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RU93049104A - REACTOR FOR GAS RICH IN HYDROGEN AND / OR CARBON OXIDE - Google Patents

REACTOR FOR GAS RICH IN HYDROGEN AND / OR CARBON OXIDE

Info

Publication number
RU93049104A
RU93049104A RU93049104/26A RU93049104A RU93049104A RU 93049104 A RU93049104 A RU 93049104A RU 93049104/26 A RU93049104/26 A RU 93049104/26A RU 93049104 A RU93049104 A RU 93049104A RU 93049104 A RU93049104 A RU 93049104A
Authority
RU
Russia
Prior art keywords
reactor
hydrogen
gas rich
carbon oxide
refractory lining
Prior art date
Application number
RU93049104/26A
Other languages
Russian (ru)
Other versions
RU2109560C1 (en
Inventor
Иварсон Примдаль Ивар
Original Assignee
Хальдор Топсеэ А/С
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 claimed from DK101392A external-priority patent/DK169614B1/en
Application filed by Хальдор Топсеэ А/С filed Critical Хальдор Топсеэ А/С
Publication of RU93049104A publication Critical patent/RU93049104A/en
Application granted granted Critical
Publication of RU2109560C1 publication Critical patent/RU2109560C1/en

Links

Claims (1)

Предлагается реактор для получения газа, богатого водородом и/или окисью углерода, включающий работающий под давлением кожух, снабженный устройством для подачи исходного углеводородного сырья и содержащий кислород среды, огнеупорной футеровкой, расположенной на внутренней стенке кожуха, и устройством для вывода продукта; реактор согласно изобретению отличается тем, что огнеупорная футеровка снабжена по крайней мере в верхней части реактора слоем катализатора риформинга в количестве 0,01 - 0,15 г/м2. Реактор по изобретению может содержать в нижней части слой катализатора.A reactor for producing a gas rich in hydrogen and / or carbon monoxide is proposed, including a pressurized casing, equipped with a device for supplying a hydrocarbon feed and containing oxygen, refractory lining located on the inner wall of the casing, and a device for outputting the product; The reactor according to the invention is characterized in that the refractory lining is provided at least in the upper part of the reactor with a layer of reforming catalyst in an amount of 0.01 - 0.15 g / m 2 . The reactor of the invention may comprise a catalyst bed at the bottom.
RU93049104A 1992-08-13 1993-08-12 Reactor for preparing gas enriched with hydrogen and/or carbon monoxide RU2109560C1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DK101392A DK169614B1 (en) 1992-08-13 1992-08-13 Process and reactor for producing hydrogen and carbon monoxide rich gases
DK1013/92 1992-08-13

Publications (2)

Publication Number Publication Date
RU93049104A true RU93049104A (en) 1997-01-27
RU2109560C1 RU2109560C1 (en) 1998-04-27

Family

ID=8100018

Family Applications (1)

Application Number Title Priority Date Filing Date
RU93049104A RU2109560C1 (en) 1992-08-13 1993-08-12 Reactor for preparing gas enriched with hydrogen and/or carbon monoxide

Country Status (7)

Country Link
US (1) US5958297A (en)
EP (1) EP0583211B1 (en)
JP (1) JP2716650B2 (en)
CA (1) CA2103939C (en)
DE (1) DE69300627T2 (en)
DK (1) DK169614B1 (en)
RU (1) RU2109560C1 (en)

Families Citing this family (19)

