-08-31 | Chio Kang Medical, Inc. | Mobile pretreatment apparatus and an operating method thereof, and a mobile analysis apparatus and an operating method thereof |
| US11103829B1 (en) | 2020-03-18 | 2021-08-31 | Chio Kang Medical, Inc. | Systems and methods for treating ethylene oxide waste gas |
| US11110390B1 (en) | 2020-03-18 | 2021-09-07 | Chio Kang Medical, Inc. | Systems and methods for treating sterilization exhaust gas containing ethylene oxide |
| US11125498B1 (en) | 2020-03-18 | 2021-09-21 | Chio Kang Medical, Inc. | Gas liquefaction separator, gas liquefaction recovery system, and method for separating and recovering ethylene oxide |
| US11123449B1 (en) | 2020-07-03 | 2021-09-21 | Chio Kang Medical, Inc. | Mobile sterilization system, mobile execution system, and mobile analysis system |
| US11123680B1 (en) | 2020-03-18 | 2021-09-21 | Chio Kang Medical, Inc. | Devices, systems, and methods for treating ethylene oxide waste gas |
| US11124438B2 (en) | 2020-01-20 | 2021-09-21 | Chio Kang Medical, Inc. | Alcaligenes faecalis for degrading ethylene oxide |
| WO2021184594A1 (en) * | 2020-03-18 | 2021-09-23 | Qiaokang Biotech (Guangdong) Co., LTD. | Gas liquefaction separator, gas liquefaction recovery system, and method for separating and recovering ethylene oxide |
| US20210291105A1 (en) | 2020-03-19 | 2021-09-23 | Chio Kang Medical, Inc. | Ethylene Oxide Adsorption Tower and Recovery System, and Method for Recovering Ethylene Oxide |
| US11130939B2 (en) | 2020-01-20 | 2021-09-28 | Chio Kang Medical, Inc. | Bacteria for degrading ethylene oxide and uses thereof |
| US11130095B1 (en) | 2020-03-18 | 2021-09-28 | Chio Kang Medical, Inc. | Sterilization exhaust gas treating system and method for treating ethylene oxide-containing sterilization exhaust gas by using the same |
| US11136253B1 (en) | 2020-03-18 | 2021-10-05 | Chio Kang Medical, Inc. | Microbiological treatment system for ethylene oxide exhaust gas |
| US11220667B2 (en) | 2020-01-20 | 2022-01-11 | Chio Kang Medical, Inc. | Bacteria for degrading ethylene oxide and applications thereof |
| CN114748943A (en) * | 2022-03-24 | 2022-07-15 | 广东美的白色家电技术创新中心有限公司 | Separator, negative pressure device with separator and pressure cooker |
| CN115445370A (en) * | 2021-06-08 | 2022-12-09 | 中国科学院理化技术研究所 | Segregator for fractional condensation |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2538270Y (en) * | 2002-04-28 | 2003-03-05 | 苏州金莱克清洁器具有限公司 | Speed reducing centrifugal dusting device for suction cleaner |
| CN2597086Y (en) * | 2003-01-15 | 2004-01-07 | 茂名学院 | Spiral flow guiding type cyclone separator |
| US20060086253A1 (en) * | 2004-10-27 | 2006-04-27 | Siddhartha Gaur | Cyclone separator cooler |
| RU2310516C1 (en) * | 2006-03-13 | 2007-11-20 | Открытое акционерное общество Научно-производственное объединение "Искара" | Device for separation of the particles of the liquid from the gas-liquid flow |
| JP2008309343A (en) * | 2007-06-12 | 2008-12-25 | Topre Corp | Expansion mechanism and refrigerating apparatus having the same |
| CN201355161Y (en) * | 2009-02-25 | 2009-12-02 | 浙江春晖智能控制股份有限公司 | High-efficiency gas-liquid separator |
| CN201744409U (en) * | 2010-06-03 | 2011-02-16 | 晁建伟 | Condensed cyclone separator |
-
2011
- 2011-08-12 CN CN2011102307472A patent/CN102921570A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2538270Y (en) * | 2002-04-28 | 2003-03-05 | 苏州金莱克清洁器具有限公司 | Speed reducing centrifugal dusting device for suction cleaner |
| CN2597086Y (en) * | 2003-01-15 | 2004-01-07 | 茂名学院 | Spiral flow guiding type cyclone separator |
