专利摘要:
The invention relates to a process of converting ethylbenzene to styrene by catalytic dehydrogenation at temperatures of about 600 DEG C. in the presence of water vapor in a tubular reactor. The heat required for the dehydrogenation is fed to the tubular reactor with a molten salt bath. The dehydrogenation is effected isothermally and in a single stage under atmospheric pressure or preferable under a subatmospheric pressure with a water vapor-ethylbenzene ratio of 1.2 to 1.5 kg of water vapor per kg of ethylbenzene. The temperature of the ethylbenzene-water-vapor mixture entering the tubular reactor is maintained 50 DEG to 100 DEG C. below the temperature of the molten salt bath.
公开号:SU1036245A3
申请号:SU802893553
申请日:1980-03-05
公开日:1983-08-15
发明作者:Меллер Фридрих-Вильхельм;Бухольд Хеннинг;Кляйн Хельмут;Гаркиш Отто-Людвиг;Гютльхубер Фридрих;Лабер Вальтер
申请人:Металлгезельшафт Аг (Фирма);
IPC主号:
专利说明:

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权利要求:
Claims (2)
[1]
1 "METHOD FOR PRODUCING STYROL by isothermal catalytic dehydrogenation of ethylbenzene at a temperature of about 600 ° C and atmospheric or reduced pressure in the presence of water vapor at a weight ratio of water vapor: ethylbenzene
1.2-1.5: 1 in a tubular reactor, characterized in that, in order to increase the yield of the target product and the selectivity of the process, heating the tubular reactor is carried out with a molten salt consisting of a mixture of sodium, potassium and lithium carbonates, and the process is carried out when the temperature difference of the molten salt and the introduced mixture of ethylbenzene with water vapor 50-100 ° C.
[2]
2. The method according to π. 1, they are distinguished by the fact that the process is carried out at a temperature difference between the salt melt and dehydrogenation less than 20 ° С.
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同族专利:
公开号 | 公开日
US4287375A|1981-09-01|
IT1174666B|1987-07-01|
DE2909763A1|1980-09-18|
GB2044287A|1980-10-15|
NL8001290A|1980-09-16|
FR2451355B1|1985-02-01|
IT8020430D0|1980-03-07|
JPS55124723A|1980-09-26|
FR2451355A1|1980-10-10|
DE2909763C2|1982-09-09|
GB2044287B|1983-01-06|
引用文献:
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US2374826A|1942-03-26|1945-05-01|Universal Oil Prod Co|Conversion process|
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US5739071A|1993-07-07|1998-04-14|Raytheon Engineers & Constructors, Inc.|Method and apparatus for regeneratinig and stabilizing dehydrogenation catalysts|
EP0841317B1|1996-11-08|2002-01-09|Fina Technology, Inc.|Process for dehydrogenation of ethylbenzene to styrene|
US6781024B2|2000-11-22|2004-08-24|Fina Technology, Inc.|Dehydrogenation process|
US6380449B1|2000-11-22|2002-04-30|Fina Technology, Inc.|Dehydrogenation process|
US20050085677A1|2003-10-15|2005-04-21|Fina Technology, Inc.|Method for improved production of cyclohexenyl and alkenyl aromatic compounds|
US7169960B2|2004-12-22|2007-01-30|Fina Technology, Inc.|Dehydrogenation process|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
DE2909763A|DE2909763C2|1979-03-13|1979-03-13|Process for the catalytic, one-step, isothermal dehydrogenation of ethylbenzene to styrene|
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