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:
Dec. 12, 2023

Filed:

Jan. 20, 2017
Applicant:

Trevi Systems Inc., Rohnert Park, CA (US);

Inventors:

Qiang Wei, Petaluma, CA (US);

Elliott Baker, Petaluma, CA (US);

John Webley, Petaluma, CA (US);

Gary Carmignani, Petaluma, CA (US);

Assignee:

Trevi Systems, Inc., Rohnert Park, CA (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01D 61/02 (2006.01); B01D 61/08 (2006.01); B01D 63/04 (2006.01); B01D 63/10 (2006.01); B01D 69/06 (2006.01); C02F 103/08 (2006.01); B01D 69/08 (2006.01); B01D 71/06 (2006.01); C02F 1/44 (2023.01);
U.S. Cl.
CPC ...
B01D 61/025 (2013.01); B01D 61/08 (2013.01); B01D 63/043 (2013.01); B01D 63/103 (2013.01); B01D 69/06 (2013.01); B01D 69/08 (2013.01); B01D 71/06 (2013.01); C02F 1/441 (2013.01); B01D 2313/04 (2013.01); B01D 2313/146 (2013.01); B01D 2313/24 (2013.01); C02F 2103/08 (2013.01);
Abstract

Membranes and filtration modules for producing a concentrated feed stream and a diluted feed stream during operation in a water purification or wastewater treatment system. Filtration modules are provided that include a semipermeable membrane having a first side and a second side, the first side configured to receive a first feed solution stream from a first feed solution source and the second side configured to receive a second feed solution stream from a second feed solution source. The semipermeable membrane may be configured to operate at a hydrostatic pressure on the second side of the membrane from about 1% to about 40% of the hydrostatic pressure on the first side of the membrane, and may in some cases exhibit a salt rejection of from about 60 percent to about 90 percent during operation.


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