CN104896873A - Improved integrated food-grade industrial-grade CO2 recovery device and process - Google Patents

Improved integrated food-grade industrial-grade CO2 recovery device and process Download PDF

Info

Publication number
CN104896873A
CN104896873A CN201510337785.6A CN201510337785A CN104896873A CN 104896873 A CN104896873 A CN 104896873A CN 201510337785 A CN201510337785 A CN 201510337785A CN 104896873 A CN104896873 A CN 104896873A
Authority
CN
China
Prior art keywords
grade
food
carbon dioxide
desulfurization
dioxide
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
CN201510337785.6A
Other languages
Chinese (zh)
Inventor
朱桂生
唐丽
丁雪梅
邵守言
王海亮
黄诚
陈志林
王忠华
徐国仲
黄永明
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.)
JIANGSU SOPO (GROUP) CO Ltd
Jiangsu Suo Pu Science And Technology Invests And Develops Co Ltd
ZHENJIANG SOPO TIANCHEN CARBON RECYCLING Co Ltd
Original Assignee
JIANGSU SOPO (GROUP) CO Ltd
Jiangsu Suo Pu Science And Technology Invests And Develops Co Ltd
ZHENJIANG SOPO TIANCHEN CARBON RECYCLING 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 JIANGSU SOPO (GROUP) CO Ltd, Jiangsu Suo Pu Science And Technology Invests And Develops Co Ltd, ZHENJIANG SOPO TIANCHEN CARBON RECYCLING Co Ltd filed Critical JIANGSU SOPO (GROUP) CO Ltd
Priority to CN201510337785.6A priority Critical patent/CN104896873A/en
Publication of CN104896873A publication Critical patent/CN104896873A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/151Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Landscapes

  • Carbon And Carbon Compounds (AREA)

Abstract

The invention discloses an improved integrated food-grade industrial-grade CO2 recovery device and process. The device comprises a carbon dioxide compressor, a cooling separator, a buffer tank, a desulfurization tower, a fine desulfurization system, a dryer, a liquefier, a rectifying tower, a reboiler and a subcooler which are connected in the material delivery direction successively. A connection pipe is arranged between the desulfurization tower and the dryer, and a valve is arranged on the pipe. The device and the process have the advantages that 1, saturated water included in raw material gas is compressed to be separated gradually effectively by multistage cooling separators, and accordingly, large pressure fluctuation of the compressor is relieved, shaking of the compressor caused by water carrying of the system is reduced, the safe and stable operation of equipment is protected; 2, water carried by the raw material gas is almost removed completely before desulfurization, water inlet damage failures of desulfurization agents in a purifier and fillers in the dryer can be prevented, the desulfurization rate of the fine desulfurization system is guaranteed, and good indexes and stability of food-grade carbon dioxide products can be maintained.

