发明名称 PROCESS FOR THE PRODUCTION OF LIGHT OLEFINS AND AROMATICS FROM A HYDROCARBON FEEDSTOCK
摘要 The present invention relates to a process for increasing the production of a light olefin hydrocarbon compound from a hydrocarbon feedstock, comprising the following steps of: (a) feeding a hydrocarbon feedstock into a reaction area for ringopening (b) separating reaction products, which are generated from said reaction area, into an overhead stream and a side stream; (c) feeding the side stream from (b) to a gasoline hydrocracker (GHC) unit, (d) separating reaction products of said GHC of step (c) into an overhead stream, which contains hydrogen, methane, ethane, and liquefied petroleum gas, and a stream, which contains aromatic hydrocarbon compounds, and a small amount of hydrogen and non-aromatic hydrocarbon compounds, (e) feeding the overhead stream from the gasoline hydrocracker (GHC) unit into a steam cracker unit.
申请公布号 US2017009157(A1) 申请公布日期 2017.01.12
申请号 US201414902068 申请日期 2014.06.30
申请人 SAUDI BASIC INDUSTRIES CORPORATION ;SABIC GLOBAL TECHNOLOGIES B.V. 发明人 Oprins Arno Johannes Maria
分类号 C10G69/06;C10G69/00 主分类号 C10G69/06
代理机构 代理人
主权项 1. A process for increasing the production of a light olefin hydrocarbon compound from a hydrocarbon feedstock, comprising: (a) feeding a hydrocarbon feedstock into a reaction area for ring opening operating at a temperature range of 300-500° C. and a pressure range of 2-10 MPa, (b) separating reaction products, which are generated from said reaction area, into an overhead stream and a side stream; (c) feeding the side stream from (b) to a gasoline hydrocracker (GHC) unit operating at a temperature range of 300-580° C. and a pressure range of 0.3-5 MPa, wherein said gasoline hydrocracker (GHC) unit is operated at a temperature higher than said ring opening reaction area, and wherein said gasoline hydrocracker (GHC) unit is operated at a pressure lower than said ring opening reaction area, (d) separating reaction products of said GHC of step (c) into an overhead gas stream, comprising C2-C4 paraffins, hydrogen and methane and a stream comprising aromatic hydrocarbon compounds and non-aromatic hydrocarbon compounds, and (e) feeding the overhead gas stream from the gasoline hydrocracker (GHC) unit into a steam cracker unit.
地址 Riyadh SA