RU2001107419A - A method of obtaining a flowing coolant used as an indirect source of heat during endothermic reactions - Google Patents

A method of obtaining a flowing coolant used as an indirect source of heat during endothermic reactions

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Publication number
RU2001107419A
RU2001107419A RU2001107419/12A RU2001107419A RU2001107419A RU 2001107419 A RU2001107419 A RU 2001107419A RU 2001107419/12 A RU2001107419/12 A RU 2001107419/12A RU 2001107419 A RU2001107419 A RU 2001107419A RU 2001107419 A RU2001107419 A RU 2001107419A
Authority
RU
Russia
Prior art keywords
water
stream
stream containing
combustion chamber
water vapor
Prior art date
Application number
RU2001107419/12A
Other languages
Russian (ru)
Other versions
RU2283272C2 (en
Inventor
Эрманно Филиппи
Original Assignee
Аммониа Казале С.А.
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 EP00106237A external-priority patent/EP1136444B1/en
Application filed by Аммониа Казале С.А. filed Critical Аммониа Казале С.А.
Publication of RU2001107419A publication Critical patent/RU2001107419A/en
Application granted granted Critical
Publication of RU2283272C2 publication Critical patent/RU2283272C2/en

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Claims (10)

1. Способ получения текучего теплоносителя, используемого в качестве косвенного источника тепла для проведения эндотермических реакций, заключающийся в том, что поток, содержащий углеводороды, и поток газа, содержащего кислород, подают в камеру сгорания, в которой эти потоки соответствующим образом сжимают, и углеводороды сжигают в присутствии кислорода в камере сгорания с получением имеющей высокую температуру текучей среды, содержащей диоксид углерода и кислород, отличающийся тем, что в имеющую высокую температуру текучую среду и/или в камеру сгорания подают поток, содержащий воду, предпочтительно в виде водяного пара.1. A method of obtaining a fluid coolant used as an indirect source of heat for carrying out endothermic reactions, which consists in the fact that the stream containing hydrocarbons and the gas stream containing oxygen are fed into the combustion chamber, in which these streams are suitably compressed, and hydrocarbons burned in the presence of oxygen in the combustion chamber to obtain a high temperature fluid containing carbon dioxide and oxygen, characterized in that in a high temperature fluid and / or a stream containing water is fed into the combustion chamber, preferably in the form of water vapor. 2. Способ по п.1, отличающийся тем, что количество подаваемой воды составляет от 0,1 до 0,7 от количества газа, содержащего кислород.2. The method according to claim 1, characterized in that the amount of water supplied is from 0.1 to 0.7 of the amount of gas containing oxygen. 3. Способ по п.1, отличающийся тем, что поток, содержащий воду, подают в имеющую высокую температуру текучую среду и/или в камеру сгорания в виде водяного пара, полученного при испарении потока воды, при заданном давлении.3. The method according to claim 1, characterized in that the stream containing water is fed into a high-temperature fluid and / or into the combustion chamber in the form of water vapor obtained by evaporation of a water stream at a given pressure. 4. Способ по п.1, отличающийся тем, что поток, содержащий воду, подают в камеру сгорания в виде водяного пара вместе с потоком газа, содержащего кислород.4. The method according to claim 1, characterized in that the stream containing water is supplied to the combustion chamber in the form of water vapor together with a stream of gas containing oxygen. 5. Способ по п.4, отличающийся тем, что поток, содержащий воду, вводят при заданном давлении в поток газа, содержащего кислород, до камеры сгорания и полученный поток нагревают таким образом, что при этом происходит по крайней мере частичное испарение воды с получением потока, содержащего кислород и водяной пар.5. The method according to claim 4, characterized in that the stream containing water is introduced at a given pressure into the stream of gas containing oxygen to the combustion chamber and the resulting stream is heated in such a way that at least partial evaporation of water takes place to obtain a stream containing oxygen and water vapor. 