Description

The integrated food-grade, the technical grade CO that improve 2retracting device and recovery process
Technical field
The present invention relates to technical field of environmental protection in chemical industry, particularly a kind ofly can reclaim food-grade, the device of technical grade carbon dioxide and technique simultaneously.
Background technology
Reducing CO2 emission, utilize carbon dioxide recovery, alleviate greenhouse effects, is that whole world the country and people cherishes the earth that the mankind depend on for existence and the target of making joint efforts.
Integration food-grade, technical grade carbon dioxide recovering apparatus and recovery process (country origin: China, publication number: 103359732A, publication date: 2013-10-23), disclose one and realize technical grade by switching annexation in same device, the retracting device of food-grade carbon-dioxide production and recovery process, the production line of technical grade carbon dioxide product increases simple fine de-sulfur system and produces food-grade carbon-dioxide product, and the food-grade carbon-dioxide total sulfur content produced is less than 0.1ppm, solving to produce in food-grade carbon-dioxide product process needs to increase complicated sulfur removal technology and the problem of energy consumption, technique is simple, energy consumption reduces, automaticity is high, waste discharge is few.
This retracting device is after the operation of certain hour, repeatedly occur that carbon-dioxide gas compressor shakes large situation, equipment is caused to there occurs the phenomenon occurring the parts rapid wears such as obvious crackle, air valve, hampered equipment safe, normally run, even there is the phenomenon of product sulfur content, ash content, Moisture high UCL, product does not reach food-grade index, this retracting device is used for integrated production food-grade, the object of technical grade carbon dioxide fails effectively to realize, and productive rate, the quality of food-grade carbon-dioxide reduce.
Summary of the invention
Goal of the invention: for the problems referred to above, the object of this invention is to provide a kind of integrated food-grade of improvement, technical grade CO 2retracting device and recovery process, improve the production stability of device, improve the validity of its desulfurization, ensures the steady quality of food-grade carbon-dioxide product.
Technical scheme: a kind of integrated food-grade of improvement, technical grade CO 2retracting device, comprise carbon-dioxide gas compressor, desulfurizing tower, fine de-sulfur system, drier, liquefier, rectifying column, reboiler, subcooler that mass transport direction connects successively, between desulfurizing tower and drier, connecting pipe is set, this pipeline arranges valve, between described carbon-dioxide gas compressor and described desulfurizing tower, is also connected with cooling separator, surge tank in turn.
Described cooling separator is at least set to one-level, and described surge tank is connected to after the described cooling separator of final stage.When described cooling separator is at least set to two-stage, the separative efficiency of every grade is successively decreased along mass transport direction.
Described fine de-sulfur system, comprises temperature raising device, hydrolysis tower and purifier that mass transport direction connects successively.
Above arbitrary described retracting device is utilized to carry out integrated food-grade, technical grade CO 2the technique reclaimed, the unstripped gas containing carbon dioxide after compressor supercharging, more progressively isolates moisture through cooling separator, and moisture is discharged by surge tank, then passes into the thick desulfurization of desulfurizing tower, removes the H in unstripped gas 2s;
Manufacture grade carbon-dioxide, then the material after thick desulfurization directly enters drier and carries out drying; Dried material enters liquefier, and with liquefied ammonia heat exchange, carbon dioxide condensing also enters rectifying column and carries out rectifying; Incoagulable gas in rectifying column Raw gas upwards evaporates, and is released by the pressure-control valve of tower top; Carbon dioxide liquid at the bottom of rectifying column enters reboiler; After the heating of reboiler gas ammonia, in liquid, incoagulable gas is again evaporated to rectifying column and releases, the carbon dioxide liquid in reboiler through subcooler cross cold after obtain technical grade carbon dioxide product; Gained technical grade carbon dioxide product purity reaches 99.99%;
Production food-grade carbon-dioxide, then the material after thick desulfurization was introduced into fine de-sulfur system fine de-sulfur before entering drier drying; Gained food-grade carbon-dioxide product total sulfur content is at below 0.1ppm.
Beneficial effect: compared with prior art, advantage of the present invention is: the saturation water 1, contained in unstripped gas after compression, by multistage cooling separator, moisture is progressively effectively separated, alleviate the pressure oscillation that compressor is larger, reduce the shock conditions that compressor causes because of rear system band water, proterctive equipment safety, even running; 2, unstripped gas is before carrying out desulfurization, namely almost entrained moisture is stripped of completely, can not cause into water broken invalid to filler in desulfurizing agent, drier in purifier, ensure that food-grade carbon-dioxide product can be kept the good and stable of index by the desulfurization degree of fine de-sulfur system.
Accompanying drawing explanation
Accompanying drawing is retracting device structural representation of the present invention.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, illustrate the present invention further, these embodiments should be understood only be not used in for illustration of the present invention and limit the scope of the invention, after having read the present invention, the amendment of those skilled in the art to the various equivalent form of value of the present invention has all fallen within the application's claims limited range.
A kind of integrated food-grade of improvement, technical grade CO 2retracting device, for the following problem that former retracting device occurs after operation, seeking solution.Retracting device has occurred that carbon-dioxide gas compressor shakes large situation repeatedly, and obvious crackle often appears in apparatus body, pipeline place, and the damage phenomenon that the frequency is higher has also appearred in the parts such as air valve; There is the phenomenon of sulfur content, ash content, Moisture high UCL in product, product does not reach food-grade index, and productive rate, the quality of food-grade carbon-dioxide reduce.
By analysis, the saturation water that the reason that above problem exists mainly contains in unstripped gas after compression, carbon-dioxide gas compressor can not effectively be separated, and causes compressor to shake large, rear system band water, cause desulfurizing agent water inlet broken invalid in purifier, product sulfur content exceeds standard, and does not reach food grade standard, causes filler water inlet broken invalid in drier, product ash content exceeds standard, and sometimes product moisture also exceeds standard.
As shown in drawings, for this reason, retracting device of the present invention comprises carbon-dioxide gas compressor, cooling separator, surge tank, desulfurizing tower, fine de-sulfur system, drier, liquefier, rectifying column, reboiler, the subcooler that mass transport direction connects successively, connecting pipe is set between desulfurizing tower and drier, this pipeline arranges valve.Fine de-sulfur system, comprises temperature raising device, hydrolysis tower and purifier that mass transport direction connects successively.
Cooling separator is used for draining, be at least one-level when arranging, multistage when arranging, surge tank is connected to after the cooling separator of final stage, and the separative efficiency of every grade of cooling separator is designed to successively decrease along mass transport direction, the steam contained almost can be separated completely in unstripped gas.
Before surge tank is arranged on material desulfurization, carry out draining, drainage effect is remarkable.
This retracting device carries out integrated food-grade, technical grade CO 2the technique reclaimed, the unstripped gas containing carbon dioxide after compressor supercharging, more progressively isolates moisture through cooling separator, and moisture is discharged by surge tank, then passes into the thick desulfurization of desulfurizing tower, removes the H in unstripped gas 2s;
Manufacture grade carbon-dioxide, then the material after thick desulfurization directly enters drier and carries out drying; Dried material enters liquefier, and with liquefied ammonia heat exchange, carbon dioxide condensing also enters rectifying column and carries out rectifying; Incoagulable gas in rectifying column Raw gas upwards evaporates, and is released by the pressure-control valve of tower top; Carbon dioxide liquid at the bottom of rectifying column enters reboiler; After the heating of reboiler gas ammonia, in liquid, incoagulable gas is again evaporated to rectifying column and releases, the carbon dioxide liquid in reboiler through subcooler cross cold after obtain technical grade carbon dioxide product; Gained technical grade carbon dioxide product purity reaches 99.99%;
Production food-grade carbon-dioxide, then the material after thick desulfurization was introduced into fine de-sulfur system fine de-sulfur before entering drier drying; Gained food-grade carbon-dioxide product total sulfur content is at below 0.1ppm.
Retracting device after adopting the present invention to improve and recovery process, make the recovery of integrated food-grade, technical grade carbon dioxide, operation conditions stability is significantly improved, Plant in good condition, product total sulfur content can reach food grade standard≤0.1ppm, and water disrepair phenomenon is not with by desulfurizing agent, and drying system filler does not occur disrepair phenomenon, rear system does not occur that evaporation residue exceeds standard (≤10ppm), Moisture high UCL (≤20ppm) phenomenon.

