公开(公告)号：US20240352346A1

公开(公告)日：2024-10-24

申请号：US18714758

申请日：2022-12-01

Applicant: SABIC Global Technologies B.V.

Inventor： Amit Sharma ,  Fabrice Cuoq ,  Ziyu Liu ,  Safa Farajzadeh Bibalan ,  Sreenivasa Rao

IPC: C10G53/12 ,  C10G1/10

CPC classification number: C10G53/12 ,  C10G1/10 ,  C10G2300/1003 ,  C10G2300/202 ,  C10G2300/4006

Abstract: Systems and methods for pretreating a raw mixed plastic waste pyrolysis oil to remove silicon and chloride contaminants using an aqueous alkaline hydroxide solution. Specifically, these systems and methods lead to at least about 30 weight percent reduction in the silicon compounds present in the pyrolysis oil and at least about 50 weight percent reduction in the chloride compounds in the pyrolysis oil.

公开(公告)号：US12024683B2

公开(公告)日：2024-07-02

申请号：US17424560

申请日：2020-01-24

Applicant: SABIC GLOBAL TECHNOLOGIES B.V.

Inventor： Anthoni Van Zijl ,  Nicolas Goyheneix ,  Lara Galan-Sanchez ,  Christoph Roosen ,  Johan Pastwa ,  Safa Farajzadeh Bibalan

IPC: C10G57/02 ,  B29B17/02 ,  B29B17/04 ,  B29C48/275 ,  C08J11/00 ,  C08J11/06 ,  C08J11/12 ,  C08J11/14 ,  C08L23/06 ,  C10G1/10 ,  C10G9/14 ,  C10G47/00 ,  C10G50/00 ,  C10G51/02 ,  C10G69/12 ,  B29B17/00

CPC classification number: C10G57/02 ,  B29B17/02 ,  B29B17/04 ,  B29C48/277 ,  C08J11/00 ,  C08J11/06 ,  C08J11/12 ,  C08J11/14 ,  C08L23/06 ,  C10G1/10 ,  C10G9/14 ,  C10G47/00 ,  C10G50/00 ,  C10G51/023 ,  C10G69/12 ,  B29B2017/0089 ,  B29B2017/0203 ,  B29B2017/0496 ,  C08J2300/30 ,  C08L2207/20 ,  C10G2300/1003 ,  C10G2300/1085 ,  C10G2300/1096 ,  C10G2300/201 ,  C10G2400/20

Abstract: A process for the production of ethylene-based polymers from waste plastics feedstocks includes the steps in this order of: providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; providing a hydrocarbon stream B; supplying a feed C including a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace having cracking coil(s); performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; supplying the cracked hydrocarbon stream D to a separation unit to obtain a product stream E containing ethylene; supplying the product stream E to a polymerisation reactor; and performing a polymerisation reaction to obtain an ethylene-based polymer; wherein in step (d): the coil outlet temperature is ≥800 and ≤870° C.; and the weight ratio of steam to feed C is >0.3 and

公开(公告)号：US20230279179A1

公开(公告)日：2023-09-07

申请号：US18017265

申请日：2021-07-15

Applicant: SABIC Global Technologies B.V.

Inventor： Anthoni Wouter Zijl Van ,  Nicolas Goyheneix ,  Lara Maria Galan-Sanchez ,  Christoph Roosen ,  Johan Pastwa ,  Safa Farajzadeh Bibalan

IPC: C08G64/02 ,  C10G55/04 ,  C10B53/07

CPC classification number: C08G64/0233 ,  C10B53/07 ,  C10G55/04 ,  C10G2300/1003 ,  C10G2300/1037

Abstract: Process for the production of polycarbonates comprising providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock; supplying a feed C comprising a fraction of the hydrocarbon stream A to a thermal cracker furnace comprising cracking coil(s); thermally cracking in the presence of steam to obtain a cracked hydrocarbon stream D; separating a product stream E comprising propylene and a product stream F comprising benzene from the cracked hydrocarbon stream D; performing a reaction and one or more separation step to obtain a product stream G comprising phenol; supplying the product stream G and acetone to a reactor and performing a reaction and one or more separation step to obtain a product stream H comprising bisphenol-A; and supplying the product stream H with phosgene or diphenyl carbonate to a reactor and performing a polymerisation reaction to obtain a polycarbonate.

公开(公告)号：US12215188B2

公开(公告)日：2025-02-04

申请号：US18017265

申请日：2021-07-15

Applicant: SABIC Global Technologies B.V.

