The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Jan. 23, 2024

Filed:

Jan. 24, 2020
Applicant:

Sabic Global Technologies B.v., Bergen Op Zoom, NL;

Inventors:

Anthoni Van Zijl, Geleen, NL;

Nicolas Goyheneix, Geleen, NL;

Lara Galan-Sanchez, Geleen, NL;

Christoph Roosen, Geleen, NL;

Johan Pastwa, Geleen, NL;

Safa Farajzadeh Bibalan, Geleen, NL;

Assignee:

SABIC GLOBAL TECHNOLOGIES B.V., Bergen Op Zoom, NL;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 57/02 (2006.01); C08J 11/14 (2006.01); C08L 23/06 (2006.01); B29B 17/04 (2006.01); C08J 11/00 (2006.01); C10G 9/14 (2006.01); C10G 50/00 (2006.01); C10G 69/12 (2006.01); C10G 1/10 (2006.01); C10G 47/00 (2006.01); B29C 48/275 (2019.01); B29B 17/02 (2006.01); C08J 11/06 (2006.01); C10G 51/02 (2006.01); C08J 11/12 (2006.01); B29B 17/00 (2006.01);
U.S. Cl.
CPC ...
C10G 57/02 (2013.01); B29B 17/02 (2013.01); B29B 17/04 (2013.01); B29C 48/277 (2019.02); C08J 11/00 (2013.01); C08J 11/06 (2013.01); C08J 11/12 (2013.01); C08J 11/14 (2013.01); C08L 23/06 (2013.01); C10G 1/10 (2013.01); C10G 9/14 (2013.01); C10G 47/00 (2013.01); C10G 50/00 (2013.01); C10G 51/023 (2013.01); C10G 69/12 (2013.01); B29B 2017/0089 (2013.01); B29B 2017/0203 (2013.01); B29B 2017/0496 (2013.01); C08J 2300/30 (2013.01); C08L 2207/20 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/1085 (2013.01); C10G 2300/1096 (2013.01); C10G 2300/201 (2013.01); C10G 2400/20 (2013.01);
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 <0.8.


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