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:
Jul. 07, 2015

Filed:

Jan. 09, 2012
Applicant:

Francois Cansell, Pessac, FR;

Inventor:

Francois Cansell, Pessac, FR;

Assignee:

INNOVEX, , FR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
A62D 3/38 (2007.01); C02F 1/72 (2006.01); C02F 11/08 (2006.01); B01J 19/24 (2006.01); C02F 11/06 (2006.01); C02F 101/30 (2006.01); C02F 103/32 (2006.01); C02F 103/34 (2006.01);
U.S. Cl.
CPC ...
C02F 1/72 (2013.01); C02F 11/086 (2013.01); C02F 2101/30 (2013.01); C02F 2103/32 (2013.01); C02F 2103/34 (2013.01); C02F 2209/001 (2013.01); C02F 2209/08 (2013.01); C02F 2209/29 (2013.01); C02F 2301/066 (2013.01); C02F 2303/08 (2013.01); C02F 1/727 (2013.01); C02F 2209/05 (2013.01); B01J 19/2415 (2013.01); C02F 11/06 (2013.01);
Abstract

Hydrothermal oxidation of organic compounds, optionally with oxidizable inorganic compounds, is contained in an aqueous effluent. The aqueous effluent is injected within a tubular reactor and brought to supercritical pressure, and temperature is increased to a supercritical temperature, without any intermediate decrease in temperature, by introducing sufficient amounts of oxidizing agent within the tubular for totally oxidizing the organic compounds, and optionally for partly oxidizing oxidizable inorganic compounds. The oxidizing agent is introduced in a fractionated way in several points increasingly located downstream, and the composition and/or the concentration of the organic compounds and/or oxidizable organic compounds within the effluent to be treated varies over time. Further, upstream from the tubular reactor where oxidation is carried out, the effluent's total chemical oxygen demand of the effluent to be treated is measured and monitored at more than 120 grams/liter (g/L) and less than 250 g/L prior to injecting the tubular reactor.


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