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:
Apr. 01, 2025

Filed:

Dec. 31, 2019
Applicant:

Eni S.p.a., Rome, IT;

Inventors:

Sivadinarayana Chinta, Sugar Land, TX (US);

Ravichander Narayanaswamy, Bengaluru, IN;

Atul Pant, Bengaluru, IN;

Assignee:

ENI S.P.A., Rome, IT;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 29/151 (2006.01); B01D 53/047 (2006.01); B01D 53/22 (2006.01); C01B 3/38 (2006.01); C07C 5/333 (2006.01); F25J 1/00 (2006.01);
U.S. Cl.
CPC ...
C07C 29/1518 (2013.01); B01D 53/047 (2013.01); B01D 53/229 (2013.01); C01B 3/382 (2013.01); C07C 5/333 (2013.01); B01D 2256/16 (2013.01); B01D 2256/24 (2013.01); B01D 2257/7022 (2013.01); C01B 2203/0261 (2013.01); C01B 2203/061 (2013.01); C01B 2203/062 (2013.01); C01B 2203/0833 (2013.01); F25J 1/001 (2013.01);
Abstract

A process for producing syngas and olefins including the steps of feeding a catalytic partial oxidation (CPO) reactant mixture (oxygen, first hydrocarbons, steam) to a CPO reactor (CPO catalyst); wherein the CPO reactant mixture reacts, via CPO reaction, in CPO reactor to produce a CPO reactor effluent (H, CO, CO, water, unreacted first hydrocarbons). The process further includes feeding a cracking unit feed (second hydrocarbons) to a cracking unit to produce a cracking unit product (olefins), a hydrogen-rich stream (hydrogen, CH), and a hydrocarbon recovery stream (Chydrocarbons); wherein the first and the second hydrocarbons are the same or different; recovering a hydrogen-enriched stream (hydrogen) and a hydrocarbon-enriched stream (CH) from the hydrogen-rich stream; and contacting the CPO reactor effluent with the hydrogen-enriched stream to yield hydrogen-enriched syngas, and wherein the M ratio ((H—CO)/(CO+CO)) of the hydrogen-enriched syngas is greater than the M ratio of the CPO reactor effluent.


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