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:
Mar. 24, 2020

Filed:

Jul. 08, 2016
Applicant:

Shell Oil Company, Houston, TX (US);

Inventors:

Johan Jan Barend Pek, Rijswijk, NL;

Karel Antonius Kusters, Rijswijk, NL;

Meta Jannetta Van Veghel, Rijswijk, NL;

Assignee:

SHELL OIL COMPANY, Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 3/02 (2006.01); F25J 1/02 (2006.01); F25J 1/00 (2006.01); F25J 3/06 (2006.01);
U.S. Cl.
CPC ...
F25J 3/0209 (2013.01); F25J 1/0022 (2013.01); F25J 1/0035 (2013.01); F25J 1/0042 (2013.01); F25J 1/0045 (2013.01); F25J 1/0052 (2013.01); F25J 1/0055 (2013.01); F25J 1/0205 (2013.01); F25J 1/0214 (2013.01); F25J 1/0216 (2013.01); F25J 1/0231 (2013.01); F25J 1/0237 (2013.01); F25J 1/0239 (2013.01); F25J 1/0255 (2013.01); F25J 1/0262 (2013.01); F25J 3/0233 (2013.01); F25J 3/0242 (2013.01); F25J 3/0247 (2013.01); F25J 3/061 (2013.01); F25J 3/0635 (2013.01); F25J 2200/02 (2013.01); F25J 2200/04 (2013.01); F25J 2200/38 (2013.01); F25J 2200/50 (2013.01); F25J 2200/72 (2013.01); F25J 2200/74 (2013.01); F25J 2200/94 (2013.01); F25J 2205/04 (2013.01); F25J 2210/06 (2013.01); F25J 2210/60 (2013.01); F25J 2215/02 (2013.01); F25J 2215/04 (2013.01); F25J 2220/62 (2013.01); F25J 2245/02 (2013.01); F25J 2260/20 (2013.01); F25J 2270/02 (2013.01); F25J 2270/04 (2013.01); F25J 2280/02 (2013.01);
Abstract

The present invention relates to a method of cooling and separating a hydrocarbon stream: (a) passing an hydrocarbon feed stream () through a first cooling and separation stage to provide a methane enriched vapour overhead stream () and a methane depleted liquid stream (); (b) passing the methane depleted liquid stream () to a fractionation column () to obtain a bottom condensate stream (), a top stream enriched in C1-C2 () and a midstream enriched in C3-C4 (), (c) cooling the upper part of the fractionation column () by a condenser (), (d) obtaining a split stream () from the methane enriched vapour overhead stream () and obtaining a cooled split stream (') by expansion-cooling the split stream (), (e) providing cooling duty to the top of the fractionation column () using the cooled split stream (′).


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