公开(公告)号：US20190062646A1

公开(公告)日：2019-02-28

申请号：US15765300

申请日：2016-09-23

Applicant: SABIC Global Technologies B.V.

Inventor： Abrar A. HAKEEM ,  Ashim Kumar GHOSH

IPC: C10G45/08 ,  C10G45/10 ,  C10G45/04 ,  C10G67/10

Abstract: A process for reducing a chloride content of a hydrocarbon feed stream involving contacting a hydrocarbon feed stream comprising a chloride containing pyrolysis oil obtained by cracking a chloride containing thermoplastic material with a sulfided catalyst comprising at least one of Co, Mo, and Ni or a catalyst comprising Pd, Pt, Cu, and/or Zn on a catalyst support in the presence of hydrogen gas to reduce one or more organic chloride compounds present in the hydrocarbon feed stream and form a hydrocarbon product stream and HCl. The HCl is removed from the hydrocarbon product stream, wherein the hydrocarbon product stream has a lower chloride content than the hydrocarbon feed stream based on the total weight of the chloride and the total weight of the hydrocarbon feed stream.

公开(公告)号：US20190299491A1

公开(公告)日：2019-10-03

申请号：US16318464

申请日：2017-07-17

Applicant: SABIC Global Technologies B.V.

Inventor： Alexander STANISLAUS ,  Ravichander NARAYANASWAMY ,  Krishna Kumar RAMAMURTHY ,  Santosh GANJI ,  Abrar A. HAKEEM ,  Ashim Kumar GHOSH ,  Girish KORIPELLY ,  Mohammad JAVEED

IPC: B29B17/04 ,  C10B53/07 ,  C10G69/06 ,  C10G11/18 ,  C10G45/02 ,  C10K1/00 ,  B01J29/08 ,  B01J29/40 ,  B01J29/18 ,  B01J29/85

Abstract: A process for processing mixed plastics comprising simultaneous pyrolysis and dechlorination of the mixed plastics, the process comprising contacting the mixed plastics with a zeolitic catalyst in a pyrolysis unit to produce a hydrocarbon product comprising a gas phase and a liquid phase; and separating the hydrocarbon product into a hydrocarbon gas stream and a hydrocarbon liquid stream, wherein the hydrocarbon gas stream comprises at least a portion of the gas phase of the hydrocarbon product, wherein the hydrocarbon liquid stream comprises at least a portion of the liquid phase of the hydrocarbon product, wherein the hydrocarbon liquid stream comprises one or more chloride compounds in an amount of less than about 100 ppmw chloride, based on the total weight of the hydrocarbon liquid stream, and wherein the hydrocarbon liquid stream is characterized by a viscosity of less than about 400 cP at a temperature of 300° C.

公开(公告)号：US20190270939A1

公开(公告)日：2019-09-05

申请号：US16319878

申请日：2017-07-17

Applicant: SABIC Global Technologies B.V.

Inventor： Mohammad JAVEED ,  Alexander STANISLAUS ,  Abrar A. HAKEEM ,  Girish KORIPELLY ,  Ravichander NARAYANASWAMY ,  Krishna Kumar RAMAMURTHY

IPC: C10G25/05 ,  C10G55/04 ,  C10G55/06 ,  C10G1/00 ,  C10G1/10

Abstract: A process for dechlorination of a hydrocarbon stream and/or a hydrocarbon stream precursor comprising introducing the hydrocarbon stream and/or hydrocarbon stream precursor, a first zeolitic catalyst, and a stripping gas to a devolatilization extruder (DE) to produce an extruder effluent, wherein the hydrocarbon stream and/or hydrocarbon stream precursor comprises one or more chloride compounds in an amount of equal to or greater than about 10 ppm chloride, based on the total weight of the hydrocarbon stream and/or hydrocarbon stream precursor, and wherein the extruder effluent comprises one or more chloride compounds in an amount of less than the chloride amount in the hydrocarbon stream and/or hydrocarbon stream precursor.

公开(公告)号：US20190161683A1

公开(公告)日：2019-05-30

申请号：US16323191

申请日：2017-09-21

Applicant: SABIC Global Technologies B.V.

Inventor： Ravichander NARAYANASWAMY ,  Krishna Kumar RAMAMURTHY ,  Abrar A. HAKEEM ,  Lara GALAN-SANCHEZ ,  Nicolas GOYHENEIX ,  Santosh GANJI

IPC: C10G1/10 ,  C10G1/06 ,  C10G69/14 ,  C10B53/07 ,  C10B47/24 ,  C10B57/06 ,  B01D53/40 ,  B01D53/78 ,  B01D3/14

Abstract: A process for processing plastic waste comprising converting plastic waste to hydrocarbon liquid and a first C1-4 gas; contacting hydrocarbon liquid with a first hydroprocessing catalyst in hydroprocessing unit to yield a second C1-4 gas and a first hydrocarbon product comprising C5+ liquid hydrocarbons; introducing the first hydrocarbon product to a first separating unit to produce treated hydrocarbon stream comprising C5-8 hydrocarbons and a first heavies stream comprising C9+ hydrocarbons; contacting the first heavies stream with a second hydroprocessing catalyst in hydrodealkylating unit to yield a second hydrocarbon product comprising C5+ liquid hydrocarbons and a third C1-4 gas; conveying the second hydrocarbon product to the first separating unit; feeding treated hydrocarbon stream to steam cracker to produce steam cracker product; separating steam cracker product into olefin gas, saturated hydrocarbons gas, aromatics, and a second heavies stream; and conveying the second heavies stream to hydroprocessing unit.