GB930682A - Improvements in and relating to the low temperature separation of gases - Google Patents

Improvements in and relating to the low temperature separation of gases

Info

Publication number
GB930682A
GB930682A GB2481358A GB2481358A GB930682A GB 930682 A GB930682 A GB 930682A GB 2481358 A GB2481358 A GB 2481358A GB 2481358 A GB2481358 A GB 2481358A GB 930682 A GB930682 A GB 930682A
Authority
GB
United Kingdom
Prior art keywords
duct
hydrogen
carbon monoxide
exchanger
mixture
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
Application number
GB2481358A
Inventor
Martin Siegfried Will Ruhemann
William Leslie Seddon
Joseph Weinreb
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.)
Petrocarbon Developments Ltd
Original Assignee
Petrocarbon Developments 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
Priority to BE581236D priority Critical patent/BE581236A/xx
Application filed by Petrocarbon Developments Ltd filed Critical Petrocarbon Developments Ltd
Priority to GB2481358A priority patent/GB930682A/en
Priority to FR801599A priority patent/FR1233248A/en
Publication of GB930682A publication Critical patent/GB930682A/en
Expired legal-status Critical Current

Links

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
    • F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
    • F25J3/0665—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of carbon monoxide
    • 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
    • F25J3/0204—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 characterised by the feed stream
    • F25J3/0209—Natural gas or substitute natural gas
    • 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
    • F25J3/0204—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 characterised by the feed stream
    • F25J3/0219—Refinery gas, cracking gas, coke oven gas, gaseous mixtures containing aliphatic unsaturated CnHm or gaseous mixtures of undefined nature
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    • 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
    • F25J3/0204—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 characterised by the feed stream
    • F25J3/0223—H2/CO mixtures, i.e. synthesis gas; Water gas or shifted synthesis gas
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    • F25J3/0228—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 characterised by the separated product stream
    • F25J3/0233—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 characterised by the separated product stream separation of CnHm with 1 carbon atom or more
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    • F25J3/0228—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 characterised by the separated product stream
    • F25J3/0242—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 characterised by the separated product stream separation of CnHm with 3 carbon atoms or more
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    • 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
    • F25J3/0228—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 characterised by the separated product stream
    • F25J3/0252—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 characterised by the separated product stream separation of hydrogen
    • 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
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    • F25J3/0228—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 characterised by the separated product stream
    • F25J3/0257—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 characterised by the separated product stream separation of nitrogen
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    • 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
    • F25J3/0228—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 characterised by the separated product stream
    • F25J3/028—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 characterised by the separated product stream separation of noble gases
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    • 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
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    • F25J3/0228—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 characterised by the separated product stream
    • F25J3/028—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 characterised by the separated product stream separation of noble gases
    • F25J3/029—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 characterised by the separated product stream separation of noble gases of helium
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    • 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
    • F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/0605—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the feed stream
    • F25J3/0625—H2/CO mixtures, i.e. synthesis gas; Water gas or shifted synthesis gas
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    • 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
    • F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
    • F25J3/0655—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of hydrogen
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    • 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
    • F25J2200/00—Processes or apparatus using separation by rectification
    • F25J2200/38—Processes or apparatus using separation by rectification using pre-separation or distributed distillation before a main column system, e.g. in a at least a double column system
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    • F25J2200/00—Processes or apparatus using separation by rectification
    • F25J2200/80—Processes or apparatus using separation by rectification using integrated mass and heat exchange, i.e. non-adiabatic rectification in a reflux exchanger or dephlegmator
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    • F25J2270/00—Refrigeration techniques used
    • F25J2270/42—Quasi-closed internal or closed external nitrogen refrigeration cycle

