公开(公告)号：US20230365878A1

公开(公告)日：2023-11-16

申请号：US18314613

申请日：2023-05-09

Applicant: PHILLIPS 66 COMPANY

Inventor： Chengtian Wu ,  Jonathan Marda ,  Karthikeyan Marimuthu ,  Dhananjay Ghonasgi ,  Jianhua Yao

IPC: C10G67/16 ,  C10G50/00 ,  C10G35/06

CPC classification number: C10G67/16 ,  C10G50/00 ,  C10G35/065 ,  C10G2400/02 ,  C10G2300/30 ,  C10G2300/1081

Abstract: Methods that increase production of a liquid transportation fuel blend component by utilizing C5 hydrocarbon streams taken from both a refinery naphtha stream and an NGL fractionator pentanes plus stream. A high vapor pressure pentane fraction from the NGL fractionator is separated to remove isopentane and produce lower vapor pressure commodity natural gasoline. A refinery naphtha stream (that is optionally an FCC naphtha stream) is separated to produce a C5 olefins stream that is then oligomerized to produce an upgraded stream having lower vapor pressure and higher octane rating, then combined with the remainder of the naphtha stream as well as the isopentane stream to produce a gasoline blend component that meets specifications for vapor pressure and octane rating.

公开(公告)号：US12264287B2

公开(公告)日：2025-04-01

申请号：US18314613

申请日：2023-05-09

Applicant: PHILLIPS 66 COMPANY

Inventor： Chengtian Wu ,  Jonathan Marda ,  Karthikeyan Marimuthu ,  Dhananjay Ghonasgi ,  Jianhua Yao

IPC: C10G67/16 ,  C10G35/06 ,  C10G50/00

Abstract: Methods that increase production of a liquid transportation fuel blend component by utilizing C5 hydrocarbon streams taken from both a refinery naphtha stream and an NGL fractionator pentanes plus stream. A high vapor pressure pentane fraction from the NGL fractionator is separated to remove isopentane and produce lower vapor pressure commodity natural gasoline. A refinery naphtha stream (that is optionally an FCC naphtha stream) is separated to produce a C5 olefins stream that is then oligomerized to produce an upgraded stream having lower vapor pressure and higher octane rating, then combined with the remainder of the naphtha stream as well as the isopentane stream to produce a gasoline blend component that meets specifications for vapor pressure and octane rating.

公开(公告)号：US20210220788A1

公开(公告)日：2021-07-22

申请号：US17153390

申请日：2021-01-20

Applicant: PHILLIPS 66 COMPANY

Inventor： Jianhua Yao ,  Anthony O. Baldridge ,  Neal D. McDaniel ,  James A. Suttil ,  Chengtian Wu ,  Dhananjay B. Ghonasgi ,  Maziar Sardashti ,  Bruce B. Randolph

IPC: B01J8/04 ,  C07C29/88 ,  B01J31/06 ,  C10L1/02

Abstract: Systems for the catalytic activation and/or dehydrogenation of a paraffin feed stream that is enriched in C5 alkanes to produce olefins that are then hydrated in the presence of water to produce C5 alcohols. Optionally, paraffin isomers are separated and the n-paraffins isomerized prior to catalytic activation and/or dehydrogenation.

公开(公告)号：US11648519B2

公开(公告)日：2023-05-16

申请号：US17153390

申请日：2021-01-20

Applicant: PHILLIPS 66 COMPANY

Inventor： Jianhua Yao ,  Anthony O. Baldridge ,  Neal D. McDaniel ,  James A. Suttil ,  Chengtian Wu ,  Dhananjay B. Ghonasgi ,  Maziar Sardashti ,  Bruce B. Randolph

IPC: B01J8/04 ,  C07C29/88 ,  C10L1/02 ,  B01J31/06

CPC classification number: B01J8/0492 ,  B01J31/06 ,  C07C29/88 ,  C10L1/02 ,  B01J2231/645 ,  B01J2531/002

Abstract: Systems for the catalytic activation and/or dehydrogenation of a paraffin feed stream that is enriched in C5 alkanes to produce olefins that are then hydrated in the presence of water to produce C5 alcohols. Optionally, paraffin isomers are separated and the n-paraffins isomerized prior to catalytic activation and/or dehydrogenation.

公开(公告)号：US20210222079A1

公开(公告)日：2021-07-22

申请号：US17153374

申请日：2021-01-20

Applicant: PHILLIPS 66 COMPANY

Inventor： Jianhua Yao ,  Anthony O. Baldridge ,  Neal D. McDaniel ,  James A. Suttil ,  Chengtian Wu ,  Dhananjay B. Ghonasgi ,  Maziar Sardashti ,  Bruce B. Randolph

IPC: C10L1/182 ,  C07C29/04 ,  C07C5/333 ,  C07C5/27

Abstract: Processes for the catalytic activation and/or dehydrogenation of a paraffin feed stream that is enriched in C5 alkanes to produce olefins that are then hydrated in the presence of water to produce C5 alcohols. Optionally, paraffin isomers are separated and the n-paraffins isomerized prior to catalytic activation and/or dehydrogenation.