CN107806742A - A kind of low-temperature liquefaction method produces CO2Method and device - Google Patents

A kind of low-temperature liquefaction method produces CO2Method and device Download PDF

Info

Publication number
CN107806742A
CN107806742A CN201710915172.5A CN201710915172A CN107806742A CN 107806742 A CN107806742 A CN 107806742A CN 201710915172 A CN201710915172 A CN 201710915172A CN 107806742 A CN107806742 A CN 107806742A
Authority
CN
China
Prior art keywords
tower
low
partition
liquefaction
temperature
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
Application number
CN201710915172.5A
Other languages
Chinese (zh)
Inventor
滕昆辰
谢斐
郑艾富
陈伟
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.)
NANJING HONGBO ENVIRONMENTAL PROTECTION INDUSTRIAL Co Ltd
Original Assignee
NANJING HONGBO ENVIRONMENTAL PROTECTION INDUSTRIAL 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 NANJING HONGBO ENVIRONMENTAL PROTECTION INDUSTRIAL Co Ltd filed Critical NANJING HONGBO ENVIRONMENTAL PROTECTION INDUSTRIAL Co Ltd
Priority to CN201710915172.5A priority Critical patent/CN107806742A/en
Publication of CN107806742A publication Critical patent/CN107806742A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification

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 invention discloses a kind of low-temperature liquefaction method to produce CO2Method and device, comprise the following steps:S1:Gas is passed through tower in first by air inlet, the first refrigerator pipes connected by the first refrigeration machine cool to gas, due to the ratio CO that tower internal temperature is set in first2Boiling point is high, and boiling point compares CO2Liquefaction and solidification occurs in low gas, and solidfied material is attached in the first refrigeration pipe outer wall, removed by scratch device;S2:The first magnetic valve is opened, gas is passed through in second inside tower, due to the ratio CO that tower internal temperature is set in second2Boiling point is high, CO2It can liquefy, by low on liquefaction piece;S3:Open second solenoid valve, the CO after liquefaction2It is collected into fluid reservoir.The low-temperature liquefaction method produces CO2Method, step is reasonable in design, liquefaction effect is good.

