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. 01, 2020

Filed:

Jul. 26, 2018
Applicants:

L'air Liquide, Société Anonyme Pour L'etude ET L'exploitation Des Procédés Georges Claude, Paris, FR;

American Air Liquide, Inc., Fremont, CA (US);

Inventors:

Jan Mante, Muenster, DE;

Vasuhi Rasanayagam, Newark, DE (US);

Midhun Joy, Bear, DE (US);

Rovshan Mahmudov, Newark, DE (US);

Siavash Isazadeh, Cambridge, MA (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C02F 1/78 (2006.01); C02F 1/72 (2006.01); A01N 59/00 (2006.01); A61L 2/18 (2006.01); B01F 3/08 (2006.01); B01F 3/20 (2006.01); B01F 5/10 (2006.01); B01F 15/00 (2006.01); C01B 13/10 (2006.01); C02F 1/32 (2006.01); B01D 53/22 (2006.01); A61L 2/20 (2006.01);
U.S. Cl.
CPC ...
C02F 1/78 (2013.01); A01N 59/00 (2013.01); A61L 2/183 (2013.01); B01F 3/0876 (2013.01); B01F 3/20 (2013.01); B01F 5/102 (2013.01); B01F 15/00162 (2013.01); C01B 13/10 (2013.01); C02F 1/725 (2013.01); A61L 2/202 (2013.01); B01D 53/22 (2013.01); B01F 2215/008 (2013.01); C02F 1/32 (2013.01); C02F 2201/782 (2013.01); C02F 2201/784 (2013.01); C02F 2303/04 (2013.01);
Abstract

Disclosed are systems for continuous production of ozone strong water, the systems comprising an injection device that injects an acidification agent into a pressurized feed liquid, a diffuser device that injects ozone into a body of the acidic pressurized feed water, and injection nozzles each controlled by a valve that adjust a flow rate of the ozone strong water discharged from a dissolution column to match a flow rate of the acidic pressurized feed water fed to the dissolution column, thereby maintaining a start-up mode in an upper portion of the dissolution column that favors a high efficiency of ozone mass transfer and a steady-state mode in a lower portion of the dissolution column that favors a high dissolved ozone concentration coexistent in the body of the acidic pressurized liquid, wherein a concentration gradient of dissolved ozone is formed along a height of the body of the acidic pressurized liquid.


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