公开(公告)号：US09752080B2

公开(公告)日：2017-09-05

申请号：US14771849

申请日：2014-03-25

Applicant: Haldor Topsøe A/S

Inventor： Thomas Sandahl Christensen ,  Ole Frej Alkilde

IPC: C10G2/00 ,  C01B3/38 ,  C10G47/00 ,  C10G65/12 ,  C10K3/02 ,  C07C5/03 ,  C07C7/148

CPC classification number: C10G2/32 ,  C01B3/382 ,  C01B3/386 ,  C01B2203/0244 ,  C01B2203/062 ,  C01B2203/063 ,  C01B2203/1052 ,  C01B2203/1058 ,  C01B2203/1241 ,  C01B2203/1247 ,  C01B2203/1264 ,  C01B2203/127 ,  C07C5/03 ,  C07C7/148 ,  C10G47/00 ,  C10G65/12 ,  C10G2300/1022 ,  C10G2300/4081 ,  C10G2400/02 ,  C10K3/026

Abstract: The invention relates to a process for the production of liquid hydrocarbons by the use of light-end fractions from downstream synthesis in the reforming section of the plant.

公开(公告)号：US20170267938A1

公开(公告)日：2017-09-21

申请号：US15532444

申请日：2015-12-16

Applicant: Haldor Topsøe A/S

Inventor： Stefan Andersen ,  Ole Frej Alkilde

IPC: C10G67/02

CPC classification number: C10G67/02 ,  C10G7/00 ,  C10G7/06 ,  C10G47/02 ,  C10G47/12 ,  C10G47/16 ,  C10G2300/1055 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/04

Abstract: In a broad aspect the present disclosure relates to a process plant and a process for upgrading a hydrocarbon mixture, withdrawn as a direct stream from a crude distillation unit and an initial boiling point below 200° C., and a fraction of at least 5% boiling above 500° C., 550° C. or 650° C. comprising the steps of a. directing said hydrocarbon mixture to a vacuum flasher unit, b. withdrawing a heavy hydrocarbon fraction from said vacuum flasher unit, c. withdrawing a light hydrocarbon mixture for hydrocracking from said vacuum flasher unit, d. directing said light hydrocarbon mixture for hydrocracking and a stream rich in hydrogen to con-tact a material catalytically active in hydrocracking, e. withdrawing a hydrocracked stream of hydrocarbon from said hydrocracker. with the associated benefit of limiting the amount of asphaltenes, metals and other heavy components contacting said material catalytically active in hydrocracking.

公开(公告)号：US12139673B2

公开(公告)日：2024-11-12

申请号：US17287729

申请日：2019-10-23

Applicant: HALDOR TOPSØE A/S

Inventor： Asbjørn Sune Andersson ,  Ole Frej Alkilde ,  Thi Hong Diep Duong

IPC: C10G65/12 ,  C10G3/00 ,  C10G45/48 ,  C10G45/52 ,  C10G45/62 ,  C10G47/14 ,  C10G47/18 ,  C10G47/20 ,  C10G67/02 ,  C10G69/04 ,  C10L1/08

Abstract: A process plant and a process for production of a hydrocarbon fraction suitable for use as jet fuel from a feedstock being a renewable feedstock or an oxygenate feedstock, including combining the feedstock with an amount of a hydrocracked intermediate product and optionally an additional liquid diluent, to form a combined feedstock, directing the combined feedstock to contact a material catalytically active in hydrodeoxygenation under hydrotreating conditions to provide a hydrodeoxygenated intermediate product, separating the hydrodeoxygenated intermediate product in at least two fractions; a vapor fraction and a liquid fraction, directing at least an amount of the liquid fraction to contact a material catalytically active in isomerization under isomerization conditions to provide an isomerized intermediate product, fractionating said isomerized intermediate product to provide at least a hydrocarbon suitable for use as jet fuel and a bottom fraction, hydrocracking the bottom fraction to provide the hydrocracked intermediate product.

公开(公告)号：US10072222B2

公开(公告)日：2018-09-11

申请号：US15532444

申请日：2015-12-16

Applicant: Haldor Topsøe A/S

Inventor： Stefan Andersen ,  Ole Frej Alkilde

IPC: C10G67/02

Abstract: In a broad aspect the present disclosure relates to a process plant and a process for upgrading a hydrocarbon mixture, withdrawn as a direct stream from a crude distillation unit and an initial boiling point below 200° C., and a fraction of at least 5% boiling above 500° C., 550° C. or 650° C. comprising the steps of a. directing said hydrocarbon mixture to a vacuum flasher unit, b. withdrawing a heavy hydrocarbon fraction from said vacuum flasher unit, c. withdrawing a light hydrocarbon mixture for hydrocrackingfrom said vacuum flasher unit, d. directing said light hydrocarbon mixture for hydrocracking and a stream rich in hydrogen to con-tact a material catalytically active in hydrocracking, e. withdrawing a hydrocracked stream of hydrocarbon from said hydrocracker. with the associated benefit of limiting the amount of asphaltenes, metals and other heavy components contacting said material catalytically active in hydrocracking.