RU2000107366A - METHOD FOR PRODUCING ACETYLENE AND SYNTHESIS-GAS. - Google Patents

METHOD FOR PRODUCING ACETYLENE AND SYNTHESIS-GAS.

Info

Publication number
RU2000107366A
RU2000107366A RU2000107366/04A RU2000107366A RU2000107366A RU 2000107366 A RU2000107366 A RU 2000107366A RU 2000107366/04 A RU2000107366/04 A RU 2000107366/04A RU 2000107366 A RU2000107366 A RU 2000107366A RU 2000107366 A RU2000107366 A RU 2000107366A
Authority
RU
Russia
Prior art keywords
reactor
reaction
initial mixture
oxygen
mixture
Prior art date
Application number
RU2000107366/04A
Other languages
Russian (ru)
Other versions
RU2242497C2 (en
Inventor
ШТАПФ Дитер
ПРЕСЛЕР Петер
Бахтлер Михаэль
ШАЙДШТЕГЕР Олаф
БАРТЕНБАХ Бернд
Original Assignee
Басф Акциенгезелльшафт
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 DE19914226A external-priority patent/DE19914226A1/en
Application filed by Басф Акциенгезелльшафт filed Critical Басф Акциенгезелльшафт
Publication of RU2000107366A publication Critical patent/RU2000107366A/en
Application granted granted Critical
Publication of RU2242497C2 publication Critical patent/RU2242497C2/en

Links

Claims (10)

1. Способ получения ацетилена и синтез-газа путем термической обработки исходной смеси, которая содержит один или несколько углеводородов и молекулярный кислород и/или соединения с одним или несколькими элементами кислорода, причем исходную смесь нагревают, в реакторе приводят реакцию, и затем охлаждают, отличающийся тем, что исходную смесь нагревают максимум до 1400oС.1. A method of producing acetylene and synthesis gas by heat treatment of an initial mixture that contains one or more hydrocarbons and molecular oxygen and / or compounds with one or more oxygen elements, the initial mixture being heated, a reaction is carried out in the reactor, and then cooled, characterized the fact that the initial mixture is heated to a maximum of 1400 o C. 2. Способ по п.1, отличающийся тем, что используют косвенное охлаждение. 2. The method according to claim 1, characterized in that indirect cooling is used. 3. Способ по п.1, отличающийся тем, что комбинируют косвенное охлаждение и непосредственное гашение реакции. 3. The method according to claim 1, characterized in that indirect cooling and direct quenching of the reaction are combined. 4. Способ по п. 1, отличающийся тем, что используют непосредственное охлаждение агентом, гасящим реакцию, при температуре максимум 1000oС.4. The method according to p. 1, characterized in that they use direct cooling with an agent quenching the reaction at a temperature of a maximum of 1000 o C. 5. Способ по одному из пп.1-4, отличающийся тем, что исходную смесь нагревают исключительно посредством реакционного тепла, которое выделяется в реакторе. 5. The method according to one of claims 1 to 4, characterized in that the initial mixture is heated exclusively by reaction heat, which is released in the reactor. 6. Способ по одному из пп.1-5, отличающийся тем, что реакцию проводят при любом давлении, предпочтительно при атмосферном давлении. 6. The method according to one of claims 1 to 5, characterized in that the reaction is carried out at any pressure, preferably at atmospheric pressure. 7. Способ по одному из пп.1-6, отличающийся тем, что реактором являются реактор с подачей пламени, регенерирующий реактор, рекуперативный реактор или проточный реактор, предпочтительно трубчатый реактор. 7. The method according to one of claims 1 to 6, characterized in that the reactor is a flame feed reactor, a regenerating reactor, a recuperative reactor or a flow reactor, preferably a tubular reactor. 8. Способ по одному из пп.1-7, отличающийся тем, что частичное количество охлажденной реакционной смеси подвергают рециклизации. 8. The method according to one of claims 1 to 7, characterized in that a partial amount of the cooled reaction mixture is recycled. 9. Способ по одному из пп.1-8, отличающийся тем, что молекулярный кислород представлен исходной смесью в виде воздуха или смеси воздуха и кислорода. 9. The method according to one of claims 1 to 8, characterized in that the molecular oxygen is represented by the initial mixture in the form of air or a mixture of air and oxygen. 10. Способ по одному из пп.1-9, отличающийся тем, что соединениями, содержащими элемент кислорода, являются водный пар и/или диоксид углерода. 10. The method according to one of claims 1 to 9, characterized in that the compounds containing the oxygen element are water vapor and / or carbon dioxide.
RU2000107366/04A 1999-03-29 2000-03-28 Acetylene and synthesis gas production process RU2242497C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19914226A DE19914226A1 (en) 1999-03-29 1999-03-29 Process for the production of acetylene and synthesis gas
DE19914226.2 1999-03-29

Publications (2)

Publication Number Publication Date
RU2000107366A true RU2000107366A (en) 2001-11-27
RU2242497C2 RU2242497C2 (en) 2004-12-20

Family

ID=7902826

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2000107366/04A RU2242497C2 (en) 1999-03-29 2000-03-28 Acetylene and synthesis gas production process

Country Status (6)

Country Link
US (1) US6365792B1 (en)
EP (1) EP1041037B1 (en)
JP (1) JP2001010984A (en)
CN (1) CN1188376C (en)
DE (2) DE19914226A1 (en)
RU (1) RU2242497C2 (en)

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