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Publication number Priority date Publication date Assignee Title
FR2726821B1 (en) * 1994-11-16 1997-01-03 Patillet Henri PROCESS AND APPARATUS FOR THE PRODUCTION OF METHANOL BY GASIFICATION OF CARBONACEOUS MATERIALS
MY128194A (en) * 1997-04-11 2007-01-31 Chiyoda Corp Process for the production of synthesis gas
DE69825884D1 (en) * 1997-04-11 2004-09-30 Chiyoda Chem Eng Construct Co METHOD FOR PRODUCING SYNTHESIS GAS BY means of OUTOTHERM REFORMING
EP0931762B1 (en) * 1998-01-21 2005-05-04 Haldor Topsoe A/S Process for the preparation of hydrogen-rich gas
JP2002521295A (en) * 1998-07-21 2002-07-16 ハルダー トプソー エイエス Method for producing synthesis gas by steam reforming
FR2789691B1 (en) 1999-02-11 2001-04-27 Inst Francais Du Petrole METHOD FOR SYNTHESIS OF ATMOSPHERIC DISTILLATE INCLUDING THE USE OF FISCHER-TROPSCH TECHNOLOGY
TWI241392B (en) * 1999-09-20 2005-10-11 Japan Science & Tech Agency Apparatus and method for gasifying solid or liquid fuel
EP1116689A1 (en) * 2000-01-11 2001-07-18 Haldor Topsoe A/S Process and reactor for the preparation of hydrogen and carbon monoxide rich gas
US20030228267A1 (en) * 2001-07-09 2003-12-11 Aust Duncan T. Suncreen composition wit enhanced spf and water resistant properties
JP5100950B2 (en) 2000-07-10 2012-12-19 ヴァーサ パワー システムズ リミテッド Integrated module for solid oxide fuel cell system
US6387843B1 (en) 2001-04-05 2002-05-14 Chiyoda Corporation Method of preparing Rh- and/or Ru-catalyst supported on MgO carrier and reforming process using the catalyst
US6656978B2 (en) * 2001-04-05 2003-12-02 Chiyoda Corporation Process of producing liquid hydrocarbon oil or dimethyl ether from lower hydrocarbon gas containing carbon dioxide
EP1403217A1 (en) 2002-09-26 2004-03-31 Haldor Topsoe A/S Process and apparatus for the preparation of synthesis gas
EP1403215B1 (en) 2002-09-26 2013-03-13 Haldor Topsoe A/S Process and apparatus for the preparation of synthesis gas
ES2381105T3 (en) 2003-02-05 2012-05-23 Haldor Topsoe A/S Procedure for the treatment of synthesis gas
CA2587289C (en) * 2004-11-18 2010-07-06 Praxair Technology, Inc. Steam methane reforming method
US7037485B1 (en) * 2004-11-18 2006-05-02 Praxair Technology, Inc. Steam methane reforming method
US20070013144A1 (en) * 2005-07-13 2007-01-18 Seungdoo Park Reactor sealing methods
DE102014004264A1 (en) * 2014-03-14 2015-09-17 Universität Stuttgart Heat-integrated high-temperature reactors for autothermal partial oxidation

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2655442A (en) * 1948-08-23 1953-10-13 Phillips Petroleum Co Process and apparatus for the manufacture of synthesis gas
US2943062A (en) * 1956-01-19 1960-06-28 Kellogg M W Co Conversion of hydrocarbons to a hydrogen-rich gas
US3071454A (en) * 1960-08-04 1963-01-01 Phelps Dodge Corp Apparatus for reforming gases
CA944563A (en) * 1971-12-02 1974-04-02 Robert W. Pfeiffer Process and apparatus for reforming hydrocarbon oils
US3920579A (en) * 1974-04-24 1975-11-18 Texaco Inc Synthesis gas production by partial oxidation
US4456703A (en) * 1982-05-07 1984-06-26 Exxon Research And Engineering Co. High surface area nickel aluminate spinel catalyst for steam reforming
US4863707A (en) * 1982-09-30 1989-09-05 Engelhard Corporation Method of ammonia production
DK163294C (en) * 1982-09-30 1992-07-13 Engelhard Corp PROCEDURE FOR PREPARING A HYDROGEN-RICH GAS BY AUTOTERMAL REFORM
GB8309359D0 (en) * 1983-04-06 1983-05-11 Ici Plc Synthesis gas
EP0194067B2 (en) * 1985-03-05 1994-05-11 Imperial Chemical Industries Plc Steam reforming hydrocarbons
ES2019383B3 (en) * 1986-05-27 1991-06-16 Ici Plc METHOD TO INITIATE A PROCESS FOR THE PRODUCTION OF A GASEOUS CURRENT CONTAINING HYDROGEN AND CARBON OXIDES.
FR2608581B1 (en) * 1986-12-18 1989-04-28 Inst Francais Du Petrole FLAME-OPERATING METHOD AND DEVICE FOR THE MANUFACTURE OF SYNTHESIS GAS
JPH01261201A (en) * 1988-04-12 1989-10-18 Mitsubishi Gas Chem Co Inc Hydrocarbon reforming reactor

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