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:
Jun. 09, 2015

Filed:

Mar. 21, 2011
Applicants:

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

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

L. Don Tyler, Midland, 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);

L. Don Tyler, Midland, 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:
Assistant Examiner:
Int. Cl.
CPC ...
F25J 3/00 (2006.01); F25J 3/02 (2006.01);
U.S. Cl.
CPC ...
F25J 3/0209 (2013.01); F25J 2200/70 (2013.01); F25J 2200/74 (2013.01); F25J 2200/80 (2013.01); F25J 2205/02 (2013.01); F25J 2210/06 (2013.01); F25J 2235/60 (2013.01); F25J 2270/02 (2013.01); F25J 3/0233 (2013.01); F25J 3/0238 (2013.01); F25J 3/0242 (2013.01); F25J 2200/02 (2013.01); F25J 2200/76 (2013.01); F25J 2205/04 (2013.01); F25J 2240/02 (2013.01); F25J 2270/12 (2013.01); F25J 2270/60 (2013.01); F25J 2290/40 (2013.01);
Abstract

A process and an apparatus are disclosed for a compact processing assembly to recover C(or C) components and heavier hydrocarbon components from a hydrocarbon gas stream. The gas stream is cooled and divided into first and second streams. The first stream is further cooled, expanded to lower pressure, and supplied as a feed between first and second absorbing means. The second stream is expanded to lower pressure and supplied as bottom feed to the second absorbing means. A distillation vapor stream from the first absorbing means is heated, compressed to higher pressure, and divided into a volatile residue gas fraction and a compressed recycle stream. The compressed recycle stream is cooled, expanded to lower pressure, and supplied as top feed to the first absorbing means. A distillation liquid stream from the second absorbing means is heated in a heat and mass transfer means to strip out its volatile components.


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