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. 13, 2018

Filed:

Jul. 22, 2013
Applicants:

Aquero Company, Llc, Eugene, OR (US);

1257 122 Alberta Ltd., Calgary, CA;

Inventors:

Timothy J. Webber, Calgary, CA;

T. Daniel Sikes, Eugene, OR (US);

C. Steven Sikes, Eugene, OR (US);

Assignees:

Aquero Company, LLC, Eugene, OR (US);

1257 122 Alberta Ltd., Calgary, CA;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 17/04 (2006.01); B01D 21/01 (2006.01); B03D 3/00 (2006.01); C02F 1/52 (2006.01); C02F 1/24 (2006.01); B03D 1/00 (2006.01); B01D 29/00 (2006.01); B03D 1/14 (2006.01); B01D 21/02 (2006.01); B03D 1/016 (2006.01); B03D 3/02 (2006.01); B03D 3/06 (2006.01); C02F 1/66 (2006.01); C02F 1/56 (2006.01); C02F 9/00 (2006.01); C02F 1/00 (2006.01); B01D 35/00 (2006.01); B01D 37/00 (2006.01); C02F 1/40 (2006.01); B01D 21/00 (2006.01); C02F 101/32 (2006.01); C02F 103/10 (2006.01); C02F 103/36 (2006.01);
U.S. Cl.
CPC ...
B03D 1/1443 (2013.01); B01D 17/047 (2013.01); B01D 21/01 (2013.01); B01D 21/02 (2013.01); B01D 25/04 (2013.01); B01D 29/0018 (2013.01); B03D 1/016 (2013.01); B03D 3/02 (2013.01); B03D 3/06 (2013.01); C02F 1/24 (2013.01); C02F 1/5281 (2013.01); C02F 1/56 (2013.01); C02F 1/66 (2013.01); C02F 9/00 (2013.01); C02F 2101/325 (2013.01); C02F 2103/10 (2013.01); C02F 2103/365 (2013.01); C02F 2201/003 (2013.01);
Abstract

A chemical treatment process and separation module are described for removal of soluble organic compounds and suspended or emulsified oils and/or solids from produced waters that accompany operations for oil and gas recovery. The process occurs in its entirety within an interval of several minutes. The solubility of organic compounds is first reduced, in an optional step, by pH reduction, followed by treatment with coagulants and flocculants, the latter in conjunction with microbubble flotation. The organic compounds that are rendered insoluble, along with other oily solids, are captured in the floe created by the coagulant and flocculant treatment, and simultaneously made buoyant by the concurrent addition of microbubbles. The water and floe is passed over an array of sloped strainers that separates and diverts the floe from the effluent water, which contains significantly reduced soluble organic content. The separated stream of oily solids can be dewatered for disposal as waste.


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