Description

A kind of low-temperature liquefaction method produces CO2Method and device
Technical field
The present invention relates to biogas treatment technical field, specially a kind of low-temperature liquefaction method production CO2Method and device.
Background technology
Biogas is a kind of mixed combustible gas body, and its composition depends not only on fermentation raw material and species and its relative amount, and And change with fermentation condition and the different of fermentation stage.Generally, the main component of biogas is methane and carbon dioxide.This Outside, the gas such as also a small amount of hydrogen, carbon monoxide, nitrogen, hydrogen sulfide.Methane content accounts for 50% to 70%, and carbon dioxide accounts for 30% to 40% or so.Biogas is colourless gas, and slightly smell is because containing a small amount of hydrogen sulfide gas.
State when being captured according to carbon dioxide is different, and low temperature process carbon trapping technique contains two kinds of trapping forms:The One kind is liquefaction separation, i.e. cryogenic condensation or rectifying, using the boiling point difference with other compositions in mixed gas, using low temperature skill Art is by CO2Liquefy and separate;Second is separation of sublimating, it mainly using other in de-sublimation temperature and mixed gas into Point difference, using cryogenic technique by CO2Solidify and separate.
The content of the invention
It is an object of the invention to provide a kind of low-temperature liquefaction method to produce CO2Method and device, to solve above-mentioned background The problem of being proposed in technology.
To achieve the above object, the present invention provides following technical scheme:A kind of low-temperature liquefaction method produces CO2Method, bag Include following steps:
S1、:Gas is passed through tower in first by air inlet, the first refrigerator pipes connected by the first refrigeration machine are to gas Cooled, due to the ratio CO that tower internal temperature is set in first2Boiling point is high, and boiling point compares CO2Low gas occurs liquefaction and consolidated Change, solidfied material is attached in the first refrigeration pipe outer wall, removed by scratch device;
S2、:The first magnetic valve is opened, gas is passed through in second inside tower, because tower internal temperature is set in second Compare CO2Boiling point is high, CO2It can liquefy, by low on liquefaction piece;
S3、:Open second solenoid valve, the CO after liquefaction2It is collected into fluid reservoir.
A kind of low-temperature liquefaction method produces CO2Device, including outer tower, Nei Ta and fluid reservoir, the outer tower be internally provided with Interior tower, vacuum chamber is provided between Wai Ta and interior tower, first partition and second partition be installed inside the interior tower, described first Dividing plate and second partition are distributed and interior tower are divided into first into tower in tower and second up and down, and tower inner tip is set in described first There are the first refrigerator pipes, the first refrigerator pipes top is provided with the first refrigeration machine, the first refrigeration machine side outside outer tower Outer tower on offer air inlet, the air inlet connects with tower in first, and the first refrigerator pipes bottom is in first partition Scratch device is installed with, the first magnetic valve is installed in the first partition of the scratch device side, tower in described second Interior side is provided with the second refrigerator pipes, and the second refrigerator pipes outer end is provided with the second refrigeration machine on the outside of outer tower, and described Two refrigerator pipes bottoms are additionally provided with liquefaction piece, are provided with second solenoid valve on the second partition of the liquefaction piece bottom, and described the Tower interior side offers gas outlet in two, and fluid reservoir, the fluid reservoir are provided with second partition bottom inside the interior tower Bottom offers liquid outlet, and the outer bottom of towe end is provided with base.
Preferably, the scratch device includes scraper, sleeve pipe and screwed pipe, and the screwed pipe is fixedly welded on set ttom of pipe Portion, described sleeve pipe are fixedly connected on the top of electric expansion bar by screwed pipe, and described sleeve pipe top is fixedly welded with scraper, institute It is loop configuration to state scraper, and diameter is identical with the first refrigerator pipes overall diameter.
Preferably, the outer tower, tower in first, tower and fluid reservoir are stainless steel material in second, and in described first Tower internal temperature is arranged to -65 DEG C, and tower internal temperature is arranged to -85 DEG C in second, fluid reservoir internal temperature and bis- Nei Tanei Portion's temperature is identical.
Preferably, the outer tower, tower in first, be enclosed with asbestos insulation board outside tower and fluid reservoir in second.
Preferably, described air inlet one end is additionally provided with valve, flow controller and pressure controller.
Preferably, first refrigeration machine and the second refrigeration machine are free-piston type sterlin refrigerator.
Preferably, it is additionally provided with the second partition of the first partition bottom and bends upward liquid collecting plate.
Compared with prior art, the beneficial effects of the invention are as follows:The low-temperature liquefaction method produces CO2 method and device, leads to The design of scratch device is crossed, avoids the thing covering that is cured outside refrigerator pipes so that influenceing refrigeration, while protect system Cold pipe, accelerate refrigerating efficiency;By the design for the piece that liquefies, in CO2During low-temperature liquefaction, guide functions can be played, are possessed The advantages that step is reasonable in design, liquefaction effect is good.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present invention;
