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. 28, 2019

Filed:

Mar. 17, 2016
Applicant:

Cameron Solutions, Inc., Houston, TX (US);

Inventors:

Wenjun Liu, Wayne, PA (US);

Luis Eduardo Caires-Fernandez, Cypress, TX (US);

Daniel E. Shannon, Houston, TX (US);

Assignee:

CAMERON SOLUTIONS, INC., Houston, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C02F 1/24 (2006.01); B01D 17/035 (2006.01); B01D 17/02 (2006.01); B01D 17/04 (2006.01); C02F 1/00 (2006.01); B01D 17/12 (2006.01); B03D 1/02 (2006.01); B03D 1/04 (2006.01); B03D 1/14 (2006.01); C02F 1/20 (2006.01); C02F 1/40 (2006.01); C02F 1/38 (2006.01); C02F 101/32 (2006.01);
U.S. Cl.
CPC ...
C02F 1/24 (2013.01); B01D 17/0205 (2013.01); B01D 17/0217 (2013.01); B01D 17/045 (2013.01); B01D 17/12 (2013.01); B03D 1/028 (2013.01); B03D 1/04 (2013.01); B03D 1/1431 (2013.01); C02F 1/008 (2013.01); C02F 1/20 (2013.01); C02F 1/40 (2013.01); C02F 1/38 (2013.01); C02F 2101/32 (2013.01); C02F 2209/03 (2013.01); C02F 2301/08 (2013.01);
Abstract

A method to remove oil from an oily water stream includes the step of pressure controlling a release of dissolved gases from the stream as the stream passes through two or more stages of gas flotation treatment. The operating pressure of the first stage of flotation treatment is purposefully reduced relative to that of an upstream unit so that a certain controlled percent volume of dissolved gases is released. The operating pressure of the second stage of flotation treatment is then purposefully reduced relative to that of the first stage so that another controlled percent volume of dissolved gases is released. Any subsequent flotation treatment stage is at a lower operating pressure than that of the previous stage so that the subsequent treatment stage releases a controlled percent volume of dissolved gases. By controlling the operating pressure in this way, overall separation performance is improved.


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