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:

Jun. 08, 2020
Applicant:

Dow Global Technologies Llc, Midland, MI (US);

Inventors:

Lin Luo, Sugar Land, TX (US);

Hangyao Wang, Pearland, TX (US);

Yu Liu, Lake Jackson, TX (US);

Matthew T. Pretz, Lake Jackson, TX (US);

Andrzej Malek, Midland, MI (US);

Assignee:

Dow Global Technoogies LLC, Midland, MI (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 5/00 (2006.01); C07C 5/333 (2006.01); B01J 23/62 (2006.01); C07C 4/04 (2006.01); C07C 7/167 (2006.01);
U.S. Cl.
CPC ...
C07C 5/3337 (2013.01); B01J 23/62 (2013.01); C07C 4/04 (2013.01); C07C 5/333 (2013.01); C07C 7/167 (2013.01); C07C 2523/62 (2013.01);
Abstract

A method for operating an acetylene hydrogenation unit in an integrated steam cracking-fluidized catalytic dehydrogenation (FCDh) system may include separating a cracked gas from a steam cracking system and an FCDh effluent from an FCDh system into a hydrogenation feed and an acetylene-depleted stream, the hydrogenation feed comprising at least hydrogen, CO, and acetylene. During normal operating conditions, at least 20% of the CO in the hydrogenation feed is from the cracked gas. The method may include contacting the hydrogenation feed with an acetylene hydrogenation catalyst to hydrogenate at least a portion of the acetylene in the hydrogenation feed to produce a hydrogenated effluent. The steam cracking is operated under conditions that increase CO production such that a concentration of CO in the cracked gas is great enough that when a flowrate of the FCDh effluent is zero, a CO concentration in the hydrogenation feed is at least 100 ppmv.


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