JPS5490073A - Mixed gas concentrator - Google Patents

Mixed gas concentrator

Info

Publication number
JPS5490073A
JPS5490073A JP15802977A JP15802977A JPS5490073A JP S5490073 A JPS5490073 A JP S5490073A JP 15802977 A JP15802977 A JP 15802977A JP 15802977 A JP15802977 A JP 15802977A JP S5490073 A JPS5490073 A JP S5490073A
Authority
JP
Japan
Prior art keywords
air
chamber
adsorption
adsorbent
tower
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
JP15802977A
Other languages
Japanese (ja)
Inventor
Tatsuo Amitani
Takei Kubo
Kiyohiro Koga
Jun Izumi
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP15802977A priority Critical patent/JPS5490073A/en
Publication of JPS5490073A publication Critical patent/JPS5490073A/en
Pending legal-status Critical Current

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  • Separation Of Gases By Adsorption (AREA)

Abstract

PURPOSE: To provide a mixed gas concentrator which accomplish an excellent adsorption and desorption through the control of the temperature in an adsorption chamber under a specified value by means of a fin tube arranged for temperature control in the adsorption chamber.
CONSTITUTION: In concnetrating O2 from air, air D is sent to an adosrption chamber 5' in an adsorption tower 5, while a cooling fluid is allowed to flow from a cooler 21 through a fin tube 33 to the temperature in the chamber 5', improving the effect of adsorbing moisture and N2 in air. The air thus O2-enriched is delivered through a pipe 16. Air for regenerating an adsorbent is allowed to flow through a pressure-reducing valve 19 to reduce the pressure thereof and then proceed to an adsorption chamber 6' in an adsorption tower 6. On the other hand, the cooling fluid from the fin tube 33 is cooled by the cooler 21 and returns to the adsorption chamber 5'. Air containing moisture and N2 which are desorbed from an adsorbent under a pressure reduced atmosphere in the chamber 6' is discharged out through a pipe 15. In additional, a remaining part of the air is adsorbed by the tower 5 and discharged out. The regeneration of the adsorbent is performed in the adsorption tower 5 while the concentration of O2 in the tower 6. Here, a heating fluid is introduced into the tube 33 of the chamber 5 and a cooling fluid, a fin tube 34. With such an arrangement, the adsorbing and desorbing capacity of the adsorbent is incre ased, thus producing O2-enriched air at a lower cost.
COPYRIGHT: (C)1979,JPO&Japio
JP15802977A 1977-12-28 1977-12-28 Mixed gas concentrator Pending JPS5490073A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15802977A JPS5490073A (en) 1977-12-28 1977-12-28 Mixed gas concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15802977A JPS5490073A (en) 1977-12-28 1977-12-28 Mixed gas concentrator

Publications (1)

Publication Number Publication Date
JPS5490073A true JPS5490073A (en) 1979-07-17

Family

ID=15662708

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15802977A Pending JPS5490073A (en) 1977-12-28 1977-12-28 Mixed gas concentrator

Country Status (1)

Country Link
JP (1) JPS5490073A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60153919A (en) * 1984-01-25 1985-08-13 Hitachi Ltd Adsorption and regeneration of adsorbing tower
JPS6391120A (en) * 1986-10-01 1988-04-21 ザ・ビ−オ−シ−・グル−プ・インコ−ポレ−テッド Pressure change-over apparatus
JPH0381515A (en) * 1989-08-25 1991-04-05 Daiwa Kogyo Kk Treatment device of combustion gas
CN103007679A (en) * 2012-12-18 2013-04-03 上海龙净环保科技工程有限公司 Flue gas cleaning system capable of switching pollutant desorption technology and adsorbent regeneration technology and method thereof

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60153919A (en) * 1984-01-25 1985-08-13 Hitachi Ltd Adsorption and regeneration of adsorbing tower
JPH0248287B2 (en) * 1984-01-25 1990-10-24 Hitachi Seisakusho Kk
JPS6391120A (en) * 1986-10-01 1988-04-21 ザ・ビ−オ−シ−・グル−プ・インコ−ポレ−テッド Pressure change-over apparatus
JPH0565206B2 (en) * 1986-10-01 1993-09-17 Boc Group Inc
JPH0381515A (en) * 1989-08-25 1991-04-05 Daiwa Kogyo Kk Treatment device of combustion gas
CN103007679A (en) * 2012-12-18 2013-04-03 上海龙净环保科技工程有限公司 Flue gas cleaning system capable of switching pollutant desorption technology and adsorbent regeneration technology and method thereof
CN103007679B (en) * 2012-12-18 2014-09-03 上海龙净环保科技工程有限公司 Flue gas cleaning system capable of switching pollutant desorption technology and adsorbent regeneration technology and method thereof

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