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公开(公告)号:US10774017B2
公开(公告)日:2020-09-15
申请号:US16364737
申请日:2019-03-26
Applicant: PHILLIPS 66 COMPANY
Inventor: Anthony O. Baldridge , Neal D. McDaniel , James A. Suttil , Soumen Kundu , Jianhua Yao , Bruce B. Randolph , Maziar Sardashti , Steven E. Lusk , Robert M. Walston, Jr.
IPC: C07C5/333 , C10L1/04 , C07C5/32 , C07C2/76 , C10G59/06 , C07C6/10 , C07C6/12 , C07C4/06 , C07C4/10 , C07C4/02 , C07C2/74 , C07C2/54 , C07C2/56 , C07C2/58 , C07C2/42 , C07C9/16 , C07C9/18 , C07C9/14 , C07C9/15
Abstract: The present disclosure relates generally to processes and systems for producing liquid transportation fuels by converting a feed stream that comprises both isopentane and n-pentane, and optionally, some C6+ hydrocarbons. Isopentane and smaller hydrocarbons are separated to form a first fraction while n-pentane and larger components of the feed stock form a second fraction. Each fraction is then catalytically-activated in a separate reaction zone with a separate catalyst, where the conditions maintained in each zone maximize the conversion of each fraction to olefins and aromatics, while minimizing the production of C1-C4 light paraffins. In certain embodiments, the first fraction is activated at a lower temperature than the second fraction. The process provides increased yields of upgraded hydrocarbon products that possess the characteristics of a liquid transportation fuel or a blend component thereof.
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公开(公告)号:US10745328B2
公开(公告)日:2020-08-18
申请号:US16364764
申请日:2019-03-26
Applicant: PHILLIPS 66 COMPANY
Inventor: Anthony O. Baldridge , Neal D. McDaniel , James A. Suttil , Soumen Kundu , Jianhua Yao , Bruce B. Randolph , Maziar Sardashti , Steven E. Lusk , Robert M. Walston, Jr.
IPC: C07C5/333 , C10L1/04 , C07C5/32 , C07C2/42 , C10G59/06 , C07C9/14 , C07C6/08 , C07C4/10 , C07C9/16 , C07C9/18 , C07C9/15 , C07C5/327 , C07C6/12 , C07C4/02 , C07C4/06 , C07C6/10 , C07C2/56 , C07C2/58 , C07C2/54 , C07C2/74 , C07C2/08 , C07C2/02 , C07C2/04 , C07C2/06
Abstract: The present disclosure relates generally to processes and systems for producing liquid transportation fuels by converting a feed stream that comprises both isopentane and n-pentane, and optionally, some C6+ hydrocarbons. Isopentane and smaller hydrocarbons are separated to form a first fraction while n-pentane and larger components of the feed stock form a second fraction. Each fraction is then catalytically-activated in a separate reaction zone with a separate catalyst, where the conditions maintained in each zone maximize the conversion of each fraction to olefins and aromatics, while minimizing the production of C1-C4 light paraffins. In certain embodiments, the first fraction is activated at a lower temperature than the second fraction. Certain embodiments additionally comprise mixing at least a portion of the two effluents and contacting with an oligomerization catalyst to provide enhanced yields of aliphatic hydrocarbons that possess the characteristics of a blend component of a liquid transportation fuel or other value-added chemical products.
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