Claims (5)

1. integrated food-grade, the technical grade CO improved 2retracting device, comprise carbon-dioxide gas compressor, desulfurizing tower, fine de-sulfur system, drier, liquefier, rectifying column, reboiler, subcooler that mass transport direction connects successively, between desulfurizing tower and drier, connecting pipe is set, this pipeline arranges valve, it is characterized in that: between described carbon-dioxide gas compressor and described desulfurizing tower, be also connected with cooling separator, surge tank in turn.
2. integrated food-grade, the technical grade CO of improvement according to claim 1 2retracting device, is characterized in that: described cooling separator is at least set to one-level, and described surge tank is connected to after the described cooling separator of final stage.
3. integrated food-grade, the technical grade CO of improvement according to claim 2 2retracting device, is characterized in that: described cooling separator is at least set to two-stage, and the separative efficiency of every grade is successively decreased along mass transport direction.
4. integrated food-grade, the technical grade CO of improvement according to claim 1 2retracting device, is characterized in that: described fine de-sulfur system, comprises temperature raising device, hydrolysis tower and purifier that mass transport direction connects successively.
5. utilize the arbitrary described retracting device of claim 1-4 to carry out integrated food-grade, technical grade CO 2the technique reclaimed, is characterized in that: the unstripped gas containing carbon dioxide after compressor supercharging, more progressively isolates moisture through cooling separator, and moisture is discharged by surge tank, then passes into the thick desulfurization of desulfurizing tower, remove the H in unstripped gas 2s;
Manufacture grade carbon-dioxide, then the material after thick desulfurization directly enters drier and carries out drying; Dried material enters liquefier, and with liquefied ammonia heat exchange, carbon dioxide condensing also enters rectifying column and carries out rectifying; Incoagulable gas in rectifying column Raw gas upwards evaporates, and is released by the pressure-control valve of tower top; Carbon dioxide liquid at the bottom of rectifying column enters reboiler; After the heating of reboiler gas ammonia, in liquid, incoagulable gas is again evaporated to rectifying column and releases, the carbon dioxide liquid in reboiler through subcooler cross cold after obtain technical grade carbon dioxide product; Gained technical grade carbon dioxide product purity reaches 99.99%;
Production food-grade carbon-dioxide, then the material after thick desulfurization was introduced into fine de-sulfur system fine de-sulfur before entering drier drying; Gained food-grade carbon-dioxide product total sulfur content is at below 0.1ppm.
CN201510337785.6A 2015-06-17 2015-06-17 Improved integrated food-grade industrial-grade CO2 recovery device and process Pending CN104896873A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510337785.6A CN104896873A (en) 2015-06-17 2015-06-17 Improved integrated food-grade industrial-grade CO2 recovery device and process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510337785.6A CN104896873A (en) 2015-06-17 2015-06-17 Improved integrated food-grade industrial-grade CO2 recovery device and process