Fig. 2 is the second refrigerator pipes structural representation of the invention;
Fig. 3 is scratch device cross-sectional view of the present invention.
In figure:1 first refrigeration machine, 2 scratch devices, 3 outer towers, 4 first partitions, tower, 6 second refrigeration machines, 7 second systems in 5 Cold pipe, 8 second partitions, 9 vacuum chambers, 10 bases, 11 liquid outlets, 12 air inlets, 13 first refrigerator pipes, tower, 15 in 14 first One magnetic valve, tower in 16 second, 17 gas outlets, 18 liquefaction pieces, 19 second solenoid valves, 20 fluid reservoirs, 21 scrapers, 22 sleeve pipes, 24 screwed pipes.
Embodiment
Below in conjunction with the brief description of the drawings in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear Chu, it is fully described by, it is clear that described embodiment is only part of the embodiment of the present invention, rather than whole embodiments. Based on the embodiment in the present invention, those of ordinary skill in the art are obtained all under the premise of creative work is not made Other embodiment, belong to the scope of protection of the invention.
Fig. 1-3 are referred to, the present invention provides a kind of technical scheme:A kind of low-temperature liquefaction method produces CO2Method, including such as Lower step:
S1、:Gas is passed through tower 14 in first by air inlet 12, the first refrigerator pipes connected by the first refrigeration machine 1 13 pairs of gases cool, due to the ratio CO that the internal temperature of tower 14 is set in first2Boiling point is high, and boiling point compares CO2Low gas is realized Now liquefaction and solidification, solidfied material are attached on the outer wall of the first refrigerator pipes 13, removed by scratch device 2;
S2、:The first magnetic valve 15 is opened, gas is passed through in second inside tower 16, due to the internal temperature of tower 16 in second The ratio CO of setting2Boiling point is high, CO2It can liquefy, by low on liquefaction piece 18;
S3、:Open second solenoid valve 19, the CO after liquefaction2It is collected into fluid reservoir 20.
A kind of low-temperature liquefaction method produces CO2Device, including outer tower 3, interior tower 5 and fluid reservoir 20, inside the outer tower 3 Interior tower 5 is provided with, vacuum chamber 9 is provided between outer tower 3 and interior tower 5, first partition 4 and second is installed inside the interior tower 5 Dividing plate 8, the first partition 4 and second partition are distributed about 8 and divide interior tower 5 for tower 16, institute in tower 14 and second in first State the inner tip of tower 14 in first and be provided with the first refrigerator pipes 13, the top of the first refrigerator pipes 13 is provided with outside outer tower 3 First refrigeration machine 1, offers air inlet 12 on the outer tower 3 of the side of the first refrigeration machine 1, tower in the air inlet 12 and first 14 connections, the bottom of the first refrigerator pipes 13 is installed with scratch device 2, the side of scratch device 2 in first partition 4 First partition 4 on the first magnetic valve 15 is installed, the interior side of tower 16 is provided with the second refrigerator pipes 7 in described second, described The outer end of second refrigerator pipes 7 is provided with the second refrigeration machine 6 in the outer outside of tower 3, and the bottom of the second refrigerator pipes 7 is additionally provided with liquefaction piece 18, second solenoid valve 19 is provided with the second partition 8 of liquefaction piece 18 bottom, and the interior side of tower 165 is opened in described second Provided with gas outlet 17, fluid reservoir 20 is provided with inside the interior tower 5 in the bottom of second partition 8, the bottom of fluid reservoir 20 opens up There is liquid outlet 11, the outer bottom of tower 3 is provided with base 10.
Further, the scratch device 2 includes scraper 21, sleeve pipe 22 and screwed pipe 24, and the screwed pipe 24 fixes weldering The bottom of sleeve pipe 22 is connected on, described sleeve pipe 22 is fixedly connected on the top of electric expansion bar by screwed pipe 24, and described sleeve pipe 22 is pushed up End is fixedly welded with scraper 21, and the scraper 21 is loop configuration, and diameter is identical with the overall diameter of the first refrigerator pipes 13.
Further, tower 16 and fluid reservoir 20 are stainless steel material in tower 14, second in the outer tower 3, first, and The internal temperature of tower 14 is arranged to -65 DEG C in described first, and the internal temperature of tower 16 is arranged to -85 DEG C in second, inside fluid reservoir 20 Temperature is identical with the internal temperature of tower in second 16.
Further, it is enclosed with asbestos guarantor outside tower 16 and fluid reservoir 20 in tower 14, second in the outer tower 3, first Warm plate.
Further, described one end of air inlet 12 is additionally provided with valve, flow controller and pressure controller.
Further, the refrigeration machine 6 of the first refrigeration machine 1 and second is free-piston type sterlin refrigerator.
Further, it is additionally provided with the second partition 8 of the bottom of first partition 4 and bends upward liquid collecting plate.
Although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with A variety of changes, modification can be carried out to these embodiments, replace without departing from the principles and spirit of the present invention by understanding And modification, the scope of the present invention is defined by the appended.

