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:
Jan. 16, 2018

Filed:

Apr. 01, 2008
Applicants:

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

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

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

Inventors:

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

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

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

Assignee:

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

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
F25J 3/00 (2006.01); F25J 3/02 (2006.01); C10L 3/10 (2006.01);
U.S. Cl.
CPC ...
F25J 3/0233 (2013.01); C10L 3/10 (2013.01); F25J 3/0214 (2013.01); F25J 3/0242 (2013.01); F25J 2200/02 (2013.01); F25J 2200/74 (2013.01); F25J 2200/78 (2013.01); F25J 2205/02 (2013.01); F25J 2205/04 (2013.01); F25J 2230/08 (2013.01); F25J 2230/60 (2013.01); F25J 2240/02 (2013.01); F25J 2240/40 (2013.01);
Abstract

A process and apparatus for the recovery of heavier hydrocarbons from a liquefied natural gas (LNG) stream is disclosed. The LNG feed stream is heated to vaporize at least part of it, then supplied to a fractionation column at a mid-column feed position. A vapor distillation stream is withdrawn from the fractionation column below the mid-column feed position and directed in heat exchange relation with the LNG feed stream, cooling the vapor distillation stream as it supplies at least part of the heating of the LNG feed stream. The vapor distillation stream is cooled sufficiently to condense at least a part of it, forming a condensed stream. At least a portion of the condensed stream is directed to the fractionation column as its top feed. The quantities and temperatures of the feeds to the column are effective to maintain the column overhead temperature at a temperature whereby the major portion of the desired components is recovered in the bottom liquid product from the column.


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