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:
Oct. 03, 2023

Filed:

Sep. 30, 2022
Applicant:

Indian Oil Corporation Limited, Mumbai, IN;

Inventors:

Siva Rama Krishna Garapati, Faridabad, IN;

Meeta Sharma, Faridabad, IN;

Mani Ramya, Faridabad, IN;

Rajesh Muralidhar Badhe, Faridabad, IN;

Alok Sharma, Faridabad, IN;

Gurpreet Kapur Singh, Faridabad, IN;

Sankara Sri Venkata Ramakumar, Faridabad, IN;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 29/151 (2006.01); C01B 3/16 (2006.01); C07C 29/154 (2006.01);
U.S. Cl.
CPC ...
C07C 29/1518 (2013.01); C01B 3/16 (2013.01); C07C 29/154 (2013.01); C01B 2203/061 (2013.01); C01B 2203/1076 (2013.01);
Abstract

The present disclosure provides an integrated process and a Cu/Zn-based catalyst system for synthesizing methanol from COand generating electricity from hydrocarbon feedstock. The process includes steps of gasifying hydrocarbon feedstock into syngas by using oxygen and using the produced syngas as a fuel in a power generation unit, reusing a first part of an exhaust stream of the power generation unit as a reactant in the gasification unit. Using a second part of the said exhaust stream as a reactant for methanol synthesis in a methanol reactor, wherein, the second part is treated to separate COand water, and COis used as the reactant for methanol synthesis. Operating an electrolyzer during non-peak hours to produce hydrogen, wherein, a required stoichiometric ratio of the produced hydrogen is transferred into the methanol reactor for methanol synthesis, wherein, a Cu/Zn-based catalyst system is used for methanol synthesis through a direct hydrogenation reaction of CO.


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