Claims (8)

1. a kind of low-temperature liquefaction method produces CO2Method, it is characterised in that comprise the following steps:
S1、:Gas is passed through tower in first (14) by air inlet (12), the first refrigeration connected by the first refrigeration machine (1) Pipe (13) cools to gas, the ratio CO that tower (14) internal temperature is set in first2Boiling point is high, and boiling point compares CO2Low gas Know from experience and liquefaction and solidification occur, solidfied material is attached on the first refrigerator pipes (13) outer wall, is removed by scratch device (2);
S2、:The first magnetic valve (15) is opened, it is internal that gas is passed through into tower in second (16), due to the internal temperature of tower (16) in second Spend the ratio CO set2Boiling point is high, CO2It can liquefy, by low on liquefaction piece (18);
S3、:Open second solenoid valve (19), the CO after liquefaction2It is collected into fluid reservoir (20).
2. a kind of low-temperature liquefaction method produces CO2Device, including outer tower (3), interior tower (5) and fluid reservoir (20), it is characterised in that: The outer tower (3) is internally provided with interior tower (5), and vacuum chamber (9), the interior tower (5) are provided between outer tower (3) and interior tower (5) Inside is provided with first partition (4) and second partition (8), and the first partition (4) and second partition (8) are distributed and by up and down Tower (5) is divided into tower (16) in tower in first (14) and second, and tower (14) inner tip is provided with the first refrigerator pipes in described first (13), the first refrigerator pipes (13) top is provided with the first refrigeration machine (1), first refrigeration machine (1) outside Wai Ta (3) Air inlet (12) is offered on the outer tower (3) of side, the air inlet (12) connects with tower in first (14), first refrigeration Pipe (13) bottom is installed with scratch device (2), the first partition of scratch device (2) side in first partition (4) (4) the first magnetic valve (15) is installed on, tower (16) interior side is provided with the second refrigerator pipes (7) in described second, and described Two refrigerator pipes (7) outer end is provided with the second refrigeration machine (6) on the outside of Wai Ta (3), and the second refrigerator pipes (7) bottom is additionally provided with Liquefy piece (18), is provided with second solenoid valve (19) on the second partition (8) of described liquefaction piece (18) bottom, tower in described second (16) interior side offers gas outlet (17), and the interior tower (5) is internal to be provided with fluid reservoir in second partition (8) bottom (20), fluid reservoir (20) bottom offers liquid outlet (11), and outer tower (3) bottom is provided with base (10).
A kind of 3. low-temperature liquefaction method production CO according to claim 22Device, it is characterised in that:The scratch device (2) scraper (21), sleeve pipe (22) and screwed pipe (24) are included, the screwed pipe (24) is fixedly welded on sleeve pipe (22) bottom, institute The top that sleeve pipe (22) is fixedly connected on electric expansion bar by screwed pipe (24) is stated, described sleeve pipe (22) top is fixedly welded with Scraper (21), the scraper (21) are loop configuration, and its diameter is identical with the first refrigerator pipes (13) overall diameter.
A kind of 4. low-temperature liquefaction method production CO according to claim 22Device, it is characterised in that:The outer tower (3), Tower (14) in one, tower (16) and fluid reservoir (20) are stainless steel material in second, and tower (14) internal temperature in described first It is arranged to -65 DEG C, tower (16) internal temperature is arranged to -85 DEG C in second, tower (16) in fluid reservoir (20) internal temperature and second Internal temperature is identical.
A kind of 5. low-temperature liquefaction method production CO according to claim 22Device, it is characterised in that:The outer tower (3), Tower (14) in one, the outside of tower (16) and fluid reservoir (20) is enclosed with asbestos insulation board in second.
A kind of 6. low-temperature liquefaction method production CO according to claim 22Device, it is characterised in that:The air inlet (12) One end is additionally provided with valve, flow controller and pressure controller.
A kind of 7. low-temperature liquefaction method production CO according to claim 22Device, it is characterised in that:First refrigeration machine (1) and the second refrigeration machine (6) is free-piston type sterlin refrigerator.
A kind of 8. low-temperature liquefaction method production CO according to claim 22Device, it is characterised in that:The first partition (4) it is additionally provided with the second partition (8) of bottom and bends upward liquid collecting plate.
CN201710915172.5A 2017-09-30 2017-09-30 A kind of low-temperature liquefaction method produces CO2Method and device Pending CN107806742A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710915172.5A CN107806742A (en) 2017-09-30 2017-09-30 A kind of low-temperature liquefaction method produces CO2Method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710915172.5A CN107806742A (en) 2017-09-30 2017-09-30 A kind of low-temperature liquefaction method produces CO2Method and device

