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:
Nov. 05, 2019

Filed:

Jun. 29, 2016
Applicant:

Linde Aktiengesellschaft, München, DE;

Inventors:

Tuat Pham Duc, Penzberg, DE;

Paul Kuhn, Baierbrunn, DE;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 3/50 (2006.01); F25J 3/02 (2006.01); C01B 3/56 (2006.01); B01D 53/00 (2006.01); B01D 53/047 (2006.01); B01D 53/14 (2006.01); B01D 53/18 (2006.01); C01B 3/52 (2006.01);
U.S. Cl.
CPC ...
C01B 3/56 (2013.01); B01D 53/002 (2013.01); B01D 53/047 (2013.01); B01D 53/1431 (2013.01); B01D 53/18 (2013.01); C01B 3/506 (2013.01); C01B 3/52 (2013.01); F25J 3/0219 (2013.01); F25J 3/0238 (2013.01); F25J 3/0252 (2013.01); C01B 2203/042 (2013.01); C01B 2203/043 (2013.01); C01B 2203/048 (2013.01); C01B 2203/0415 (2013.01); C01B 2203/147 (2013.01); F25J 2200/70 (2013.01); F25J 2205/02 (2013.01); F25J 2205/04 (2013.01); F25J 2205/30 (2013.01); F25J 2205/40 (2013.01); F25J 2205/60 (2013.01); F25J 2210/12 (2013.01); F25J 2215/62 (2013.01); F25J 2230/08 (2013.01); F25J 2230/60 (2013.01); F25J 2245/02 (2013.01); F25J 2270/02 (2013.01);
Abstract

To obtain hydrogen from a gaseous C2minus feed, it is cooled from a first to a second temperature level at a first pressure level forming one or more condensates. A gaseous remainder is cooled to a third temperature level and subjected to a counterflow absorption at the first pressure level, obtaining a top gas rich in hydrogen and methane and a sump liquid. The former is heated and subjected to pressure swing adsorption at the first pressure level, forming a product stream rich in hydrogen and depleted in or free from methane. The condensate(s) and/or the sump liquid is/are expanded to and fed into a low pressure demethanizer at the second pressure level. The counterflow absorption is carried out using fluid taken from the demethanizer at the second pressure level, compressed in gaseous form to the first pressure level and cooled to the third temperature level.


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