Invention Grant
- Patent Title: Process for the preparation of polypropylenes from waste plastic feedstocks
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Application No.: US17425173Application Date: 2020-01-24
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Publication No.: US11667854B2Publication Date: 2023-06-06
- Inventor: Anthoni Van Zijl , Nicolas Goyheneix , Lara Galan-Sanchez , Christoph Roosen , Johan Pastwa , Safa Farajzadeh Bibalan
- Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
- Applicant Address: NL Bergen Op Zoom
- Assignee: SABIC GLOBAL TECHNOLOGIES B.V.
- Current Assignee: SABIC GLOBAL TECHNOLOGIES B.V.
- Current Assignee Address: NL Bergen Op Zoom
- Agency: Cantor Colburn LLP
- Priority: EP 153458 2019.01.24 EP 153897 2019.01.28 EP 157064 2019.02.14 EP 157324 2019.02.14 EP 157898 2019.02.19
- International Application: PCT/EP2020/051731 2020.01.24
- International Announcement: WO2020/152320A 2020.07.30
- Date entered country: 2021-07-22
- Main IPC: C10G50/00
- 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

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
Public/Granted literature
- US20220089957A1 PROCESS FOR THE PREPARATION OF POLYPROPYLENES FROM WASTE PLASTIC FEEDSTOCKS Public/Granted day:2022-03-24
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