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:
Nov. 01, 2022

Filed:

May. 10, 2013
Applicants:

1304338 Alberta Ltd, Edmonton, CA;

1304342 Alberta Ltd, Edmonton, CA;

Inventors:

Jose Lourenco, Edmonton, CA;

MacKenzie Millar, Edmonton, CA;

Assignees:

1304338 ALBERTA LTD, Edmonton, CA;

1304342 ALBERTA LTD, Edmonton, CA;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 3/02 (2006.01); F25J 1/00 (2006.01); C01B 3/50 (2006.01); C10G 5/06 (2006.01); F25J 3/06 (2006.01);
U.S. Cl.
CPC ...
F25J 1/0022 (2013.01); C01B 3/506 (2013.01); C10G 5/06 (2013.01); F25J 3/0219 (2013.01); F25J 3/0233 (2013.01); F25J 3/0238 (2013.01); F25J 3/0242 (2013.01); F25J 3/0252 (2013.01); F25J 3/062 (2013.01); F25J 3/064 (2013.01); F25J 3/0635 (2013.01); F25J 3/0655 (2013.01); C01B 2203/046 (2013.01); F25J 2200/02 (2013.01); F25J 2205/02 (2013.01); F25J 2205/30 (2013.01); F25J 2210/04 (2013.01); F25J 2210/12 (2013.01); F25J 2210/62 (2013.01); F25J 2215/62 (2013.01); F25J 2270/904 (2013.01);
Abstract

A method to recover olefins and Cfractions from refineries gas streams. The traditional recovery methods employed at refineries are absorption with solvents and cryogenic technology using compression and expansion aided by external refrigeration systems. In contrast to known methods, there is provided first a pre-cooling heat exchanger on a feed line feeding the gas stream to a in-line mixer, secondly by injecting and mixing a stream of LNG to condense the Cfractions upstream of the fractionator. The temperature of the gas stream entering the fractionator is monitored downstream of the in-line mixer. A LNG stream is temperature controlled to flow through the injection inlet and mix with the feed gas at a temperature which results in the condensation of the Cfractions before entering the fractionator. A LNG reflux stream is temperature controlled to maintain fractionator overhead temperature. The fractionator bottoms temperature is controlled by a circulating reboiler stream.


Find Patent Forward Citations

Loading…