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.

Patent No.:

US 9115006 B1

PDF
Full Text
Expired
Date of Patent:
Aug. 25, 2015

Filed:

Jan. 12, 2011
Applicants:

Jason Gilmour, Huntington Beach, CA (US);

William A. Greene, Long Beach, CA (US);

Inventors:

Jason Gilmour, Huntington Beach, CA (US);

William A. Greene, Long Beach, CA (US);

Assignee:

Spintek Filtration, Inc., Los Alamitos, CA (US);

Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01D 1/00 (2006.01); B03B 5/60 (2006.01); B03D 1/00 (2006.01); C02F 1/24 (2006.01); B01F 3/04 (2006.01); B01F 5/04 (2006.01); B01F 5/06 (2006.01); B01F 15/00 (2006.01); B03D 1/02 (2006.01); B03D 1/04 (2006.01); B03D 1/24 (2006.01); B03D 1/14 (2006.01);
U.S. Cl.
CPC ...
C02F 1/24 (2013.01); B01F 3/04503 (2013.01); B01F 5/0451 (2013.01); B01F 5/0465 (2013.01); B01F 5/0653 (2013.01); B01F 5/0657 (2013.01); B01F 15/00136 (2013.01); B01F 15/00162 (2013.01); B01F 15/00357 (2013.01); B03D 1/028 (2013.01); B03D 1/04 (2013.01); B03D 1/1475 (2013.01); B03D 1/247 (2013.01); B01F 2215/0431 (2013.01); B01F 2215/0468 (2013.01); B03D 1/245 (2013.01); C02F 2209/005 (2013.01); C02F 2209/38 (2013.01);
Abstract

A system is provided for introducing gas bubbles (usually air bubbles) into a liquid stream to coalesce material such as unwanted bits, or particles, of hydrocarbons that lie in the liquid stream along with wanted dissolved bits of metal, for removal of the hydrocarbons. The system is constructed to produce a large number of bubbles of an optimum range such as 60 to 100 μm which best coalesce the hydrocarbons. A controller receives the outputs of sensors such as pressure and flow rate sensors (P, F) and uses them to make changes in other parameters such as the pressure of air introduced into the liquid stream and the pressure in a third conduit of the liquid-bubble stream.


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