发明名称 PROCESS FOR CONVERTING HYDROCARBONS INTO OLEFINS
摘要 A process for converting hydrocarbon feedstock into olefins and BTX including feeding a hydrocarbon feedstock to a first hydrocracking unit, feeding effluent from the first hydrocracking unit to a first separation section to be separated, feeding a steam including propane to a dehydrogenation unit, and feeding effluent from the dehydrogenation unit to a second separation section.
申请公布号 US2016369186(A1) 申请公布日期 2016.12.22
申请号 US201415120949 申请日期 2014.12.23
申请人 SAUDI BASIC INDUSTRIES CORPORATION ;SAVIC GLOBAL TECHNOLOGIES B.V. 发明人 Dittrich Christoph;Van Willigenburg Joris;Pelaez Raúl Velasco;Schaerlaeckens Egidius Jacoba Maria;Rajagopalan Vijayanand;Ward Andrew Mark;Oprins Amo Johannes Maria;Narayanaswamy Ravichander
分类号 C10G69/00 主分类号 C10G69/00
代理机构 代理人
主权项 1. A process for converting a hydrocarbon feedstock into olefins and BTX, said converting process comprising the steps of: feeding a hydrocarbon feedstock to a first hydrocracking unit; feeding effluent from said first hydrocracking unit to a first separation section; separating said effluent in said first separation section into one or more streams from the group including a stream comprising hydrogen, a stream comprising methane, a stream comprising ethane, a stream comprising propane, a stream comprising butanes, a stream comprising C1-minus, a stream comprising C2-minus, a stream comprising C3-minus, a stream comprising C4-minus, a stream comprising C1-C2, a stream comprising C1-C3, a stream comprising C1-C4, a stream comprising C2-C3, a stream comprising C2-C4, a stream comprising C3-C4 and a stream comprising C5+; feeding said stream comprising propane to at least one dehydrogenation unit from the group including a combined propane/butanes dehydrogenation unit (PDH-BDH) and a propane dehydrogenation unit (PDH); feeding at least one stream from the group including said stream comprising C2-minus, said stream comprising ethane, and said stream comprising C1-C2 to a gas steam cracking unit and/or to a second separation unit; and feeding at least one of effluents from said dehydrogenation unit(s) and said gas steam cracking unit to said second separation section.
地址 Riyadh NL