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:
Mar. 17, 2015

Filed:

Apr. 23, 2013
Applicant:

Aquatech International Corporation, Canonsburg, PA (US);

Inventor:

Ravi Chidambaran, Canonsburg, PA (US);

Assignee:

Aquatech International Corporation, Canonsburg, PA (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01J 49/00 (2006.01); C02F 1/42 (2006.01); B01D 15/00 (2006.01); B01J 39/00 (2006.01); B01D 37/00 (2006.01); C02F 1/00 (2006.01); B01D 61/00 (2006.01); A61M 1/16 (2006.01); C02F 9/00 (2006.01); C02F 1/44 (2006.01); B01D 61/58 (2006.01); B01D 65/02 (2006.01); B01D 65/06 (2006.01); C02F 1/48 (2006.01); B01D 1/00 (2006.01); B03D 1/00 (2006.01); C02F 1/24 (2006.01); B01D 24/00 (2006.01); B01D 25/00 (2006.01); B01D 27/00 (2006.01); B01D 29/00 (2006.01); B01D 33/00 (2006.01); B01D 36/02 (2006.01); B01D 61/02 (2006.01); B01D 61/14 (2006.01); C02F 1/46 (2006.01); C02F 103/08 (2006.01);
U.S. Cl.
CPC ...
C02F 1/444 (2013.01); B01D 61/58 (2013.01); B01D 65/02 (2013.01); B01D 65/06 (2013.01); C02F 1/48 (2013.01); C02F 9/00 (2013.01); B01D 61/025 (2013.01); B01D 61/145 (2013.01); C02F 1/24 (2013.01); C02F 1/42 (2013.01); C02F 1/441 (2013.01); C02F 1/46 (2013.01); C02F 2103/08 (2013.01); C02F 2303/10 (2013.01); C02F 2303/16 (2013.01);
Abstract

We provide a system and method for reverse osmosis treatment of water, including seawater and brackish water. Methods and systems of embodiments of the invention may include, for example, ultrafiltration followed by biofoulant removal, both of which precede reverse osmosis. In preferred embodiments the system is run at a low flux. For example, a flux of 6-8 GFD may be used with seawater. Additional embodiments may provide the above process in conjunction with a reverse-osmosis membrane cleaning system. The membrane cleaning system is a 'clean in place' system that includes use of the natural pressure differential in the reverse osmosis system to remove biofoulants and their precursors.


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