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. 29, 2018

Filed:

Mar. 31, 2011
Applicants:

Siew-mung Patricia Ho, Como, AU;

Derek William Hodges, Dianella, AU;

Christiane Kerber, Poecking, DE;

Manfred Steinbauer, Raisting, DE;

Markus Hammerdinger, Tacherting, DE;

Inventors:

Siew-Mung Patricia Ho, Como, AU;

Derek William Hodges, Dianella, AU;

Christiane Kerber, Poecking, DE;

Manfred Steinbauer, Raisting, DE;

Markus Hammerdinger, Tacherting, DE;

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
F25J 1/00 (2006.01); F28F 9/00 (2006.01); F25J 1/02 (2006.01); F28D 7/00 (2006.01); F28D 7/02 (2006.01); F28F 27/02 (2006.01); F25J 5/00 (2006.01);
U.S. Cl.
CPC ...
F28F 9/001 (2013.01); F25J 1/0022 (2013.01); F25J 1/0055 (2013.01); F25J 1/0244 (2013.01); F25J 1/0262 (2013.01); F25J 1/0267 (2013.01); F25J 5/002 (2013.01); F28D 7/0066 (2013.01); F28D 7/024 (2013.01); F28F 27/02 (2013.01); F25J 2210/06 (2013.01); F25J 2220/62 (2013.01); F25J 2290/32 (2013.01);
Abstract

A process for cooling a tube side stream in a main heat exchanger is described. The process comprises: a) supplying a first mass flow of a tube side stream to a first zone of individual tubes in the tube bundle; b) supplying a second mass flow of the tube side stream to a second zone of individual tubes in the tube bundle, the second zone being offset from the first zone; c) supplying a refrigerant stream on the shell side for cooling the first and second mass flows; d) removing the evaporated refrigerant stream from the warm end of the main heat exchanger; and, e) adjusting the first mass flow of the tube side stream relative to the second mass flow of the tube side stream to maximise the temperature of the removed evaporated refrigerant stream.


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