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:
Aug. 24, 2021

Filed:

Jun. 01, 2018
Applicant:

Linde Aktiengesellschaft, Munich, DE;

Inventor:

Dimitri Golubev, Geretsried, DE;

Assignee:
Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
F25J 3/04 (2006.01);
U.S. Cl.
CPC ...
F25J 3/04915 (2013.01); F25J 3/0406 (2013.01); F25J 3/0409 (2013.01); F25J 3/04024 (2013.01); F25J 3/04084 (2013.01); F25J 3/04109 (2013.01); F25J 3/04175 (2013.01); F25J 3/04296 (2013.01); F25J 3/04351 (2013.01); F25J 3/04381 (2013.01); F25J 3/04393 (2013.01); F25J 3/04412 (2013.01); F25J 3/04666 (2013.01); F25J 3/04678 (2013.01); F25J 3/04727 (2013.01); F25J 2200/92 (2013.01); F25J 2215/54 (2013.01); F25J 2230/20 (2013.01); F25J 2240/04 (2013.01); F25J 2240/46 (2013.01);
Abstract

The invention proposes a process and an air separation plant comprising a rectification column system comprising a high-pressure column, a low-pressure column, a main heat exchanger, and a main air compressor. The total air supplied to the rectification column system is compressed in the main air compressor to a first pressure level. The high-pressure column is operated at a second pressure level, at least 3 bar below the first pressure level. A gaseous, nitrogen-rich fluid is removed from the high-pressure column and warmed up in the gaseous state without prior liquefaction. A first partial quantity of the gaseous, nitrogen-rich fluid is warmed to a first temperature level of −150 to −100° C., supplied at this first temperature level to a booster and compressed further to a third pressure level. The first partial quantity is then warmed to a second temperature level and discharged from the air separation plant.


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