| US20060086253A1 (en) * | 2004-10-27 | 2006-04-27 | Siddhartha Gaur | Cyclone separator cooler |
| RU2310516C1 (en) * | 2006-03-13 | 2007-11-20 | Открытое акционерное общество Научно-производственное объединение "Искара" | Device for separation of the particles of the liquid from the gas-liquid flow |
| JP2008309343A (en) * | 2007-06-12 | 2008-12-25 | Topre Corp | Expansion mechanism and refrigerating apparatus having the same |
| CN201355161Y (en) * | 2009-02-25 | 2009-12-02 | 浙江春晖智能控制股份有限公司 | High-efficiency gas-liquid separator |
| CN201744409U (en) * | 2010-06-03 | 2011-02-16 | 晁建伟 | Condensed cyclone separator |
Cited By (30)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104128267A (en) * | 2014-07-15 | 2014-11-05 | 山东博润工业技术股份有限公司 | High efficiency cyclone separator having lower exhaust structure |
| CN104654823A (en) * | 2014-12-02 | 2015-05-27 | 成都聚智工业设计有限公司 | Industrial waste steam condensing device |
| CN104548854A (en) * | 2015-01-27 | 2015-04-29 | 苏州巨联科技有限公司 | Waste gas humidity adjusting device for recovering solvent |
| CN104740964A (en) * | 2015-03-05 | 2015-07-01 | 鲁西化工集团股份有限公司硅化工分公司 | Recycling system containing 'Si-O' link body and recycling method |
| CN104888982A (en) * | 2015-04-27 | 2015-09-09 | 上海遨提新材料技术咨询有限公司 | Asphalt flue gas processing cyclone separator |
| CN107234010A (en) * | 2017-06-20 | 2017-10-10 | 大连理工大学 | From ejection circulation backflow supersonic cyclone separator and its separation method |
| CN110384981A (en) * | 2019-08-29 | 2019-10-29 | 湖北襄化机械设备有限公司 | A kind of moisture trap of enhancing water recycling |
| CN110685892B (en) * | 2019-10-31 | 2021-09-03 | 福雪莱冷暖设备(东莞)有限公司 | Diaphragm vacuum pump |
| CN110685892A (en) * | 2019-10-31 | 2020-01-14 | 汤业禧 | Diaphragm vacuum pump |
| US11220667B2 (en) | 2020-01-20 | 2022-01-11 | Chio Kang Medical, Inc. | Bacteria for degrading ethylene oxide and applications thereof |
| US11085016B1 (en) | 2020-01-20 | 2021-08-10 | Chio Kang Medical, Inc. | Method for screening bacteria capable of degrading ethylene oxide |
| US11130939B2 (en) | 2020-01-20 | 2021-09-28 | Chio Kang Medical, Inc. | Bacteria for degrading ethylene oxide and uses thereof |
| US11124438B2 (en) | 2020-01-20 | 2021-09-21 | Chio Kang Medical, Inc. | Alcaligenes faecalis for degrading ethylene oxide |
| US11123680B1 (en) | 2020-03-18 | 2021-09-21 | Chio Kang Medical, Inc. | Devices, systems, and methods for treating ethylene oxide waste gas |
| US11136253B1 (en) | 2020-03-18 | 2021-10-05 | Chio Kang Medical, Inc. | Microbiological treatment system for ethylene oxide exhaust gas |
| US11110390B1 (en) | 2020-03-18 | 2021-09-07 | Chio Kang Medical, Inc. | Systems and methods for treating sterilization exhaust gas containing ethylene oxide |
| US11125498B1 (en) | 2020-03-18 | 2021-09-21 | Chio Kang Medical, Inc. | Gas liquefaction separator, gas liquefaction recovery system, and method for separating and recovering ethylene oxide |
| WO2021184594A1 (en) * | 2020-03-18 | 2021-09-23 | Qiaokang Biotech (Guangdong) Co., LTD. | Gas liquefaction separator, gas liquefaction recovery system, and method for separating and recovering ethylene oxide |
| US11103829B1 (en) | 2020-03-18 | 2021-08-31 | Chio Kang Medical, Inc. | Systems and methods for treating ethylene oxide waste gas |
| US11130095B1 (en) | 2020-03-18 | 2021-09-28 | Chio Kang Medical, Inc. | Sterilization exhaust gas treating system and method for treating ethylene oxide-containing sterilization exhaust gas by using the same |
