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:
May. 05, 2015

Filed:

Dec. 28, 2010
Applicants:

Michael C. Pierce, Erie, CO (US);

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

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

Inventors:

Michael C. Pierce, Erie, CO (US);

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

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

Assignee:

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

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 3/02 (2006.01);
U.S. Cl.
CPC ...
F25J 3/0209 (2013.01); F25J 3/0219 (2013.01); F25J 3/0233 (2013.01); F25J 3/0238 (2013.01); F25J 2200/04 (2013.01); F25J 2200/70 (2013.01); F25J 2200/72 (2013.01); F25J 2200/74 (2013.01); F25J 2200/78 (2013.01); F25J 2205/04 (2013.01); F25J 2210/12 (2013.01); F25J 2230/30 (2013.01); F25J 2235/60 (2013.01); F25J 2240/02 (2013.01); F25J 2245/02 (2013.01); F25J 2270/12 (2013.01); F25J 2270/60 (2013.01);
Abstract

A process and an apparatus are disclosed for recovering ethane, ethylene, and heavier hydrocarbon components from a hydrocarbon gas stream. The stream is cooled, expanded to lower pressure, and supplied to a first fractionation tower at a mid-column feed position. A distillation liquid stream is withdrawn from the first fractionation tower below the feed position of the expanded stream, heated, and directed into a second fractionation tower that produces an overhead vapor stream and a bottom liquid stream. The overhead vapor stream is cooled to condense it, with a portion of the condensed stream directed to the second fractionation tower as its top feed and the remainder directed to the first fractionation tower at a lower column feed position. The bottom liquid stream from the second fractionation tower is cooled and directed to the first fractionation tower as its top feed.


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