Publications (1)

Publication Number Publication Date
CN107806742A true CN107806742A (en) 2018-03-16

Family

ID=61583417

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710915172.5A Pending CN107806742A (en) 2017-09-30 2017-09-30 A kind of low-temperature liquefaction method produces CO2Method and device

Country Status (1)

Country Link
CN (1) CN107806742A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1186842A1 (en) * 2000-09-11 2002-03-13 Carboxyque Française Process and device for the packaging of carbon dioxide snow in a plastic film
CN101126609A (en) * 2006-08-14 2008-02-20 张吉礼 Condensation tube drainage device
CN102257341A (en) * 2008-12-19 2011-11-23 乔治洛德方法研究和开发液化空气有限公司 Method for trapping carbon dioxide by cryocondensation
CN106237648A (en) * 2016-09-29 2016-12-21 天津大学 Low-temperature carbon dioxide segregation apparatus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1186842A1 (en) * 2000-09-11 2002-03-13 Carboxyque Française Process and device for the packaging of carbon dioxide snow in a plastic film
CN101126609A (en) * 2006-08-14 2008-02-20 张吉礼 Condensation tube drainage device
CN102257341A (en) * 2008-12-19 2011-11-23 乔治洛德方法研究和开发液化空气有限公司 Method for trapping carbon dioxide by cryocondensation
CN106237648A (en) * 2016-09-29 2016-12-21 天津大学 Low-temperature carbon dioxide segregation apparatus

Similar Documents

Publication Publication Date Title
CN100588702C (en) The method and apparatus of the cut of Sweet natural gas of production liquefiable simultaneously and natural gas liquids
CN106178807B (en) A kind of gas recovery system for oil of " double condensation-absorption " integrated technology
CN106979664B (en) Atmospheric carbon dioxide liquifying method
RU2014141580A (en) METHOD AND DEVICE FOR CO2 SEPARATION DURING COOLING USING LAVAL NOZZLE
CN106500461A (en) There is the HYCO cold box systems for accelerating precooling effect and its accelerate forecooling method
CN104845692A (en) Oilfield associated gas complete liquefaction recovery system and method thereof
CN106642988A (en) System of utilizing liquid nitrogen wash to produce syngas for synthetic ammonia and LNG
RU2010101417A (en) DESIGN OF THE REBOILER OF THE DEASOTIC COLUMN
CN106595223B (en) The system and method for three or more heavy hydrocarbon of carbon in a kind of recycling natural gas
US2433604A (en) Separation of the constituents of gaseous mixtures
CN100416197C (en) Method and apparatus for removing nitrogen
CN106871576B (en) Commercial syngas low temperature front-end demethanization method and system
CN106123487B (en) A kind of devices and methods therefor that pure neon is produced by ne-He mixture
CN103773529B (en) Pry-mounted associated gas liquefaction system
CN107806742A (en) A kind of low-temperature liquefaction method produces CO2Method and device
CN107084594A (en) A kind of liquid CO circularly coolings synthesising gas systeming carbinol coproduction LNG devices and its application method
US2213338A (en) Method and apparatus for fractionating gaseous mixtures
WO2017046462A1 (en) Method and apparatus for producing a mixture of carbon monoxide and hydrogen
CN102829569B (en) Refrigeration equipment
CN105423701A (en) Method for preparing synthetic natural gas (SNG) through coke-oven gas cryogenic separating
CN206291622U (en) The system that syngas for synthetic ammonia and LNG are produced using liquid nitrogen washing
CN205279605U (en) Preparation synthetic natural gas's coke oven gas cryogenic separation system
CN110044133B (en) Apparatus and method for separating and purifying carbon monoxide
KR890001743B1 (en) Highly pure nitrogen gas producing apparatus
CN213631179U (en) Normal-temperature feeding purification ammonia synthesis gas liquid nitrogen washing device with precooling function

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20180316