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:
Oct. 04, 2016

Filed:

Apr. 03, 2013
Applicant:

Linde Aktiengesellschaft, Munich, DE;

Inventor:

Dimitri Goloubev, Munich, DE;

Assignee:
Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
F02C 3/00 (2006.01); F25J 3/04 (2006.01);
U.S. Cl.
CPC ...
F02C 3/00 (2013.01); F25J 3/0406 (2013.01); F25J 3/04018 (2013.01); F25J 3/04181 (2013.01); F25J 3/04224 (2013.01); F25J 3/04254 (2013.01); F25J 3/04303 (2013.01); F25J 3/04309 (2013.01); F25J 3/04363 (2013.01); F25J 3/04393 (2013.01); F25J 3/04496 (2013.01); F25J 3/04509 (2013.01); F25J 3/04533 (2013.01); F25J 3/04545 (2013.01); F25J 3/04581 (2013.01); F25J 3/04618 (2013.01); F25J 3/04836 (2013.01); F25J 2210/06 (2013.01); F25J 2210/50 (2013.01); F25J 2230/04 (2013.01); F25J 2230/06 (2013.01); F25J 2240/70 (2013.01); F25J 2245/50 (2013.01); Y02E 20/16 (2013.01);
Abstract

The method and the apparatus described are used for generating electrical energy in a combined system comprising a power plant and a low-temperature air separation unit. A feed air stream is compressed in a main air compressor, cooled, and introduced into a distillation column system having a high-pressure column and a low-pressure column. A first oxygen-enriched stream from the distillation column system is introduced into the power plant. In a first operating mode, cryogenic liquid from the distillation column system is introduced into a liquid tank and is stored there at least in part. In a second operating mode, stored cryogenic liquid is removed from the liquid tank and introduced into the distillation column system. A second process fluid from the distillation column system is heated and then actively depressurized in a hot expansion turbine. In addition, in the second operating mode, a nitrogen-enriched product stream from the high-pressure column is also heated to a high temperature and then depressurized in the hot expansion turbine.


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