CN202126142U - Air separation device capable of rapidly putting into rectification operation - Google Patents

Air separation device capable of rapidly putting into rectification operation Download PDF

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Publication number
CN202126142U
CN202126142U CN2011201169907U CN201120116990U CN202126142U CN 202126142 U CN202126142 U CN 202126142U CN 2011201169907 U CN2011201169907 U CN 2011201169907U CN 201120116990 U CN201120116990 U CN 201120116990U CN 202126142 U CN202126142 U CN 202126142U
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CN
China
Prior art keywords
storage tank
liquid oxygen
air separation
pipe
liquid
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 - Fee Related
Application number
CN2011201169907U
Other languages
Chinese (zh)
Inventor
施英虎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ZHEJIANG YUANDA AIR CONDITIONING EQUIPMENT CO Ltd
Original Assignee
ZHEJIANG YUANDA AIR CONDITIONING EQUIPMENT CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by ZHEJIANG YUANDA AIR CONDITIONING EQUIPMENT CO Ltd filed Critical ZHEJIANG YUANDA AIR CONDITIONING EQUIPMENT CO Ltd
Priority to CN2011201169907U priority Critical patent/CN202126142U/en
Application granted granted Critical
Publication of CN202126142U publication Critical patent/CN202126142U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04248—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion
    • F25J3/04254—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using the cold stored in external cryogenic fluids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04406—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system
    • F25J3/04412—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04472—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages
    • F25J3/04478—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using the cold from cryogenic liquids produced within the air fractionation unit and stored in internal or intermediate storages for controlling purposes, e.g. start-up or back-up procedures
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04763—Start-up or control of the process; Details of the apparatus used
    • F25J3/04769—Operation, control and regulation of the process; Instrumentation within the process
    • F25J3/04812—Different modes, i.e. "runs" of operation
    • F25J3/04818—Start-up of the process
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04763—Start-up or control of the process; Details of the apparatus used
    • F25J3/04769—Operation, control and regulation of the process; Instrumentation within the process
    • F25J3/04854—Safety aspects of operation
    • F25J3/0486—Safety aspects of operation of vaporisers for oxygen enriched liquids, e.g. purging of liquids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04763—Start-up or control of the process; Details of the apparatus used
    • F25J3/04866—Construction and layout of air fractionation equipments, e.g. valves, machines
    • F25J3/04951—Arrangements of multiple air fractionation units or multiple equipments fulfilling the same process step, e.g. multiple trains in a network
    • F25J3/04963—Arrangements of multiple air fractionation units or multiple equipments fulfilling the same process step, e.g. multiple trains in a network and inter-connecting equipment within or downstream of the fractionation unit(s)
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2205/00—Processes or apparatus using other separation and/or other processing means
    • F25J2205/60—Processes or apparatus using other separation and/or other processing means using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/50—Oxygen
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2245/00—Processes or apparatus involving steps for recycling of process streams
    • F25J2245/50—Processes or apparatus involving steps for recycling of process streams the recycled stream being oxygen
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2280/00—Control of the process or apparatus
    • F25J2280/10—Control for or during start-up and cooling down of the installation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/62—Details of storing a fluid in a tank

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

The utility model relates to an air separation device capable of rapidly putting into rectification operation, comprising main condensers, main condenser liquid oxygen circulating pipes, a storage tank, a storage tank pressure booster, a storage tank liquid inlet pipe, a storage tank pressure booster liquid inlet pipe and a storage tank pressure booster liquid discharge pipe, wherein the storage tank liquid inlet pipe is connected with the main condenser liquid oxygen circulating pipes which are connected with the main condensers and the storage tank, and communicating valves are arranged on the main condenser liquid oxygen circulating pipe; and one ends of the liquid inlet pipe and a liquid return pipe of the storage tank pressure booster are connected with the storage tank pressure booster, the other ends are connected with more than two sets of oxygen making units, and the main condenser liquid oxygen circulating pipes between two units and the storage tank are connected through a communicating pipe on which communicating valves are arranged. In the utility model, the air separation device comprises more than two sets of oxygen making units, the main condenser liquid oxygen circulating pipes between two units and the storage tank are connected through the communicating pipe on which the communicating valves are arranged, and the storage tank is a low temperature liquid tank car. The air separation device capable of rapidly putting into rectification operation has the improvement of using the liquid oxygen circulating pipe to communicate the main condensers and the storage tank as well as main condensers of more than two oxygen making units.

