JPS5691802A - Selective gas permeable membrane cell - Google Patents

Selective gas permeable membrane cell

Info

Publication number
JPS5691802A
JPS5691802A JP17203479A JP17203479A JPS5691802A JP S5691802 A JPS5691802 A JP S5691802A JP 17203479 A JP17203479 A JP 17203479A JP 17203479 A JP17203479 A JP 17203479A JP S5691802 A JPS5691802 A JP S5691802A
Authority
JP
Japan
Prior art keywords
gas
cell units
enriched
permeable
cell
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
JP17203479A
Other languages
Japanese (ja)
Inventor
Yoshimasa Ito
Yukihiro Saito
Soji Tsuchiya
Shiro Asakawa
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP17203479A priority Critical patent/JPS5691802A/en
Publication of JPS5691802A publication Critical patent/JPS5691802A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE: To effectively obtain an objective enriched gas by using a cell fabricated by laminating cell units provided with an outlet for enriched gas at intervals of plural cell units group on the side of a permeated gas chamber whose both sides are formed of two selective permeable membranes.
CONSTITUTION: A still unused permeable mixed gas is flowed into a still unused permeable gas inlet 32 by turning a fan 35 by a motor 36, the gas is flowed through laminated cell units 20 by being accelerated by the fan 35. Since a gas flow control plate 37 is provided between the fan 35 and the cell unit 20, the gas uniformly flows through the cell units 20 without biasing to partial cell units. Part of still unused permeable mixed gas flowing through the cell units 20 passes through the gas permeable membrane 21 of the cell units 20, enriched there, and then taken out of the outlet 31 as an enriched gas. On the other hand, still unused permeated gas is partially flowed out of the outlet 33 by as much an amount as regulated by the flow control valve 38, and another part is circulated through a circulation path 34.
COPYRIGHT: (C)1981,JPO&Japio
JP17203479A 1979-12-26 1979-12-26 Selective gas permeable membrane cell Pending JPS5691802A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17203479A JPS5691802A (en) 1979-12-26 1979-12-26 Selective gas permeable membrane cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17203479A JPS5691802A (en) 1979-12-26 1979-12-26 Selective gas permeable membrane cell

Publications (1)

Publication Number Publication Date
JPS5691802A true JPS5691802A (en) 1981-07-25

Family

ID=15934294

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17203479A Pending JPS5691802A (en) 1979-12-26 1979-12-26 Selective gas permeable membrane cell

Country Status (1)

Country Link
JP (1) JPS5691802A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58221338A (en) * 1982-06-18 1983-12-23 Toyota Central Res & Dev Lab Inc Oxygen enriched air supply device
JPS59131229U (en) * 1982-03-26 1984-09-03 松下電器産業株式会社 Selective gas permeable membrane module
JPS61157323A (en) * 1984-12-28 1986-07-17 Tadahiro Omi Apparatus for purifying high purity hydrogen gas
JPS62125823A (en) * 1985-11-27 1987-06-08 Matsushita Electric Ind Co Ltd Oxygen enrichment membrane unit
WO2010104684A1 (en) * 2009-03-12 2010-09-16 Fluid Equipment Development Company, Llc Continuous process batch-operated reverse osmosis system with in-tank membranes and circulation of concentrate
US9975089B2 (en) 2016-10-17 2018-05-22 Fluid Equipment Development Company, Llc Method and system for performing a batch reverse osmosis process using a tank with a movable partition

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59131229U (en) * 1982-03-26 1984-09-03 松下電器産業株式会社 Selective gas permeable membrane module
JPS58221338A (en) * 1982-06-18 1983-12-23 Toyota Central Res & Dev Lab Inc Oxygen enriched air supply device
JPS61157323A (en) * 1984-12-28 1986-07-17 Tadahiro Omi Apparatus for purifying high purity hydrogen gas
JPS62125823A (en) * 1985-11-27 1987-06-08 Matsushita Electric Ind Co Ltd Oxygen enrichment membrane unit
WO2010104684A1 (en) * 2009-03-12 2010-09-16 Fluid Equipment Development Company, Llc Continuous process batch-operated reverse osmosis system with in-tank membranes and circulation of concentrate
US8231784B2 (en) 2009-03-12 2012-07-31 Fluid Equipment Development Company, Llc Continuous process batch-operated reverse osmosis system with in-tank membranes and circulation
US9975089B2 (en) 2016-10-17 2018-05-22 Fluid Equipment Development Company, Llc Method and system for performing a batch reverse osmosis process using a tank with a movable partition
US10293306B2 (en) 2016-10-17 2019-05-21 Fluid Equipment Development Company, Llc Method and system for performing a batch reverse osmosis process using a tank with a movable partition
US10710024B2 (en) 2016-10-17 2020-07-14 Fluid Equipment Development Company, Llc Method and system for performing a batch reverse osmosis process using a tank with a movable partition

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