JPS6443329A - Gas separation method employing two kinds of membranes - Google Patents

Gas separation method employing two kinds of membranes

Info

Publication number
JPS6443329A
JPS6443329A JP20033387A JP20033387A JPS6443329A JP S6443329 A JPS6443329 A JP S6443329A JP 20033387 A JP20033387 A JP 20033387A JP 20033387 A JP20033387 A JP 20033387A JP S6443329 A JPS6443329 A JP S6443329A
Authority
JP
Japan
Prior art keywords
gas
pass
components
volatile
membrane
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
JP20033387A
Other languages
Japanese (ja)
Inventor
Moritaka Kato
Norio Inoue
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP20033387A priority Critical patent/JPS6443329A/en
Publication of JPS6443329A publication Critical patent/JPS6443329A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To make it easy to control the dew point in the removal of low- volatile components, by allowing a mixed gas composed of at least any of H2, CO2 and CO and a volatile hydrocarbon gas to pass through two membrane modules having different adsorption rates for specific components. CONSTITUTION:A mixed gas composed of any of H2, CO2 and CO gases and a gas of volatile hydrocarbons is allowed to pass through a first-step membrane module through which high boiling-point components in the volatile hydrocarbon gas pass faster than methane. Subsequently, H2, CO2 or CO is separated from the resulting mixed gas by allowing the gas of H2, CO2 or CO to pass faster than the volatile hydrocarbon gas components. For example, by the use of a silicon membrane for the first-step membrane module 1 and a cellulose membrane or a second-step membrane module 2, a natural gas having a CO2 concentration of 6.23vol.% is allowed to pass through the modules, thereby obtaining a pipeline gas having a CO2 concentration of 2vol.%.
JP20033387A 1987-08-11 1987-08-11 Gas separation method employing two kinds of membranes Pending JPS6443329A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20033387A JPS6443329A (en) 1987-08-11 1987-08-11 Gas separation method employing two kinds of membranes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20033387A JPS6443329A (en) 1987-08-11 1987-08-11 Gas separation method employing two kinds of membranes

Publications (1)

Publication Number Publication Date
JPS6443329A true JPS6443329A (en) 1989-02-15

Family

ID=16422552

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20033387A Pending JPS6443329A (en) 1987-08-11 1987-08-11 Gas separation method employing two kinds of membranes

Country Status (1)

Country Link
JP (1) JPS6443329A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5401300A (en) * 1993-10-25 1995-03-28 Membrane Technology And Research, Inc. Sour gas treatment process including dehydration of the gas stream
WO1995011739A1 (en) * 1993-10-25 1995-05-04 Membrane Technology And Research, Inc. Membrane and non-membrane sour gas treatment process
WO1995011738A1 (en) * 1993-10-25 1995-05-04 Membrane Technology And Research, Inc. Sour gas treatment process
US5482539A (en) * 1993-09-22 1996-01-09 Enerfex, Inc. Multiple stage semi-permeable membrane process and apparatus for gas separation
US6085549A (en) * 1998-04-08 2000-07-11 Messer Griesheim Industries, Inc. Membrane process for producing carbon dioxide
US6128919A (en) * 1998-04-08 2000-10-10 Messer Griesheim Industries, Inc. Process for separating natural gas and carbon dioxide
US6565626B1 (en) 2001-12-28 2003-05-20 Membrane Technology And Research, Inc. Natural gas separation using nitrogen-selective membranes
US6572679B2 (en) 2000-05-19 2003-06-03 Membrane Technology And Research, Inc. Gas separation using organic-vapor-resistant membranes in conjunction with organic-vapor-selective membranes
US6572678B1 (en) 2001-12-28 2003-06-03 Membrane Technology And Research, Inc. Natural gas separation using nitrogen-selective membranes of modest selectivity
US6648944B1 (en) 2003-01-28 2003-11-18 Membrane Technology And Research, Inc. Carbon dioxide removal process
WO2017056134A1 (en) * 2015-10-01 2017-04-06 日揮株式会社 Nonhydrocarbon gas separation device and nonhydrocarbon gas separation method
WO2017056135A1 (en) * 2015-10-01 2017-04-06 日揮株式会社 Nonhydrocarbon gas separation device and nonhydrocarbon gas separation method

