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公开(公告)号:US08168838B2
公开(公告)日:2012-05-01
申请号:US12689709
申请日:2010-01-19
IPC分类号: C10M105/04 , C07C9/22
CPC分类号: C07C9/22 , C10G50/02 , C10G2300/1088 , C10G2300/301 , C10G2300/302 , C10M107/10 , C10M2205/0285 , C10N2220/022 , C10N2220/023 , C10N2220/028 , C10N2220/031 , C10N2230/06 , C10N2230/08 , C10N2230/10 , C10N2230/74 , C10N2240/10 , C10N2260/02
摘要: A process for the preparation of a synthetic predominantly single carbon number hydrocarbon fluid comprises the steps of: contacting an alpha olefin having a carbon number of 4 to 30 with a single site catalyst under conditions effective to produce reactive hydrocarbon oligomers that contain reactive double bonds and comprising predominantly dimers, trimers, and tetramers wherein at least 10 weight percent of such reactive hydrocarbon oligomers at least one of trimers and tetramers; separating at least one of said trimers and tetramers in said reactive hydrocarbon oligomers; dimerizing said separated one of said trimers tetramers by contacting said separated one of said trimers or tetramers with a dimerization catalyst thereby producing an unsaturated synthetic hydrocarbon fluid; and contacting said unsaturated synthetic hydrocarbon fluid with hydrogen in the presence of a hydrogenation catalyst thereby producing a synthetic hydrocarbon fluid having predominantly single carbon number.
摘要翻译: 用于制备主要为单一碳原子数合成烃合成流体的方法包括以下步骤:在有效产生含有反应性双键的活性烃低聚物的条件下,将碳数为4〜30的α-烯烃与单中心催化剂接触, 主要包含二聚体,三聚体和四聚体,其中至少10重量%的这种活性烃低聚物至少一种三聚体和四聚体; 在所述反应性烃低聚物中分离所述三聚体和四聚体中的至少一种; 通过使所述三聚体或四聚体中的所述分离的一个与二聚催化剂接触来使所述三聚体四聚体中的所述分离的一个二聚,由此产生不饱和的合成烃流体; 并在氢化催化剂存在下使所述不饱和合成烃流体与氢气接触,从而产生主要具有单一碳数的合成烃流体。