6. Способ по п.4, отличающийся тем, что нагревают поток, содержащий воду и нагретый поток, содержащий воду, вводят при заданном давлении в поток газа, содержащего кислород, до камеры сгорания таким образом, что при этом происходит по крайней мере частичное испарение воды с получением потока, содержащего кислород и водяной пар.6. The method according to claim 4, characterized in that the stream containing water is heated and the heated stream containing water is introduced at a given pressure into the stream of gas containing oxygen to the combustion chamber in such a way that at least partial evaporation occurs water to obtain a stream containing oxygen and water vapor. 7. Способ проведения реакций реформинга углеводородов в выполненной в виде теплообменника реформинг-установке, состоящий в том, что поток газа, содержащего углеводороды и водяной пар, подают в заполненное катализатором реакционное пространство (25) выполненной в виде теплообменника реформинг-установки, в пространство (26), расположенное в выполненной в виде теплообменника реформинг-установки рядом с реакционным пространством (25), подают текучий теплоноситель и компоненты потока газа, содержащего углеводороды, подвергают каталитическому взаимодействию в процессе косвенного теплообмена с текучим теплоносителем с получением потока газа, содержащего водород, отличающийся тем, что текучий теплоноситель содержит воду, предпочтительно в виде водяного пара.7. A method for carrying out hydrocarbon reforming reactions in a reforming unit made in the form of a heat exchanger, consisting in the fact that a stream of gas containing hydrocarbons and water vapor is fed into the reaction space (25), made in the form of a heat exchanger, of a reforming unit, into the space ( 26) located in a reforming unit made in the form of a heat exchanger near the reaction space (25), a fluid coolant is supplied and the components of the gas stream containing hydrocarbons are subjected to catalytic interacting ones in indirect heat exchange with a heating fluid to obtain a gas stream containing hydrogen, wherein said heating fluid comprises water, preferably in the form of water vapor. 8. Способ по п.7, отличающийся тем, что текучий теплоноситель получают способом по любому из пп.1-6.8. The method according to claim 7, characterized in that the fluid coolant is obtained by the method according to any one of claims 1 to 6. 9. Способ по п.8, отличающийся тем, что текучий теплоноситель, выходящий из выполненной в виде теплообменника реформинг-установке, охлаждают путем косвенного теплообмена с содержащим кислород и/или воду потоком, который подают в камеру сгорания.9. The method according to claim 8, characterized in that the fluid coolant leaving the reforming unit made in the form of a heat exchanger is cooled by indirect heat exchange with a stream containing oxygen and / or water, which is supplied to the combustion chamber. 10. Применение воды, предпочтительно в виде водяного пара, в способе получения текучего теплоносителя, используемого в качестве косвенного источника тепла для проведения эндотермических реакций, таких как реакции реформинга углеводородов.10. The use of water, preferably in the form of water vapor, in a method for producing a flowing coolant used as an indirect heat source for carrying out endothermic reactions, such as hydrocarbon reforming reactions.
RU2001107419/12A 2000-03-22 2001-03-21 Method of production of the liquid heat carrier used as the indirect source of heat at realization of the endothermal reactions and the method of realization of the reactions of reforming of the hydrocarbons RU2283272C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP00106237A EP1136444B1 (en) 2000-03-22 2000-03-22 Process for hydrocarbon reforming
EP00106237.1 2000-03-22

Publications (2)

Publication Number Publication Date
RU2001107419A true RU2001107419A (en) 2003-05-27
RU2283272C2 RU2283272C2 (en) 2006-09-10

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RU2001107419/12A RU2283272C2 (en) 2000-03-22 2001-03-21 Method of production of the liquid heat carrier used as the indirect source of heat at realization of the endothermal reactions and the method of realization of the reactions of reforming of the hydrocarbons

Country Status (17)