Description

Drop into the air separation unit of rectifying operation fast
Technical field:
The utility model relates to a kind of equipment that makes gas or admixture of gas liquefy or separate through pressurization and cooling processing, refers in particular to a kind of air separation unit of quick input rectifying operation.
Background technology:
At present; The big-and-middle-sized oxygenerator that uses in the production generally all be with air by compressor compresses, through the cooling after portion of air obtain low temperature through decompressor; Another part air advances to cool off rectifying column and plate type heat exchanger cooling and liquefaction back to be separated in rectifying column, produces oxygen and nitrogen etc. respectively.Because supporting with it expander refrigeration ability is little, the start-up time of its air separation unit, board-like flow process reached about 40 hours mostly, and the molecular sieve flow startup time was at 70-80 hour, and is that have even longer.Air separation unit product-free output in start-up course, and supporting with it corollary equipments such as air compressor machine consumed power as usual.So start-up time is long more, then water, electric flux consumption are high more.
Summary of the invention:
The utility model provides a kind of air separation unit that can improve the quick startup of air separation unit productivity ratio and energy savings.
The utility model is realized through following technical scheme: the air separation unit that drops into the rectifying operation fast comprises that main cold, main cold liquid oxygen circulation pipe, storage tank, storage tank booster, storage tank feed tube, storage tank booster feed tube, storage tank booster discharging tube, storage tank feed tube link to each other with main cold liquid oxygen circulation pipe; Main cold liquid oxygen circulation pipe links to each other with main cold-peace storage tank, which is provided with communicating valve.One end of the feed tube of storage tank booster, liquid back pipe connects the storage tank booster, the other end and the above oxygenerator group of cover, and cold liquid oxygen circulation pipe of the master between two units and storage tank interconnected through communicating pipe, also were provided with communicating valve on the pipeline; This device comprises the above oxygenerator group of two covers, and cold liquid oxygen circulation pipe of the master between two units and storage tank interconnected through communicating pipe, also were provided with communicating valve on the pipeline; Storage tank is a cryogenic liquid tank lorry.
The utility model improvements are will lead between cold and storage tank and cold of the master of two above oxygenerator groups is communicated with the liquid oxygen circulation pipe.When needing; Open the valve on the pipeline; The liquid oxygen that operation oxygenerator group master is stored in the cold or storage tank is counter deliver to the master who starts unit cold in, thereby utilize the vaporization of low temperature liquid oxygen to absorb a large amount of evaporation latent heats, auxiliary expander refrigeration; Thereby make the cold accumulating liquid as early as possible of master that starts unit, set up nominal situation.
Description of drawings:
Fig. 1 is the structural representation of the utility model.
The specific embodiment:
As shown in Figure 1, this device comprises 2 cover oxygenerator groups, and 1# is board-like flow process oxygenerator group, and 2# is a molecular sieve flow process oxygenerator group.The master of oxygenerator group cold 1 links to each other with main cold liquid oxygen circulation pipe 2; The cold liquid oxygen circulation pipe 2 of master and the storage tank feed tube 12 of two cover oxygenerator groups interconnected through communicating pipe 19; Communicating valve 4,5,6 on communicating pipe 19 is cold angle valve, and 7 of storage tank 3 and storage tank boosters are communicated with corresponding feed liquor valve 10, the tapping valve 11 of being provided with on it through storage tank booster feed tube 8 and storage tank booster discharging tube 9; Main cold liquid oxygen circulation pipe is provided with liquid oxygen adsorber 17, is used for adsorbing the impurity of liquid oxygen.1# oxygenerator group also is provided with import and is connected with main cold 1, the liquid oxygen pump 16 that outlet is connected with main cold liquid oxygen circulation pipe.
When 1# oxygenerator group is normally moved, when 2# oxygenerator group starts, can pass through communicating pipe 19 to the anti-topping up body of 2# oxygenerator group by 1# oxygenerator group, utilize vaporizing liquid to obtain cold, cooling device makes main cold accumulating liquid as early as possible.Open cold angle valve 5, stop valve 13,14, crack cold angle valve 6 preheating pipelines.After stop valve 14 frostings, close, open stop valve 15, close cold angle valve 5, to the cold liquor charging of master that starts unit.When the cold liquid level of 2# oxygenerator group master reached certain altitude, 1# oxygenerator group was because of receiving the restriction of liquid oxygen pump 16 lifts, and liquid oxygen is crossed and do not come.Open cold angle valve 4 this moment, close stop valve 15, be about to the unnecessary liquid of 1# oxygenerator and be transported in the storage tank and accumulate.
When 2# oxygenerator group is normally moved, when 1# oxygenerator group starts, can utilize communicating pipe 19 oppositely to use.Open cold angle valve 6, stop valve 13, cold angle valve 5 and 1# oxygenerator group liquid oxygen adsorber by-passing valve are closed when stop valve 13 frostings, and 2# oxygenerator group liquid gets into 1# oxygenerator master cold 1.Because the resistance of liquid oxygen adsorber 17 when cold angle valve 5 mistake liquid are slow, can be closed cold angle valve 5, opens stop valve 15.When the cold liquid level of 1# oxygenerator group master reach a certain height, after pressure rose gradually, 2# oxygenerator group liquid can not be mended into 1# oxygenerator group by pressure reduction, opened cold angle valve 4, closed cold angle valve 6 and can liquid be accumulated in the storage tank.
When the cold liquid of unit master adds to certain altitude, when another set of unit liquid can not be annotated into, the liquid in the available storage tank 3 instead was charged to main coldly 1 through communicating pipe 19, continues fluid injection.Close storage tank feed liquor valve 18, open storage tank booster 7 the storage tank internal pressure is increased, open storage tank feed liquor valve 18 again, open cold angle valve 4,6, to the cold anti-topping up body of 1# oxygenerator group master; Open stop valve 15 or cold angle valve 5, to the cold anti-topping up body of 2# oxygenerator group master.