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5482539A (en) * 1993-09-22 1996-01-09 Enerfex, Inc. Multiple stage semi-permeable membrane process and apparatus for gas separation
US5873928A (en) * 1993-09-22 1999-02-23 Enerfex, Inc. Multiple stage semi-permeable membrane process and apparatus for gas separation
US5401300A (en) * 1993-10-25 1995-03-28 Membrane Technology And Research, Inc. Sour gas treatment process including dehydration of the gas stream
WO1995011739A1 (en) * 1993-10-25 1995-05-04 Membrane Technology And Research, Inc. Membrane and non-membrane sour gas treatment process
WO1995011738A1 (en) * 1993-10-25 1995-05-04 Membrane Technology And Research, Inc. Sour gas treatment process
WO1995011737A1 (en) * 1993-10-25 1995-05-04 Membrane Technology And Research, Inc. Sour gas membrane treatment process including dehydration
WO1996011048A1 (en) * 1994-10-11 1996-04-18 Enerfex, Inc. Multiple stage semi-permeable membrane gas separation process
US6128919A (en) * 1998-04-08 2000-10-10 Messer Griesheim Industries, Inc. Process for separating natural gas and carbon dioxide
US6085549A (en) * 1998-04-08 2000-07-11 Messer Griesheim Industries, Inc. Membrane process for producing carbon dioxide
US6572679B2 (en) 2000-05-19 2003-06-03 Membrane Technology And Research, Inc. Gas separation using organic-vapor-resistant membranes in conjunction with organic-vapor-selective membranes
US6565626B1 (en) 2001-12-28 2003-05-20 Membrane Technology And Research, Inc. Natural gas separation using nitrogen-selective membranes
US6572678B1 (en) 2001-12-28 2003-06-03 Membrane Technology And Research, Inc. Natural gas separation using nitrogen-selective membranes of modest selectivity
US6648944B1 (en) 2003-01-28 2003-11-18 Membrane Technology And Research, Inc. Carbon dioxide removal process
WO2017056134A1 (en) * 2015-10-01 2017-04-06 日揮株式会社 Nonhydrocarbon gas separation device and nonhydrocarbon gas separation method
WO2017056135A1 (en) * 2015-10-01 2017-04-06 日揮株式会社 Nonhydrocarbon gas separation device and nonhydrocarbon gas separation method
US10737214B2 (en) 2015-10-01 2020-08-11 Jgc Corporation Nonhydrocarbon gas separation device and nonhydrocarbon gas separation method
US10744455B2 (en) 2015-10-01 2020-08-18 Jgc Corporation Nonhydrocarbon gas separation device and nonhydrocarbon gas separation method
AU2015410455B2 (en) * 2015-10-01 2022-03-03 Jgc Corporation Nonhydrocarbon gas separation device and nonhydrocarbon gas separation method

Similar Documents

Publication Publication Date Title
JPS6443329A (en) Gas separation method employing two kinds of membranes
MY131778A (en) Hydrogen recovery by adsorbent membranes
KR910009323A (en) Oversorption Recovery System in Pressure Swing Adsorption
CA2005946A1 (en) Composition and method for sweetening hydrocarbon
EP0579289A3 (en) Separation of gas mixtures
DK1627041T3 (en) Progress seed and gas separation apparatus
ES462788A1 (en) Hydrogen purification by selective adsorption
KR920006229A (en) Integrated method for producing carbon monoxide
EP0326360A3 (en) Process for selectively separating water vapour from a gaseous mixture
BR0000842A (en) Single bed pressure oscillation flow control process and system
DE68911179D1 (en) Membrane process for the recovery of liquid hydrocarbons.
EP0358915A3 (en) Prevention of membrane degradation
KR880005958A (en) Separation Process of Gas Stream Components
RU94039537A (en) Method to extract ethylene from gass-shaped hydrocarbons
SE0002037D0 (en) Method of operating a combustion plant as well as a combustion plant
AR016142A1 (en) PROCEDURE FOR SEPARATION / RECOVERY OF GASES THROUGH A MEMBRANE / PRESSURE SWING ADSORTION SYSTEM (AOP)
ATE261759T1 (en) ARRANGEMENT FOR REMOVING WATER VAPOR FROM GASES OR GAS MIXTURES CONTAINING HYDROCARBON UNDER PRESSURE
CA2032560A1 (en) Process and apparatus for removing carbon monoxide from a gaseous mixture containing hydrogen
NO893574L (en) PROCEDURE AND APPARATUS FOR SEPARATING A COMPONENT WITH INTERMEDIATE PERMISSIBILITY FROM A GAS MIXTURE.
ATA630477A (en) MEBRANE METHOD FOR SEPARATING A GASEOUS ALIPHATICALLY UNSATURATED CARBON HYDROGEN, SUCH AS e.g. AETHYLENE, OR MIXED SUCH HYDROCARBONS FROM A GAS MIXTURE
EP0878533A3 (en) Process and apparatus for the photobiological separation of carbondioxide and methane containing gases
GB995548A (en) Separating water and hydrocarbons from natural gas
PL371266A1 (en) A separation method and separation apparatus of isotopes from gaseous substances
WO1992013628A3 (en) Gas separations utilizing glassy polymer membranes at sub-ambient temperatures
ATE86137T1 (en) DEVICE FOR RECOVERING HYDROCARBONS FROM HIGHLY CONCENTRATED GAS STREAM.