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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
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.
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公开(公告)号:US10384991B2
公开(公告)日:2019-08-20
申请号:US15763743
申请日:2016-11-01
Applicant: SABIC Global Technologies B.V.
Inventor: Kuldeep Wadhwa , Antonio Matarredona , Radu Ignat , Sekhar Mamilla , Christoph Roosen , Alex Londono
IPC: C07C7/148 , C07C7/05 , C07C11/167
Abstract: The presently disclosed subject matter relates to methods and systems for purifying 1,3-butadiene from a C4 hydrocarbon stream. An example method includes introducing a C4 hydrocarbon stream including 1,3-butadiene and acetlyenes to an organic azide in the presence of a catalyst to generate a first stream including triazole, separating triazole from the first stream to produce a second stream including 1,3-butadiene, and distilling 1,3-butadiene from the second stream to produce a purified 1,3-butadiene product stream.
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公开(公告)号:US20230272286A1
公开(公告)日:2023-08-31
申请号:US18017010
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
CPC classification number: C10G1/10 , C10G47/02 , C10G47/36 , C10G2400/30 , C10G2300/1003 , C10G2300/4006 , C10G2300/807
Abstract: The present invention relates to a process for the production of aromatics 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 comprising benzene, toluene, styrene, ethylbenzene and xylenes; wherein in step (d): ⋅ the coil outlet temperature is ≥800 and ≤80° C., preferably ≥830 and ≤870° C.; 7 and ⋅ the weight ratio of steam to feed C is >0.3 and 0.3 and
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公开(公告)号:US20230257323A1
公开(公告)日:2023-08-17
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
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
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公开(公告)号:US11685867B2
公开(公告)日:2023-06-27
申请号:US17425466
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 , B29B17/04 , C08J11/00 , C10G9/14 , C10G50/00 , C10G69/12 , C10G1/10 , C10G47/00 , B29C48/275 , B29B17/02 , C08J11/06 , C10G51/02 , C08J11/12 , C08J11/14 , C08L23/06 , 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 polymers 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) optionally 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 a separation unit; (f) performing a separation operation in the separation unit to obtain a product stream E comprising a monomer; (g) supplying the product stream E to a polymerisation reactor; and (h) performing a polymerisation reaction in the polymerisation reactor to obtain an polymer. The process of the present invention allows for optimisation of the quantity of waste plastic material that finds its way back into a polymer that is produced as outcome of the process.
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公开(公告)号:US20230183579A1
公开(公告)日:2023-06-15
申请号:US18017345
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
CPC classification number: C10B53/07 , C10G1/10 , C10G9/14 , C10G2400/20
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 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; (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 805 and 0.3 and 0.3 and
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公开(公告)号:US11667854B2
公开(公告)日:2023-06-06
申请号:US17425173
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: C10G50/00 , C10G55/04 , B29B17/04 , C08J11/00 , C10G9/14 , C10G57/02 , C10G69/12 , C10G1/10 , C10G47/00 , B29C48/275 , B29B17/02 , C08J11/06 , C10G51/02 , C08J11/12 , C08J11/14 , C08L23/06 , B29B17/00
CPC classification number: C10G50/00 , B29B17/02 , B29B17/04 , B29C48/277 , C08J11/00 , C08J11/06 , C08J11/12 , C08J11/14 , C08L23/06 , C10G1/10 , C10G9/14 , C10G47/00 , C10G51/023 , C10G57/02 , 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 propylene-based polymers 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 a separation unit; (f) performing a separation operation in the separation unit to obtain a product stream E comprising propylene; (g) supplying the product stream E to a polymerisation reactor; and (h) performing a polymerisation reaction in the polymerisation reactor to obtain an propylene-based polymer; wherein in step (d): •⋅ the coil outlet temperature is 2:: 800 and:::; 850° C., preferably 2:: 805 and:::; 835° C.; and •⋅ the weight ratio of steam to feed C is >0.3 and
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公开(公告)号:US11230516B2
公开(公告)日:2022-01-25
申请号:US16375208
申请日:2019-04-04
Applicant: SABIC Global Technologies B.V.
Inventor: Kuldeep Wadhwa , Antonio Matarredona , Radu Ignat , Sekhar Mamilla , Christoph Roosen , Alex Londono
IPC: C07C7/148 , C07C7/05 , C07C11/167
Abstract: The presently disclosed subject matter relates to methods and systems for purifying 1,3-butadiene from a C4 hydrocarbon stream. An example method includes introducing a C4 hydrocarbon stream including 1,3-butadiene and acetylenes to an organic azide in the presence of a catalyst to generate a first stream including triazole, separating triazole from the first stream to produce a second stream including 1,3-butadiene, and distilling 1,3-butadiene from the second stream to produce a purified 1,3-butadiene product stream.
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