Publications (1)

Publication Number Publication Date
CN104896873A true CN104896873A (en) 2015-09-09

Family

ID=54029692

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510337785.6A Pending CN104896873A (en) 2015-06-17 2015-06-17 Improved integrated food-grade industrial-grade CO2 recovery device and process

Country Status (1)

Country Link
CN (1) CN104896873A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105439145A (en) * 2016-01-12 2016-03-30 广西新天德能源有限公司 Biological fermentation waste carbon dioxide recovery and purification device
CN109163504A (en) * 2018-10-11 2019-01-08 欧中电子材料(重庆)有限公司 The preparation process and device of electronics grade carbon-dioxide
CN110160316A (en) * 2019-04-26 2019-08-23 大连伊立特科技有限公司 Dry-ice machine CO 2 waste gas processing unit
CN110801639A (en) * 2019-11-11 2020-02-18 杭州快凯高效节能新技术有限公司 Method for recovering carbon dioxide by multistage liquefaction and fractional refrigeration of industrial tail gas

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2606739Y (en) * 2003-03-14 2004-03-17 大连理工大学 CO2 purifying device by adsorptive fine disstillation
CN101343061A (en) * 2008-08-15 2009-01-14 杭州快凯高效节能新技术有限公司 Method and apparatus for preparing food level liquid carbon dioxide with flue gas
WO2011026587A1 (en) * 2009-09-03 2011-03-10 Linde-Kca-Dresden Gmbh Method and device for treating a carbon dioxide-containing gas flow, wherein the energy of the vent gas (work and cold due to expansion) is used
CN102303865A (en) * 2011-08-15 2012-01-04 安庆凯美特气体有限公司 Improved production method of food-grade liquid carbon dioxide product
US20120006054A1 (en) * 2010-07-09 2012-01-12 Arnold Keller Carbon dioxide capture and liquefaction
CN102449124A (en) * 2009-05-26 2012-05-09 巴斯夫欧洲公司 Process for recovery of carbon dioxide from a fluid stream, in particular from syngas
CN202265414U (en) * 2011-10-26 2012-06-06 唐加彬 Carbon dioxide collection system preventing pipeline vibration
CN202281455U (en) * 2011-10-26 2012-06-20 唐加彬 Collecting system for carbon dioxide
JP2013013876A (en) * 2011-07-06 2013-01-24 Jfe Steel Corp Apparatus and method for recovering co2
CN103359732A (en) * 2013-06-24 2013-10-23 江苏索普(集团)有限公司 Integrated food grade/industrial grade carbon dioxide recovery device and recovery process
CN204739844U (en) * 2015-06-17 2015-11-04 镇江索普天辰碳回收有限公司 Modified integration food level, industrial grade CO2 recovery unit

