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:
May. 12, 2020

Filed:

Aug. 30, 2018
Applicant:

Indian Oil Corporation Limited, Mumbai, IN;

Inventors:

Mainak Sarkar, Faridabad, IN;

Darshankumar Manubhai Dave, Faridabad, IN;

Ramesh Karumanchi, Faridabad, IN;

Madhusudan Sau, Faridabad, IN;

Ganesh Vitthalrao Butley, Faridabad, IN;

Nepal Vishwakarma, Faridabad, IN;

Kamal Kumar, Faridabad, IN;

Pravesh Kumar, Faridabad, IN;

Sarvesh Kumar, Faridabad, IN;

Debasis Bhattacharyya, Faridabad, IN;

Sanjiv Kumar Mazumdar, Faridabad, IN;

Sankara Sri Venkata Ramakumar, Faridabad, IN;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 47/24 (2006.01); C10G 47/00 (2006.01); C10G 47/26 (2006.01); B01J 4/00 (2006.01); B01J 8/12 (2006.01);
U.S. Cl.
CPC ...
C10G 47/24 (2013.01); B01J 4/002 (2013.01); B01J 4/004 (2013.01); B01J 8/12 (2013.01); B01J 8/125 (2013.01); C10G 47/00 (2013.01); C10G 47/26 (2013.01); B01J 2208/00911 (2013.01); B01J 2219/185 (2013.01); B01J 2219/1943 (2013.01); C10G 2300/206 (2013.01); C10G 2300/80 (2013.01);
Abstract

The present invention relates to a hydrocracking reactor system and a process utilizing the same for upgrading heavy hydrocarbonaceous material to value-added products. Accordingly, an aspect of the present invention includes dispersing a liquid feedstock pre-mixed with a catalyst from top of a reactor vessel to obtain dispersed droplets having a predetermined droplet size less than 500 μm, introducing a gaseous feed comprising primarily of hydrogen from bottom of the reactor vessel to form a continuous gaseous phase throughout a cross-section of the reactor vessel, and allowing the dispersed droplets to contact the continuous gaseous phase throughout the cross-section of the reactor vessel to form reaction effluent comprising one or more lighter product hydrocarbons. The method may further include removing at least a top portion and at least a bottom portion of the reaction effluent from the reactor vessel.


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