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:
Sep. 03, 2019

Filed:

Nov. 14, 2017
Applicant:

Exxonmobil Research and Engineering Company, Annandale, NJ (US);

Inventors:

Tien V. Le, Houston, TX (US);

Brenda A. Raich, Annandale, NJ (US);

Bing Du, Pittstown, NJ (US);

Mohsen N. Harandi, New Hope, PA (US);

Suriyanarayanan Rajagopalan, Spring, TX (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 2/06 (2006.01); C07C 4/04 (2006.01); C10J 3/84 (2006.01); C10B 49/22 (2006.01); C10B 55/10 (2006.01); C07C 29/151 (2006.01);
U.S. Cl.
CPC ...
C10B 55/10 (2013.01); C07C 2/06 (2013.01); C07C 4/04 (2013.01); C07C 29/1518 (2013.01); C10B 49/22 (2013.01); C10J 3/84 (2013.01); C10J 2300/0903 (2013.01); C10J 2300/0943 (2013.01); C10J 2300/0959 (2013.01); C10J 2300/1659 (2013.01);
Abstract

Systems and methods are provided for integrating a fluidized coking process, optionally a coke gasification process, and processes for production of additional liquid products from the coking and/or gasification process. In some aspects, the integrated processes can allow for conversion of olefins generated during a fluidized coking process to form additional liquid products. Additionally or alternately, in some aspects the integrated processes can allow for separation of syngas from the flue gas/fuel gas generated by a gasifier integrated with a fluidized coking process. This syngas can then be used to form methanol, which can then be converted in a methanol conversion process to form heavier products. In such aspects, olefins generated during the fluidized coking process can be added to the methanol conversion process to improve the yield. Additionally, in various aspects, the off-gas from the integrated conversion process can be used as an additional paraffin feed that can be recycled to one of the heat integration conduits in the fluidized coker for additional generation of olefins. This can provide a further increase in liquid yields using a carbon source (Cparaffins) that is conventionally viewed as a low value product from coking.


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