Country Link
US (1) US7465324B2 (en)
EP (1) EP1136444B1 (en)
KR (1) KR100824082B1 (en)
CN (1) CN1220622C (en)
AR (1) AR027700A1 (en)
AT (1) ATE556987T1 (en)
AU (1) AU779544B2 (en)
BR (1) BR0101071A (en)
CA (1) CA2341124C (en)
EG (1) EG22750A (en)
GC (1) GC0000275A (en)
ID (1) ID29700A (en)
MX (1) MXPA01002887A (en)
MY (1) MY148606A (en)
NZ (1) NZ510414A (en)
RU (1) RU2283272C2 (en)
UA (1) UA78671C2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080016768A1 (en) 2006-07-18 2008-01-24 Togna Keith A Chemically-modified mixed fuels, methods of production and used thereof
FR2909445B1 (en) * 2006-12-05 2009-02-06 Air Liquide METHOD FOR CONTROLLING A REFORMING REACTION BY MEASURING THE TEMPERATURE OF THE REFORMING TUBES
CN102137817B (en) * 2008-06-26 2015-02-18 赫多特普索化工设备公司 Process for the production of ammonia
EP2147896A1 (en) * 2008-07-22 2010-01-27 Uhde GmbH Low energy process for the production of ammonia or methanol
CN102556965B (en) * 2012-01-13 2013-07-17 清华大学 Method for cooling high temperature parts through catalytic reforming of liquid hydrocarbon fuel
US10730749B2 (en) * 2018-11-07 2020-08-04 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Process for integrating a partial oxidation plant with an oxy-combustion plant utilizing a steam turbine
KR20220145650A (en) * 2021-04-22 2022-10-31 현대자동차주식회사 Combustion control device of lpg reforming system and control method thereof

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3717129A (en) * 1970-09-28 1973-02-20 Phillips Petroleum Co Method and apparatus for reducing engine exhaust pollutants
US4047935A (en) * 1974-12-11 1977-09-13 United States Steel Corporation Process for direct-reduction of iron-ore employing nuclear reactor-powdered catalytic reformer
US4003343A (en) * 1975-04-04 1977-01-18 Phillips Petroleum Company Method and apparatus for maintaining the operating temperature in a device for reducing engine exhaust pollutants
US4337170A (en) * 1980-01-23 1982-06-29 Union Carbide Corporation Catalytic steam reforming of hydrocarbons
US4488866A (en) * 1982-08-03 1984-12-18 Phillips Petroleum Company Method and apparatus for burning high nitrogen-high sulfur fuels
US4479925A (en) * 1982-09-13 1984-10-30 The M. W. Kellogg Company Preparation of ammonia synthesis gas
GB8521608D0 (en) * 1985-08-30 1985-10-02 Shell Int Research Producing synthesis gas
US5011625A (en) * 1989-12-11 1991-04-30 The M. W. Kellogg Company Autothermal steam reforming process
US5122299A (en) * 1989-12-11 1992-06-16 The M. W. Kellogg Company Autothermal steam reforming process
ZA911838B (en) * 1990-04-03 1991-12-24 Standard Oil Co Ohio Endothermic reaction apparatus
DE4327176C1 (en) * 1993-08-13 1995-01-26 Metallgesellschaft Ag Tube furnace for the production of gas mixtures containing carbon monoxide
DE4340688C2 (en) * 1993-11-30 1997-05-07 Uhde Gmbh Process for adjusting the carbon activity in a synthesis gas production process
US6170264B1 (en) * 1997-09-22 2001-01-09 Clean Energy Systems, Inc. Hydrocarbon combustion power generation system with CO2 sequestration
DE19613905A1 (en) * 1996-04-06 1997-10-09 Metallgesellschaft Ag Metal surface protected against metal dusting corrosion that has a thermal insulation layer
AU5633499A (en) * 1998-08-19 2000-03-14 Methanex Corporation Method for performing a process wherein a feedstock is subjected to an endothermic reaction
FR2807746B1 (en) * 2000-04-13 2002-12-13 Air Liquide METHOD FOR PRODUCING A MIXTURE COMPRISING HYDROGEN AND CO
US6871502B2 (en) * 2002-02-15 2005-03-29 America Air Liquide, Inc. Optimized power generation system comprising an oxygen-fired combustor integrated with an air separation unit

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