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

930,682. Cold separation of gas mixtures. PETROCARBON DEVELOPMENTS Ltd. July 30, 1959 [Aug. 1, 1958], No. 24813/58. Class 8(2). In cooling a compressed gas mixture e.g., hydrogen and carbon monoxide in heat exchangers 1, 2, Fig. 1, traversed by the cold products of separating, the cooling being sufficient to condense the less volatile component prior to separation in a chamber 3, part of the cold requirements of heat exchanger 2 is met by evaporating a portion of the separated liquid i.e. carbon monoxide in direct contact with a portion of the uncondensed hydrogen at a pressure intermediate that of the initial mixture and atmospheric. In separation the separated hydrogen after leaving exchangers 1, 2 through a duct 26 is expanded in a turbine 4 and a portion thereof is fed into a duct 211 where it is joined by liquid carbon monoxide after expansion in a valve 6 before traversing a duct 213 passing through exchangers 2, 1. The remaining expanded hydrogen gas in a duct 28 also serves to cool the exchangers. In a modification wherein ethylene, methane and hydrogen are separated from a mixture also containing nitrogen and carbon monoxide, the incoming mixture in a duct 31, Fig. 2, is first cooled in an exchanger 11 in countercurrent flow to product methane in a duct 325, product hydrogen in a duct 317, ethylene in a duct 323 and a mixture of hydrogen, nitrogen and carbon monoxide in a duct 322 and after further cooling in an exchanger 12 is separated in a column 17 into condensed hydrocarbons which pass through a duct 34 into a further column (not shown) and into a gaseous mixture of nitrogen, hydrogen and carbon monoxide which is partially liquefied in an exchanger 15 and separated in a chamber 16 from which the condensed nitrogen and carbon monoxide is expanded at a valve 8 and is vaporized in duct 318 of exchanger 15 in direct contact with a portion of gaseous hydrogen from the chamber 16 after warming in exchangers 15, 13, 12 and expansion in a turbine 19. The remaining expanded hydrogen gas traverses a duct 315 of exchangers 15, 13, a duet 316 and the duct 317 of exchanger 11 whilst the hydrogen nitrogen mixture traverses ducts 320, 321 leading to the outlet duct 322. Methane and ethylene separated in the further column passes along ducts 35, 36 respectively to the outlets 325, 323. Reflux for column 17 is provided by an auxiliary nitrogen cycle comprising a compressor 18 discharging partly into an expansion turbine 20 which provides cold for exchanger 13 and partly through an expansion valve 9 provides cold for a condenser at the head of column 17.
GB2481358A 1958-08-01 1958-08-01 Improvements in and relating to the low temperature separation of gases Expired GB930682A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
BE581236D BE581236A (en) 1958-08-01
GB2481358A GB930682A (en) 1958-08-01 1958-08-01 Improvements in and relating to the low temperature separation of gases
FR801599A FR1233248A (en) 1958-08-01 1959-07-30 Improvements in non-condensable gas recovery processes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2481358A GB930682A (en) 1958-08-01 1958-08-01 Improvements in and relating to the low temperature separation of gases

Publications (1)

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GB930682A true GB930682A (en) 1963-07-10

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GB2481358A Expired GB930682A (en) 1958-08-01 1958-08-01 Improvements in and relating to the low temperature separation of gases

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BE (1) BE581236A (en)
FR (1) FR1233248A (en)
GB (1) GB930682A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3293869A (en) * 1964-02-10 1966-12-27 Phillips Petroleum Co Gas liquefaction with recombining of separated gas-liquid fractions
JPS5130026B1 (en) * 1971-04-20 1976-08-28
WO2009087324A2 (en) * 2008-01-10 2009-07-16 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Column for separating a carbon monoxide and nitrogen mixture by cryogenic distillation, and apparatus including such column
CN105605883A (en) * 2016-03-25 2016-05-25 北京中科瑞奥能源科技股份有限公司 Oxygen-bearing coalbed methane liquefaction separation system and technique
CN109437106A (en) * 2018-12-26 2019-03-08 浙江海畅气体有限公司 A kind of hydrogen purification device
WO2022106699A3 (en) * 2020-11-23 2022-09-29 Xenon Holding Gmbh Cryogenic process for obtaining product of value from a hydrogen-rich input gas

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1046640B (en) * 1957-07-04 1958-12-18 Linde Eismasch Ag Process and device for generating cold through work-performing relaxation
US3091097A (en) * 1960-08-11 1963-05-28 Ingersoll Rand Co Method of removing impurities from a compressed gas
GB1057020A (en) * 1964-12-17 1967-02-01 Petrocarbon Dev Ltd Recovery of hydrogen from a gas mixture

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3293869A (en) * 1964-02-10 1966-12-27 Phillips Petroleum Co Gas liquefaction with recombining of separated gas-liquid fractions
JPS5130026B1 (en) * 1971-04-20 1976-08-28
WO2009087324A2 (en) * 2008-01-10 2009-07-16 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Column for separating a carbon monoxide and nitrogen mixture by cryogenic distillation, and apparatus including such column
FR2926355A1 (en) * 2008-01-10 2009-07-17 Air Liquide COLUMN FOR SEPARATING A MIXTURE OF CARBON MONOXIDE AND NITROGEN BY CRYOGENIC DISTILLATION AND APPARATUS INCORPORATING SUCH A COLUMN.
WO2009087324A3 (en) * 2008-01-10 2013-03-21 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Column for separating a carbon monoxide and nitrogen mixture by cryogenic distillation, and apparatus including such column
CN105605883A (en) * 2016-03-25 2016-05-25 北京中科瑞奥能源科技股份有限公司 Oxygen-bearing coalbed methane liquefaction separation system and technique
CN109437106A (en) * 2018-12-26 2019-03-08 浙江海畅气体有限公司 A kind of hydrogen purification device
WO2022106699A3 (en) * 2020-11-23 2022-09-29 Xenon Holding Gmbh Cryogenic process for obtaining product of value from a hydrogen-rich input gas

Also Published As

Publication number Publication date
BE581236A (en)
FR1233248A (en) 1960-10-12

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