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:
Mar. 19, 2019

Filed:

Nov. 03, 2015
Applicant:

Shell Oil Company, Houston, TX (US);

Inventors:

Gerald Sprachmann, Amsterdam, NL;

Gerardus Antonius Franciscus Van Mossel, Amsterdam, NL;

Hendrik Dathe, Amsterdam, NL;

Tobias Proell, Vienna, AT;

Gerhard Schoeny, Vienna, AT;

Assignee:

SHELL OIL COMPANY, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/08 (2006.01); B01D 53/62 (2006.01); B01D 53/12 (2006.01); B01J 20/28 (2006.01); B01J 20/34 (2006.01); B01J 20/22 (2006.01);
U.S. Cl.
CPC ...
B01D 53/12 (2013.01); B01J 20/22 (2013.01); B01J 20/28004 (2013.01); B01J 20/28011 (2013.01); B01J 20/28061 (2013.01); B01J 20/28064 (2013.01); B01J 20/28073 (2013.01); B01J 20/28076 (2013.01); B01J 20/3425 (2013.01); B01J 20/3466 (2013.01); B01J 20/3483 (2013.01); B01D 2253/202 (2013.01); B01D 2257/504 (2013.01); B01D 2259/402 (2013.01); B01D 2259/40086 (2013.01); B01D 2259/40096 (2013.01); B01D 2259/65 (2013.01);
Abstract

The present invention relates to a process for capturing carbon dioxide from a gas stream. The gas stream is contacted with solid adsorbent particles in an adsorption zone. The adsorption zone has at least two beds of fluidized solid adsorbent particles, and the solid adsorbent particles are flowing downwards from bed to bed. The solid adsorbent particles comprise 15 to 75 weight % of organic amine compounds. The gas stream entering the adsorption zone has a dew point which is at least 5° C. below the forward flow temperature of the coolest cooling medium in the adsorption zone. Carbon dioxide enriched solid adsorbent particles are heated, and then regenerated. The desorption zone has at least two beds of fluidized solid adsorbent particles, and the stripping gas is steam. The regenerated particles are cooled and recycled to the adsorption zone.


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