Inventor： Anthoni Wouter Zijl Van ,  Nicolas Goyheneix ,  Lara Maria Galan-Sanchez ,  Christoph Roosen ,  Johan Pastwa ,  Safa Farajzadeh Bibalan

IPC: C08G64/02 ,  C10B53/07 ,  C10G55/04

Abstract: Process for the production of polycarbonates comprising: providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock; supplying a feed C comprising a fraction of the hydrocarbon stream A to a thermal cracker furnace comprising cracking coil(s); thermally cracking in the presence of steam to obtain a cracked hydrocarbon stream D; separating a product stream E comprising propylene and a product stream F comprising benzene from the cracked hydrocarbon stream D; performing a reaction and one or more separation step to obtain a product stream G comprising phenol; supplying the product stream G and acetone to a reactor and performing a reaction and one or more separation step to obtain a product stream H comprising bisphenol-A; and supplying the product stream H with phosgene or diphenyl carbonate to a reactor and performing a polymerisation reaction to obtain a polycarbonate.

公开(公告)号：US12152001B2

公开(公告)日：2024-11-26

申请号：US18017325

申请日：2021-07-15

Applicant: SABIC Global Technologies B.V.

Inventor： Anthoni Wouter Zijl Van ,  Nicolas Goyheneix ,  Lara Maria Galan-Sanchez ,  Christoph Roosen ,  Johan Pastwa ,  Safa Farajzadeh Bibalan

IPC: C07C4/04 ,  C07C7/00

Abstract: Process for the production of butenes and butadienes from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; and (f) performing a separation operation to obtain different streams comprising isobutene, 1-butene, 2-butene, 1,2-butediene and 1,3-butadiene; wherein in step (d): •the coil outlet temperature is ≥800 and ≤850° C.; and•the weight ratio of steam to feed C is >0.3 and

公开(公告)号：US20230323213A1

公开(公告)日：2023-10-12

申请号：US18017335

申请日：2021-07-15

Applicant: SABIC Global Technologies B.V.

Inventor： Anthoni Wouter Zijl Van ,  Nicolas Goyheneix ,  Lara Maria Galan-Sanchez ,  Christoph Roosen ,  Johan Pastwa ,  Safa Farajzadeh Bibalan

IPC: C10G1/10 ,  C10G1/00 ,  C10G9/36

CPC classification number: C10G1/10 ,  C10G1/002 ,  C10G9/36 ,  C10G2300/1003 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2400/20

Abstract: Process for the production of butenes and butadienes from waste plastics feedstocks comprising the steps: (a) providing a hydrocarbon stream A obtained by hydrotreatment of pyrolysis oil produced from a waste plastics feedstock; (b) optionally providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and optionally a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; and (f) performing a separation operation to obtain different streams comprising isobutene, 1-butene, 2-butene, 1,2-butediene and 1,3-butadiene; wherein in step (d): • the coil outlet temperature is ≥ 800 and ≤ 850° C.; and • the weight ratio of steam to feed C is > 0.3 and

公开(公告)号：US20230287175A1

公开(公告)日：2023-09-14

申请号：US18017253

申请日：2021-07-15

Applicant: SABIC Global Technologies B.V.

Inventor： Anthoni Wouter Zijl Van ,  Nicolas Goyheneix ,  Lara Maria Galan-Sanchez ,  Christoph Roosen ,  Johan Pastwa ,  Safa Farajzadeh Bibalan

IPC: C08G64/30 ,  C08J11/10

CPC classification number: C08G64/307 ,  C08J11/10 ,  C08J2369/00

Abstract: Process for the production of polycarbonates comprising: providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of a hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); thermally cracking in the presence of steam to obtain a cracked hydrocarbon stream D; separating a product stream E comprising propylene and a product stream F comprising benzene from the cracked hydrocarbon stream D; performing a reaction and one or more separation step to obtain a product stream G comprising phenol; supplying the product stream G and acetone to a reactor and performing a reaction and one or more separation step to obtain a product stream H comprising bisphenol-A; and supplying the product stream H with phosgene or diphenyl carbonate to a reactor and performing a polymerisation reaction to obtain a polycarbonate.

公开(公告)号：US12264129B2

公开(公告)日：2025-04-01

申请号：US18017340

申请日：2021-07-15

Applicant: SABIC Global Technologies B.V.

