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公开(公告)号：US3718607A
公开(公告)日：1973-02-27
申请号：US3718607D
申请日：1971-07-19
Applicant: DOW CHEMICAL CO
Inventor： MARTIN G
IPC: B01J27/043 , B01J37/20 , C07C5/32 , C07C5/333 , B01J11/74
CPC classification number: C07C5/3332 , B01J27/043 , B01J37/20 , C07C5/322 , Y02P20/52 , Y10S585/906 , C07C11/02 , C07C11/06
Abstract: A process for dehydrogenating an alkane to form an olefin by passing it over a catalyst comprising nickel or cobalt sulfide and cerium oxide alone or in combination with barium oxide, preferably on an alumina support, at a temperature of from about 550* to 625* C. and recovering the olefin.
Abstract translation: 一种使烷烃脱氢以形成烯烃的方法，该方法通过将催化剂在约550℃至625℃的温度下通过包含镍或硫化钴和氧化铈的催化剂或与氧化钡，优选氧化铝载体组合， 并回收烯烃。
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公开(公告)号：US3793392A
公开(公告)日：1974-02-19
申请号：US3793392D
申请日：1972-10-02
Applicant: DOW CHEMICAL CO
Inventor： MARTIN G
IPC: B01J27/043 , B01J37/20 , C07C5/333 , C07C5/18
CPC classification number: B01J37/20 , B01J27/043 , C07C5/3332 , C07C11/02
Abstract: A PROCESS FOR DEHYDROGENATING AN ALKANE TO FORM AN OLEFIN BY PASSING IT OVER A CATALYST COMPRISING NICKEL OR COBALT SULFIDE AND CERIUM OXIDE ALONE OR IN COMBINATION WITH BARIUM OXIDE, PREFERABLY ON AN ALUMINA SUPPORT, AT A TEMPERATURE OF FROM ABOUT 550* TO 625* C. AND RECOVERING THE OLEFIN.
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公开(公告)号：US3773656A
公开(公告)日：1973-11-20
申请号：US3773656D
申请日：1971-12-01
Applicant: DOW CHEMICAL CO
Abstract: Heavy hydrocarbon feed oils such as heavy gas oils, residium, topped crude oils and the like are hydrocracked by mixing hydrogen with the feed oil in the ratio of hydrogen to feed oil in the range from 4000 to 10,000 SCF of hydrogen per barrel of feed oil and contacting this mixture under hydro-treating conditions with a supported micro-spherical catalyst having 5-20 weight per cent tungsten and 0.5 to 5.0 weight per cent rhenium. Increased isoparaffin and aromatic content in the cracked product is obtained.
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