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. 03, 2018

Filed:

May. 03, 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); C10G 5/06 (2006.01);
U.S. Cl.
CPC ...
F25J 3/0238 (2013.01); C10G 5/06 (2013.01); F25J 3/0209 (2013.01); F25J 3/0219 (2013.01); F25J 3/0233 (2013.01); F25J 3/0242 (2013.01); C10G 2400/20 (2013.01); F25J 2200/02 (2013.01); F25J 2200/30 (2013.01); F25J 2200/70 (2013.01); F25J 2200/78 (2013.01); F25J 2200/80 (2013.01); F25J 2205/04 (2013.01); F25J 2210/06 (2013.01); F25J 2210/12 (2013.01); F25J 2240/02 (2013.01); F25J 2270/12 (2013.01); F25J 2270/60 (2013.01); F25J 2290/40 (2013.01); F25J 2290/42 (2013.01); Y02C 20/20 (2013.01);
Abstract

A process and an apparatus are disclosed for a compact processing assembly to recover ethane, ethylene, 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, heated, and its liquid fraction is supplied as a first top feed to an absorbing means. The second stream is expanded to lower pressure and supplied as a bottom feed to the absorbing means. A distillation vapor stream from the absorbing means is combined with the vapor fraction of the first stream, then cooled by the expanded first stream to form a condensed stream that is supplied as a second top feed to the absorbing means. A distillation liquid stream from the bottom of the absorbing means is heated in a heat and mass transfer means to strip out its volatile components.


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