Inventor： Anthoni Wouter Zijl Van ,  Nicolas Goyheneix ,  Lara Maria Galan-Sanchez ,  Christoph Roosen ,  Johan Pastwa ,  Safa Farajzadeh Bibalan

IPC: C07C4/04 ,  C10B53/07

Abstract: The present invention relates to a process for the production of butenes and butadienes from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; (f) performing a separation operation to obtain different streams of chemical products comprising ethylene, propylene, isobutene, 1-butene, 2-butene, 1,2-butadiene, 1,3-butadiene, benzene, styrene, toluene, ethylbenzene and xylenes; wherein in step (d): ⋅ the coil outlet temperature is ≥800 and ≤870° C., preferably ≥805 and ≤835° C.; and ⋅ the weight ratio of steam to feed C is >0.3 and 0.3 and

公开(公告)号：US11879102B2

公开(公告)日：2024-01-23

申请号：US17424701

申请日：2020-01-24

Applicant: SABIC GLOBAL TECHNOLOGIES B.V.

Inventor： Anthoni Van Zijl ,  Nicolas Goyheneix ,  Lara Galan-Sanchez ,  Christoph Roosen ,  Johan Pastwa ,  Safa Farajzadeh Bibalan

IPC: C10G57/02 ,  C08J11/14 ,  C08L23/06 ,  B29B17/04 ,  C08J11/00 ,  C10G9/14 ,  C10G50/00 ,  C10G69/12 ,  C10G1/10 ,  C10G47/00 ,  B29C48/275 ,  B29B17/02 ,  C08J11/06 ,  C10G51/02 ,  C08J11/12 ,  B29B17/00

CPC classification number: C10G57/02 ,  B29B17/02 ,  B29B17/04 ,  B29C48/277 ,  C08J11/00 ,  C08J11/06 ,  C08J11/12 ,  C08J11/14 ,  C08L23/06 ,  C10G1/10 ,  C10G9/14 ,  C10G47/00 ,  C10G50/00 ,  C10G51/023 ,  C10G69/12 ,  B29B2017/0089 ,  B29B2017/0203 ,  B29B2017/0496 ,  C08J2300/30 ,  C08L2207/20 ,  C10G2300/1003 ,  C10G2300/1085 ,  C10G2300/1096 ,  C10G2300/201 ,  C10G2400/20

Abstract: The present invention relates to a process for the production of ethylene-based polymers from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by hydrotreatment of a pyrolysis oil produced from a waste plastics feedstock; (b) optionally providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and optionally a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to a separation unit; (f) performing a separation operation in the separation unit to obtain a product stream E comprising ethylene; (g) supplying the product stream E to a polymerisation reactor; and (h) performing a polymerisation reaction in the polymerisation reactor to obtain an ethylene-based polymer; wherein in step (d): ⋅ · the coil outlet temperature is 2: 800 and:::; 870° C., preferably 2: 820 and:::; 870° C.; and ⋅ · the weight ratio of steam to feed C is >0.3 and

公开(公告)号：US20230295061A1

公开(公告)日：2023-09-21

申请号：US18017340

申请日：2021-07-15

Applicant: SABIC Global Technologies B.V.

Inventor： Anthoni Wouter Zijl Van ,  Nicolas Goyheneix ,  Lara Maria Galan-Sanchez ,  Christoph Roosen ,  Johan Pastwa ,  Safa Farajzadeh Bibalan

IPC: C07C4/04 ,  C10B53/07

CPC classification number: C07C4/04 ,  C10B53/07

Abstract: The present invention relates to a process for the production of butenes and butadienes from waste plastics feedstocks comprising the steps in this order of: (a) providing a hydrocarbon stream A obtained by treatment of a waste plastics feedstock; (b) providing a hydrocarbon stream B; (c) supplying a feed C comprising a fraction of the hydrocarbon stream A and a fraction of the hydrocarbon stream B to a thermal cracker furnace comprising cracking coil(s); (d) performing a thermal cracking operation in the presence of steam to obtain a cracked hydrocarbon stream D; (e) supplying the cracked hydrocarbon stream D to one or more separation units; (f) performing a separation operation to obtain different streams of chemical products comprising ethylene, propylene, isobutene, 1-butene, 2-butene, 1,2-butadiene, 1,3-butadiene, benzene, styrene, toluene, ethylbenzene and xylenes; wherein in step (d): ⋅ the coil outlet temperature is ≥800 and ≤870° C., preferably ≥805 and ≤835° C.; and ⋅ the weight ratio of steam to feed C is >0.3 and 0.3 and