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. 12, 2015

Filed:

Feb. 29, 2012
Applicants:

Bjoern Ungerer, Bad Schoenborn, DE;

Christoph Weingaertner, Gaualgesheim, DE;

Hans-peter Dornik, Oberramstadt, DE;

Inventors:

Bjoern Ungerer, Bad Schoenborn, DE;

Christoph Weingaertner, Gaualgesheim, DE;

Hans-Peter Dornik, Oberramstadt, DE;

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01D 1/06 (2006.01); C02F 1/04 (2006.01); B01D 61/02 (2006.01); B01D 1/28 (2006.01); C02F 1/44 (2006.01); B01D 3/14 (2006.01); C02F 101/38 (2006.01); C02F 103/18 (2006.01);
U.S. Cl.
CPC ...
C02F 1/048 (2013.01); B01D 1/06 (2013.01); B01D 1/28 (2013.01); B01D 61/022 (2013.01); C02F 1/441 (2013.01); C02F 2101/38 (2013.01); C02F 2103/18 (2013.01); B01D 2311/04 (2013.01); B01D 2311/25 (2013.01); B01D 3/145 (2013.01);
Abstract

Disclosed herein is a system comprising an evaporation unit comprising a first heat exchanger in fluid communication with a second heat exchanger; where the first heat exchanger is operative to heat an effluent stream comprising an amine solvent and/or amine byproducts and water and to discharge the effluent stream to the second heat exchanger; where the second heat exchanger is operative to convert the effluent stream into a distillate stream and a concentrate stream; and a reverse osmosis unit in fluid communication with the evaporation unit; where the reverse osmosis unit comprises a first reverse osmosis unit that is operative to receive the distillate stream and to separate water from byproducts of the amine solvent such that the water has a purity of greater than 95%, based on the weight of the distillate stream.


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