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:
Jul. 14, 2020

Filed:

Oct. 27, 2017
Applicant:

Uop Llc, Des Plaines, IL (US);

Inventor:

Eleftherios Adamopoulos, Gurnee, IL (US);

Assignee:

UOP LLC, Des Plaines, IL (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 3/50 (2006.01); B01D 53/22 (2006.01); B01D 53/047 (2006.01); B01D 53/02 (2006.01); B01D 69/08 (2006.01); B01D 71/16 (2006.01); B01D 71/64 (2006.01); B01D 71/68 (2006.01);
U.S. Cl.
CPC ...
C01B 3/503 (2013.01); B01D 53/02 (2013.01); B01D 53/047 (2013.01); B01D 53/228 (2013.01); B01D 53/229 (2013.01); B01D 69/08 (2013.01); B01D 71/16 (2013.01); B01D 71/64 (2013.01); B01D 71/68 (2013.01); C01B 3/50 (2013.01); C01B 3/508 (2013.01); B01D 2256/16 (2013.01); B01D 2257/102 (2013.01); B01D 2257/104 (2013.01); B01D 2257/502 (2013.01); B01D 2257/504 (2013.01); B01D 2257/702 (2013.01); C01B 2203/0227 (2013.01); C01B 2203/043 (2013.01); C01B 2203/0405 (2013.01); C01B 2203/1235 (2013.01); C01B 2203/146 (2013.01); Y02C 10/08 (2013.01); Y02C 10/10 (2013.01); Y02P 20/152 (2015.11);
Abstract

The process can be used in any hydrocarbon process in which it is desirable to recover hydrogen. The process can include catalytically reforming a hydrocarbon feed, a paraffin dehydrogenation to produce light olefins or a synthesis gas generating process. There is an effluent stream having hydrogen and hydrocarbons that is first sent to an adsorption zone to produce a pure hydrogen stream and a tail gas stream. The tail gas stream is then sent across a feed side of a membrane having the feed side and a permeate side. The membrane that is selected is selective for hydrogen over one or more C1-C6 hydrocarbons and light ends including CO, CO2, N2 and O2, and withdrawing from the permeate side a permeate stream enriched in hydrogen compared with a residue stream withdrawn from the feed side. The permeate stream is then recycled to be sent through the adsorption zone.


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