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2606739Y (en) * 2003-03-14 2004-03-17 大连理工大学 CO2 purifying device by adsorptive fine disstillation
CN101343061A (en) * 2008-08-15 2009-01-14 杭州快凯高效节能新技术有限公司 Method and apparatus for preparing food level liquid carbon dioxide with flue gas
CN102449124A (en) * 2009-05-26 2012-05-09 巴斯夫欧洲公司 Process for recovery of carbon dioxide from a fluid stream, in particular from syngas
WO2011026587A1 (en) * 2009-09-03 2011-03-10 Linde-Kca-Dresden Gmbh Method and device for treating a carbon dioxide-containing gas flow, wherein the energy of the vent gas (work and cold due to expansion) is used
US20120006054A1 (en) * 2010-07-09 2012-01-12 Arnold Keller Carbon dioxide capture and liquefaction
JP2013013876A (en) * 2011-07-06 2013-01-24 Jfe Steel Corp Apparatus and method for recovering co2
CN102303865A (en) * 2011-08-15 2012-01-04 安庆凯美特气体有限公司 Improved production method of food-grade liquid carbon dioxide product
CN202265414U (en) * 2011-10-26 2012-06-06 唐加彬 Carbon dioxide collection system preventing pipeline vibration
CN202281455U (en) * 2011-10-26 2012-06-20 唐加彬 Collecting system for carbon dioxide
CN103359732A (en) * 2013-06-24 2013-10-23 江苏索普(集团)有限公司 Integrated food grade/industrial grade carbon dioxide recovery device and recovery process
CN204739844U (en) * 2015-06-17 2015-11-04 镇江索普天辰碳回收有限公司 Modified integration food level, industrial grade CO2 recovery unit

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李凤: ""制氢装置尾气中二氧化碳的回收和利用"", 《石化技术》 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105439145A (en) * 2016-01-12 2016-03-30 广西新天德能源有限公司 Biological fermentation waste carbon dioxide recovery and purification device
CN105439145B (en) * 2016-01-12 2019-02-19 广西新天德能源有限公司 Biofermentation discards carbon dioxide recovery purification devices
CN109163504A (en) * 2018-10-11 2019-01-08 欧中电子材料(重庆)有限公司 The preparation process and device of electronics grade carbon-dioxide
CN110160316A (en) * 2019-04-26 2019-08-23 大连伊立特科技有限公司 Dry-ice machine CO 2 waste gas processing unit
CN110160316B (en) * 2019-04-26 2024-04-12 大连伊立特科技有限公司 Carbon dioxide waste gas treatment device of dry ice machine
CN110801639A (en) * 2019-11-11 2020-02-18 杭州快凯高效节能新技术有限公司 Method for recovering carbon dioxide by multistage liquefaction and fractional refrigeration of industrial tail gas

Similar Documents

Publication Publication Date Title
CN101342441B (en) Method for treating tail gas of acyl chlorination
CN100579631C (en) Method for recovery of carbon dioxide from gas, use thereof and device for recovery of carbon dioxide
CN104896873A (en) Improved integrated food-grade industrial-grade CO2 recovery device and process
CN101538040B (en) Method for coproducing or singly producing food grade carbon dioxide and industrial grade carbon dioxide by utilizing industrial waste gas
CN102564062B (en) Method for extracting high-purity liquid neon
CN103277980B (en) Carbon dioxide capture device utilizing both part oxygen-enriched combustion and nitrogen-and-oxygen separation
CN101846436A (en) Full-liquid air separation device using cold energy of liquefied natural gas (LNG)
CN105110304B (en) The apparatus and method for preparing high-purity nitrous oxide using adipic acid production tail gas
CN204897856U (en) Membrane separation marsh gas purification system
CN204739844U (en) Modified integration food level, industrial grade CO2 recovery unit
CN105502294B (en) A kind of electronic grade high-purity hydrogen chloride high pressure method for preparing
CN105413429A (en) Method for separating and purifying lime kiln tail gas
CN105289256A (en) Method used for recycling carbon dioxide from exhaust gas obtained via alcoholic fermentation
CN111991997A (en) Method and equipment for recovering high-concentration dichloromethane in tail gas
CN104560254A (en) Freeze-drying, purification and dehydration process of natural gas
CN106440661B (en) Energy-saving device and method for preparing high-purity liquid carbon dioxide
CN210825439U (en) System for synchronous carbon dioxide and nitrogen recovery of coal fired power plant boiler flue gas
CN114518016A (en) Carbon dioxide capturing, liquefying and recycling device and method
CN104457138A (en) Method for recovering carbon sulfide and hydrogen in separation mode
CN103466550B (en) Recovery system of D-acid esterification tail gas in amoxicillin production technology
CN103361138B (en) Method for preparing liquefied natural gas and synthesis ammonia raw material gases by use of hydrogen extraction desorption gas
CN108821290B (en) Production device and method of carbon dioxide
CN204151077U (en) The device of a kind of Separation and Recovery dithiocarbonic anhydride and nitrogen
CN205011723U (en) Rely on device of low temperature methanol solution desorption synthetic natural gas normal water
CN107837641A (en) A kind of tail gas recycle recycling processing method and change system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20150909

RJ01 Rejection of invention patent application after publication