Method for treatment of process waters

1. A method for treating water, comprising:

contacting a first effluent comprising water, one or more thermally destructible contaminants, and one or more thermally indestructible contaminants with steam, to provide a second effluent comprising the steam and at least a portion of the one or more thermally indestructible contaminants and an intermediate comprising the water and at least a portion of the one or more thermally destructible contaminants;

treating the second effluent within an acid recovery unit;

contacting the intermediate with one or more oxidants to provide a third effluent comprising the one or more oxidants and at least a portion of the one or more thermally destructible contaminants and a fourth effluent comprising water; and

destructing the thermally destructible contaminants present in the third effluent using one or more combustion processes.

2. The method of claim 1 , wherein the combustion process is a hydrocarbon gasification process.

3. The method of claim 1 , wherein the one or more oxidants comprise air, oxygen, oxygen-enriched air, or any combination thereof.

4. The method of claim 1 , wherein the pressure of the steam ranges from about 200 kPa to about 1,130 kPa.

5. The method of claim 2 , wherein the acid recovery unit is an acid gas unit within a hydrocarbon gasification process.

6. The method of claim 1 , wherein the first effluent comprises a mixture of contact and non-contact cooling water.

7. The method of claim 1 , wherein a weight ratio of the steam-to-first effluent ranges from about 1:1 to about 20:1.

8. The method of claim 1 , wherein the concentration of the one or more oxidants in the intermediate is about 0.1% wt to about 5.0% wt.

9. The method of claim 1 , further comprising:

gasifying a feedstock comprising a polymer and coal to produce a raw syngas comprising the one or more thermally destructible contaminants, wherein the polymer comprises polyethylene, polypropylene, polystyrene, polyethylene terephthalate (PET), or any combination thereof, and

cooling the raw syngas by directly contacting the raw syngas with water to provide a cooled syngas and the first effluent.

10. The method of claim 1 , wherein the thermally indestructible contaminants comprise hydrogen chloride, carbonyl sulfide, or a combination thereof.

11. The method of claim 1 , wherein the thermally destructible contaminants comprise ammonia, and wherein the first effluent has an ammonia concentration of about 500 ppm to about 3 wt %.

12. A method for treating water, comprising:

gasifying a hydrocarbon using one or more gasifiers to provide a raw syngas comprising one or more thermally destructible contaminants, and one or more thermally indestructible contaminants at an elevated temperature;

cooling the raw syngas using contact and non-contact cooling to provide a cooled syngas and a first effluent comprising water, one or more thermally indestructible contaminants, and one or more thermally destructible contaminants;

contacting the first effluent with steam to provide a second effluent comprising the steam and at least a portion of the one or more thermally indestructible contaminants and an intermediate comprising the water and at least a portion of the one or more thermally destructible contaminants;

treating the second effluent within an acid gas unit in a hydrocarbon gasification process;

stripping the intermediate with one or more oxidants to provide a third effluent comprising the one or more oxidants and at least a portion of the one or more thermally destructible contaminants and a fourth effluent comprising the water;

destructing the thermally destructible contaminants in the third effluent using one or more combustion processes; and

treating the fourth effluent for reuse.

13. The method of claim 12 , further comprising:

combusting at least a portion of the cooled syngas to provide an exhaust gas; and

cooling the exhaust gas to provide the heat necessary to provide at least a portion of the steam.

14. The method of claim 12 , wherein the one or more oxidants comprise air, oxygen, oxygen-enriched air, or any combination thereof.

15. The method of claim 12 , wherein a weight ratio of the steam-to-first effluent ranges from about 1:1 to about 20:1.

16. The method of claim 12 , wherein the concentration of the one or more oxidants in the intermediate is about 0.1% wt to about 5.0% wt.

17. The method of claim 12 , wherein the pressure of the steam ranges from about 200 kPa to about 1,130 kPa.

18. The method of claim 12 , wherein the one or more thermally indestructible contaminants comprise, hydrogen chloride, hydrogen sulfide, carbonyl sulfide, mixtures thereof, or any combination thereof.

19. The method of claim 12 , wherein the hydrocarbon comprises polyethylene, polypropylene, polystyrene, polyethylene terephthalate (PET), or any combination thereof.