| US20210291105A1 (en) | 2020-03-19 | 2021-09-23 | Chio Kang Medical, Inc. | Ethylene Oxide Adsorption Tower and Recovery System, and Method for Recovering Ethylene Oxide |
| US11129914B1 (en) | 2020-03-19 | 2021-09-28 | Chio Kang Medical, Inc. | Ethylene oxide adsorption tower and recovery system, and method for recovering ethylene oxide |
| US11123449B1 (en) | 2020-07-03 | 2021-09-21 | Chio Kang Medical, Inc. | Mobile sterilization system, mobile execution system, and mobile analysis system |
| US10987443B1 (en) | 2020-07-03 | 2021-04-27 | Chio Kang Medical, Inc. | Container sterilization device and system, assembling method thereof, and use thereof |
| US11103608B1 (en) | 2020-07-03 | 2021-08-31 | Chio Kang Medical, Inc. | Mobile pretreatment apparatus and an operating method thereof, and a mobile analysis apparatus and an operating method thereof |
| CN111804116B (en) * | 2020-07-31 | 2021-12-14 | 宁波巨化化工科技有限公司 | Trichloroethylene quenching coarse separation tower |
| CN111804116A (en) * | 2020-07-31 | 2020-10-23 | 宁波巨化化工科技有限公司 | Trichloroethylene quenching coarse separation tower |
| CN115445370A (en) * | 2021-06-08 | 2022-12-09 | 中国科学院理化技术研究所 | Segregator for fractional condensation |
| CN113244733A (en) * | 2021-06-16 | 2021-08-13 | 韩松 | Water-gas separator with dual separation |
| CN114748943A (en) * | 2022-03-24 | 2022-07-15 | 广东美的白色家电技术创新中心有限公司 | Separator, negative pressure device with separator and pressure cooker |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102921570A (en) | Gas-liquid separator with internal condensation | |
| CN207187325U (en) | A kind of efficiently liquefaction condensation separator | |
| CN206965171U (en) | Whirlwind is vortexed gas-liquid separator | |
| CN105737639A (en) | Afterheat utilization cyclone separator | |
| CN211358240U (en) | Complete processing system for oil-containing solid waste thermal desorption steam | |
| CN203582809U (en) | Condenser | |
| CN205175855U (en) | Device of farine volume and tar flow measurement among high -temperature gas | |
| CN201930645U (en) | Spiral air-lift type steam separator | |
| CN209161961U (en) | A kind of purification-recovery system for damaged tire cracking oil gas | |
| CN105597480A (en) | Condensation-type gas-liquid separation apparatus | |
| CN206009025U (en) | Cyclone separator for crushed coal pressure gasifying raw gas dedusting | |
| CN203258666U (en) | Liquid drop recovery device of hanging type chimney | |
| CN205391788U (en) | Waste gas recovery heat transfer system | |
| CN202316145U (en) | Air-cooled type cyclone dust collector | |
| CN205258389U (en) | Whirlwind condensation decoking device | |
| CN207071240U (en) | Segregate the low pressure drop demister of isolation integral equipment | |
| CN201545718U (en) | Urea process condensed fluid treatment device | |
| CN206736192U (en) | A kind of biogas combustion purification device | |
| CN110652833A (en) | Complete processing system for oil-containing solid waste thermal desorption steam | |
| CN203249525U (en) | Heat pipe type organic working medium falling film evaporator utilizing low temperature exhaust heat | |
| CN202538524U (en) | Novel oil-gas separator | |
| CN204944228U (en) | A kind of condenser avoiding fixed gas to gather | |
| CN104128267A (en) | High efficiency cyclone separator having lower exhaust structure | |
| CN211885462U (en) | Oil seal condensation system for waste tire thermal cracking | |
| CN108854456B (en) | System and method for recycling heat energy of desorption tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20130213 |