Non-scaling wet air oxidation system
View Patent ↗There is provided a system and a method for regenerating a material that reduce the incidence of scaling due to scale forming contaminants. The method may include reducing a temperature of a treated material exiting a wet air oxidation unit in a scale reducing heat exchanger prior to delivery of the treated material to a second heat exchanger which heats a source waste material comprising a scale forming contaminant therein with heat from the first treated material to form a heated waste material comprising the scale forming contaminant.
1. A treatment system comprising:
a source waste material comprising spent carbon material and a scale forming contaminant;
a wet air oxidation unit for receiving a heated waste material comprising the spent carbon material and the scale forming contaminant and discharging a first treated material comprising a regenerated carbon material;
a scale reducing heat exchanger in fluid communication with the wet air oxidation unit for receiving the first treated material from the wet air oxidation unit and for discharging a second treated material comprising regenerated carbon and having a reduced temperature relative to the first treated material; and
a second heat exchanger in fluid communication with the scale reducing heat exchanger for receiving the second treated material, the second heat exchanger further arranged to receive the source waste material comprising the spent carbon material and the scale forming contaminant and discharge the heated waste material for delivery to the wet air oxidation unit;
wherein the heated waste material comprises an increased temperature relative to the source waste material due to heat exchange of the source waste material with the second treated material; and
wherein the second treated material comprises a temperature less than a solubility temperature limit of the scale forming contaminant at a given concentration of the scale forming contaminant.
2. The system of claim 1 , wherein the scale reducing heat exchanger is effective to reduce a temperature of the first treated material such that the second treated material comprises a temperature of from about 100° C. to about 185° C.
3. The system of claim 1 , wherein the scale forming contaminant comprises a member selected from the group consisting of aluminum, calcium, carbonate, iron, magnesium, phosphorus, sulfate, and combinations thereof.
4. The system of claim 3 , wherein the scale forming contaminant comprises calcium.
5. The system of claim 4 , wherein the scale forming contaminant comprises calcium sulfate.
6. The system of claim 1 , wherein the second heat exchanger comprises a shell and tube heat exchanger.
7. The system of claim 1 , wherein the system further comprises a fluid source in fluid communication with the scale reducing heat exchanger to deliver an amount of a fluid to the scale reducing heat exchanger effective to control an extent of temperature reduction for the first treated material.
8. The system of claim 7 , further comprising a fluid flow controller in communication with the fluid source and effective to regulate the amount of the fluid delivered to the scale reducing heat exchanger.
9. The system of claim 1 , wherein the source waste material is from a powdered activated carbon treatment (PACT) system or a granular activated carbon (GAC) system.