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. 10, 2018

Filed:

Jun. 02, 2010
Applicants:

Andrew F. Johnke, Beresford, SD (US);

W. Larry Lewis, Houston, TX (US);

John D. Wilkinson, Midland, TX (US);

Joe T. Lynch, Midland, TX (US);

Hank M. Hudson, Midland, TX (US);

Kyle T. Cuellar, Katy, TX (US);

Inventors:

Andrew F. Johnke, Beresford, SD (US);

W. Larry Lewis, Houston, TX (US);

John D. Wilkinson, Midland, TX (US);

Joe T. Lynch, Midland, TX (US);

Hank M. Hudson, Midland, TX (US);

Kyle T. Cuellar, Katy, TX (US);

Assignees:

Ortloff Engineers, Ltd., Midland, TX (US);

S.M.E. Products LP, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 3/02 (2006.01);
U.S. Cl.
CPC ...
F25J 3/0209 (2013.01); F25J 3/0233 (2013.01); F25J 3/0266 (2013.01); F25J 3/0295 (2013.01); F25J 2200/02 (2013.01); F25J 2200/50 (2013.01); F25J 2200/74 (2013.01); F25J 2200/80 (2013.01); F25J 2205/04 (2013.01); F25J 2215/04 (2013.01); F25J 2235/80 (2013.01); F25J 2240/02 (2013.01); F25J 2240/40 (2013.01); F25J 2260/20 (2013.01); F25J 2260/80 (2013.01); F25J 2270/02 (2013.01); F25J 2270/90 (2013.01); F25J 2290/40 (2013.01); Y02C 10/12 (2013.01);
Abstract

A process and an apparatus are disclosed for a compact processing assembly to remove carbon dioxide from a hydrocarbon gas stream. The gas stream is cooled, expanded to intermediate pressure, and fed to the top of a mass transfer means. A distillation liquid stream from the mass transfer means is heated in a first heat and mass transfer means to strip out its volatile components and form a bottom liquid product. A distillation vapor stream from the mass transfer means is combined with any vapor in the expanded cooled gas stream, and the combined vapor stream is cooled in a second heat and mass transfer means to partially condense it, forming a condensed stream that is fed to the top of the mass transfer means. A portion of the bottom liquid product is subcooled, expanded to lower pressure, and used to cool the combined vapor stream.


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