JPS56125213A - Production and recovery of carbon dioxide from a carbon monoxide mixture - Google Patents

Production and recovery of carbon dioxide from a carbon monoxide mixture

Info

Publication number
JPS56125213A
JPS56125213A JP2656980A JP2656980A JPS56125213A JP S56125213 A JPS56125213 A JP S56125213A JP 2656980 A JP2656980 A JP 2656980A JP 2656980 A JP2656980 A JP 2656980A JP S56125213 A JPS56125213 A JP S56125213A
Authority
JP
Japan
Prior art keywords
absorption
carbon dioxide
sent
reformer
heater
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
JP2656980A
Other languages
Japanese (ja)
Inventor
Noriaki Yamamoto
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP2656980A priority Critical patent/JPS56125213A/en
Publication of JPS56125213A publication Critical patent/JPS56125213A/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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • 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
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Carbon And Carbon Compounds (AREA)

Abstract

PURPOSE: Two absorption bands are set in the absorption column and the reaction mixture gas from the first reformer is led into the first absorption band to remove carbon dioxide, then the resultant gas is sent to the second reformer to effect the reaction and the absorption solution in the second absorption band is combined with the one in the first absorption band, thus increasing the carbon dioxide conversion.
CONSTITUTION: A carbon monoxide-containing mixture gas is sent through pipe 7 and heater 15 together with high-temperature steam fed from pipe 8 into the first reformer 1 where the shift reaction is effected in the reforming zone A filled with a catalyst to form carbon dioxide. The resultant mixture gas is sent through heater 15 and reboiler 5a into the lower absorption band in the absorption column 3 where carbon dioxide is absorbed and removed. The rest of the mixture gas is fed through pipe 22 and heater 16 along with steam from pipe 23 into the second reformer 2 where the sift reaction is effected in the reforming band B filled with a catalyst. The resultant gas is sent through heater 16 and reboiler 5b into the absorption band D in the upper part of the column 3 to remove carbon dioxide by absorption. At the same time, hydrogen gas is recovered by separation. The absorption solution is sent to regenerator 4 to separate carbon dioxide and pressurized into the top of the column 3.
COPYRIGHT: (C)1981,JPO&Japio
JP2656980A 1980-03-05 1980-03-05 Production and recovery of carbon dioxide from a carbon monoxide mixture Pending JPS56125213A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2656980A JPS56125213A (en) 1980-03-05 1980-03-05 Production and recovery of carbon dioxide from a carbon monoxide mixture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2656980A JPS56125213A (en) 1980-03-05 1980-03-05 Production and recovery of carbon dioxide from a carbon monoxide mixture

Publications (1)

Publication Number Publication Date
JPS56125213A true JPS56125213A (en) 1981-10-01

Family

ID=12197170

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2656980A Pending JPS56125213A (en) 1980-03-05 1980-03-05 Production and recovery of carbon dioxide from a carbon monoxide mixture

Country Status (1)

Country Link
JP (1) JPS56125213A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011517294A (en) * 2008-02-27 2011-06-02 ケロッグ ブラウン アンド ルート エルエルシー Shunt contactor
JP2011162385A (en) * 2010-02-09 2011-08-25 Hitachi Ltd Co2 recovery method and co2 recovery apparatus
JP2012162424A (en) * 2011-02-08 2012-08-30 Hitachi Ltd Co2 recovery method and co2 recovery apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011517294A (en) * 2008-02-27 2011-06-02 ケロッグ ブラウン アンド ルート エルエルシー Shunt contactor
JP2011162385A (en) * 2010-02-09 2011-08-25 Hitachi Ltd Co2 recovery method and co2 recovery apparatus
JP2012162424A (en) * 2011-02-08 2012-08-30 Hitachi Ltd Co2 recovery method and co2 recovery apparatus

Similar Documents

Publication Publication Date Title
US3904389A (en) Process for the production of high BTU methane-containing gas
EP0964829B1 (en) Removal of acidic gases in a gasification power system with production of hydrogen
US4409196A (en) Synthesis gas for ammonia production
EP0011404B1 (en) Integrated process for synthesis of methanol and of ammonia
KR880012483A (en) Dichlorosilane Production Process and Apparatus
DE3068921D1 (en) Process for producing ammonia and corresponding synthesis gas
JPH0253365B2 (en)
EP0317235A3 (en) Separation of gas mixtures including hydrogen
JPS55154303A (en) Method and apparatus for steam-reforming hydrocarbon
GB1467027A (en) Removal of impurities from gaseous mixtures and the regeneratio of absorbent solutions used therefor
JPS59205336A (en) Manufacture of oxygen addition organic compounds such as methanol
US3074783A (en) Production of sulfur-free hydrogen and carbon dioxide
US3420633A (en) Removal of impurities from hydrogen
CA1269819C (en) Plural absorption stages for hydrogen purification
GB1309872A (en) Process for producing methanol
GB2168718A (en) Producing synthesis gas
ES2050284T3 (en) PROCEDURE FOR OBTAINING SYNTHESIS GAS BY PARTIAL OXIDATION.
DK156638B (en) PROCEDURE FOR THE PREPARATION OF AN AMMONIA SYNTHESIC GAS
JPS56125213A (en) Production and recovery of carbon dioxide from a carbon monoxide mixture
ES433277A1 (en) Production of methane-rich gas stream
US3584998A (en) Process for making ammonia
JPS6126481B2 (en)
ES433280A1 (en) Production of methane
EP0111376A3 (en) Process for the preparation of methanol
EP0601886A1 (en) Manufacture of organic liquids