Claims (4)

1. one kind is dropped into the air separation unit that rectifying moves fast; Comprise that main cold, main cold liquid oxygen circulation pipe, storage tank, storage tank booster, storage tank feed tube, storage tank booster feed tube, storage tank booster discharging tube, storage tank feed tube link to each other with main cold liquid oxygen circulation pipe; Main cold liquid oxygen circulation pipe links to each other with main cold-peace storage tank; Which is provided with communicating valve, an end of the feed tube of storage tank booster, liquid back pipe connects the storage tank booster, and the other end links to each other with storage tank; Main cold liquid oxygen circulation pipe is provided with communicating valve; It is characterized in that this device comprises the above oxygenerator group of two covers, cold liquid oxygen circulation pipe of the master between two units and storage tank interconnected through communicating pipe, also were provided with communicating valve on the pipeline.
2. the air separation unit of a kind of quick input rectifying operation as claimed in claim 1 is characterized in that said communicating valve is cold angle valve.
3. the air separation unit of a kind of quick input rectifying operation as claimed in claim 1 is characterized in that the cold liquid oxygen circulation pipe of said master is provided with liquid oxygen adsorber.
4. according to claim 1 or claim 2 the air separation unit of a kind of quick input rectifying operation is characterized in that said storage tank is a cryogenic liquid tank lorry.
CN2011201169907U 2011-04-14 2011-04-14 Air separation device capable of rapidly putting into rectification operation Expired - Fee Related CN202126142U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011201169907U CN202126142U (en) 2011-04-14 2011-04-14 Air separation device capable of rapidly putting into rectification operation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011201169907U CN202126142U (en) 2011-04-14 2011-04-14 Air separation device capable of rapidly putting into rectification operation

Publications (1)

Publication Number Publication Date
CN202126142U true CN202126142U (en) 2012-01-25

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Application Number Title Priority Date Filing Date
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103344091A (en) * 2013-07-26 2013-10-09 四川德胜集团钢铁有限公司 Method for shortening time from effusion to oxygen generation for industrial oxygen generator
CN105300031A (en) * 2015-11-11 2016-02-03 巴彦淖尔市飞尚铜业有限公司 Starting method for rapid oxygen outflow
CN105486033A (en) * 2015-12-11 2016-04-13 武汉钢铁(集团)公司 Cold starting system of air separation unit

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103344091A (en) * 2013-07-26 2013-10-09 四川德胜集团钢铁有限公司 Method for shortening time from effusion to oxygen generation for industrial oxygen generator
CN103344091B (en) * 2013-07-26 2015-08-19 四川德胜集团钒钛有限公司 A kind of industrial oxygenerating machine that shortens is from hydrops to the method for time going out oxygen
CN105300031A (en) * 2015-11-11 2016-02-03 巴彦淖尔市飞尚铜业有限公司 Starting method for rapid oxygen outflow
CN105300031B (en) * 2015-11-11 2017-07-11 巴彦淖尔市飞尚铜业有限公司 A kind of startup method for quickly going out oxygen
CN105486033A (en) * 2015-12-11 2016-04-13 武汉钢铁(集团)公司 Cold starting system of air separation unit

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120125

Termination date: 20140414