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:
Jun. 09, 2020

Filed:

Jun. 30, 2014
Applicants:

Saudi Basic Industries Corporation, Riyadh, SA;

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

Inventors:

Andrew Mark Ward, Stockton-on-Tees, GB;

Ravichander Narayanaswamy, Bangalore, IN;

Arno Johannes Maria Oprins, Maastricht, NL;

Vijayanand Rajagopalan, Bangalore, IN;

Egidius Jacoba Maria Schaerlaeckens, Geleen, NL;

Raul Velasco Pelaez, Maastricht, NL;

Assignees:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 69/02 (2006.01); C10G 65/10 (2006.01); C10G 47/14 (2006.01); C10G 47/16 (2006.01); C10G 65/18 (2006.01); C10G 47/02 (2006.01); C10G 65/00 (2006.01); C10G 47/20 (2006.01);
U.S. Cl.
CPC ...
C10G 69/02 (2013.01); C10G 47/02 (2013.01); C10G 47/14 (2013.01); C10G 47/16 (2013.01); C10G 47/20 (2013.01); C10G 65/00 (2013.01); C10G 65/10 (2013.01); C10G 65/18 (2013.01); B01J 2219/00002 (2013.01); B01J 2219/0004 (2013.01); B01J 2219/00006 (2013.01); B01J 2219/00027 (2013.01); B01J 2219/00033 (2013.01); B01J 2219/0038 (2013.01); B01J 2219/00042 (2013.01); C10G 2300/104 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/1051 (2013.01); C10G 2300/1055 (2013.01); C10G 2300/1059 (2013.01); C10G 2400/20 (2013.01); C10G 2400/30 (2013.01); Y02P 20/125 (2015.11);
Abstract

The present invention relates to an integrated process to convert crude oil into petrochemical products comprising crude oil distillation, hydrocracking and olefins synthesis, which process comprises subjecting a hydrocracker feed to hydrocracking to produce LPG and BTX and subjecting the LPG produced in the process to olefins synthesis. Furthermore, the present invention relates to a process installation to convert crude oil into petrochemical products comprising: a crude distillation unit comprising an inlet for crude oil and at least one outlet for one or more of naphtha, kerosene and gasoil; a hydrocracker comprising an inlet for a hydrocracker feed, an outlet for LPG and an outlet for BTX; and a unit for olefins synthesis comprising an inlet for LPG produced by the integrated petrochemical process installation and an outlet for olefins. The hydrocracker feed used in the process and the process installation of the present invention comprises one or more of naphtha, kerosene and gasoil produced by crude oil distillation in the process; and refinery unit-derived light-distillate and/or refinery unit-derived middle-distillate produced in the process. The process and process installation of the present invention have an increased production of petrochemicals at the expense of the production of fuels and an improved carbon efficiency in terms of the conversion of crude oils into petrochemicals.


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