Wet air oxidation process using recycled copper catalyst

1. A catalytic wet oxidation system comprising:

a wet oxidation unit;

a source of an aqueous mixture comprising at least one undesirable constituent fluidly connected to the wet oxidation unit;

a source of copper catalyst soluble in the aqueous mixture fluidly connected to the aqueous mixture, the aqueous mixture desired to have a solubility pH at which the catalyst is substantially soluble, the solubility pH being below about 4 or above about 12;

a first pH sensor configured to detect a pH level of the aqueous mixture;

a pH controller in communication with the first pH sensor configured to generate a first control signal to adjust the pH level of the aqueous mixture to the solubility pH of below about 4 or above about 12 for treatment of the at least one undesirable constituent in the wet oxidation reactor in response to the first pH sensor registering a pH level above about 4 or below about 12; and

a second sensor in communication with the controller, the second sensor configured to detect a pH level of an oxidized aqueous mixture formed in the wet oxidation unit, the pH controller configured to generate a second control signal to adjust the pH level of the oxidized aqueous mixture to a second range at which the catalyst is substantially insoluble downstream of the wet oxidation unit.

2. The system of claim 1 , further comprising:

a separator in direct fluid communication downstream of the wet oxidation unit and downstream of the pH controller and configured to precipitate, solely by the adjustment of the pH level of the oxidized aqueous mixture at least a portion of the catalyst,

the pH controller further configured to generate the second control signal to adjust a pH level of the oxidized aqueous mixture in the separator to within a range from about 6 to about 12;

a recirculation line fluidly connected to an outlet of the separator and to an inlet of the at least one of the source of catalyst and an inlet to the wet oxidation system; and

a source of alkali compound positioned downstream of and fluidly connected to at least one of the separator and the wet oxidation unit and configured to deliver alkali compound to at least one of the separator and the wet oxidation unit.

3. The system of claim 2 , further comprising a source of an acid positioned downstream of and fluidly connected to at least one of the separator and the wet oxidation unit.

4. The system of claim 1 , wherein the solubility pH is below about 2 and above about 13.

5. The system of claim 2 , further comprising a clarifier upstream of and fluidly connected to the separator configured to clarify the oxidized aqueous mixture, thereby forming a reject.

6. The system of claim 5 , further comprising a conduit configured to transport at least a portion of the reject to a location in the system upstream of and in fluid communication with the wet oxidation unit and to contact the reject with the aqueous mixture comprising at least one undesirable constituent.

7. The system of claim 2 , wherein substantially all of the catalyst is recovered.

8. The system of claim 2 , further including a source of a pH adjuster fluidly connected with the recirculation line.

9. The system of claim 8 , further comprising a third pH sensor in communication with the pH controller, configured to detect a pH level of an aqueous mixture in the recirculation line, the pH controller further configured to generate a control signal to adjust a pH level of the aqueous mixture in the recirculation line in response to the third pH sensor registering a pH level outside a predetermined pH solubility range for the catalyst.