Purified terephthalic acid (PTA) vent dryer vapor effluent treatment

1. A process for manufacturing a purified aromatic carboxylic acid comprising:

contacting crude aromatic carboxylic acid with hydrogen in the presence of a catalyst in a hydrogenation reactor to form a purified aromatic carboxylic acid;

separating a vapor effluent from the purified aromatic carboxylic acid;

scrubbing the vapor effluent to form a scrubber effluent;

treating the scrubber effluent to form a gaseous treated scrubber effluent and a liquid treated scrubber effluent; and

removing at least a portion of organic impurities from the liquid treated scrubber effluent.

2. The process of claim 1 , wherein the removing step comprises recovering the at least a portion of organic impurities from the liquid treated scrubber effluent.

3. The process of claim 1 , wherein the removing step comprises decomposing the at least a portion of organic impurities from the liquid treated scrubber effluent.

4. The process of claim 1 , wherein the removing step comprises recovering at least a first portion of organic impurities from the liquid treated scrubber effluent and decomposing at least a second portion of organic impurities from the liquid treated scrubber effluent.

5. The process of claim 1 , further comprising oxidizing a substituted aromatic compound in a reaction zone to form the crude aromatic carboxylic acid.

6. The process of claim 1 , further comprising crystallizing the purified aromatic carboxylic acid in a crystallization zone to form a slurry stream comprising solid purified aromatic carboxylic acid.

7. The process of claim 6 , further comprising separating purified carboxylic acid solids from the slurry stream in a separation zone.

8. The process of claim 7 , wherein the separating step comprises drying the purified carboxylic acid solids in a drying zone to form a purified carboxylic acid product and the vapor effluent.

9. The process of claim 1 , wherein the scrubber effluent comprises more than about 5 percent non-methane hydrocarbons on a dry basis.

10. The process of claim 1 , wherein the gaseous treated scrubber effluent comprises less than about 5 percent non-methane hydrocarbons on a dry basis.

11. The process of claim 1 , wherein the treating step comprises condensing the scrubber effluent in at least one heat exchanger to form the liquid treated scrubber effluent and the gaseous treated scrubber effluent.

12. The process of claim 11 , wherein the scrubber effluent is at a temperature of about 95-102 degrees Celsius, and wherein the liquid treated scrubber effluent is at a temperature of about 30-80 degrees Celsius.

13. The process of claim 11 , wherein the treating step further comprises thermally oxidizing the gaseous treated scrubber effluent.

14. The process of claim 1 , wherein the treating step comprises scrubbing the scrubber effluent with a caustic substance to form the liquid treated scrubber effluent and the gaseous treated scrubber effluent.

15. The process of claim 14 , wherein the scrubbing step and the treating step are performed in the same piece of equipment.

16. The process of claim 14 , wherein the treating step further comprises cooling the gaseous treated scrubber effluent and thermally oxidizing the gaseous treated scrubber effluent.

17. The process of claim 1 , wherein the treating step comprises oxidizing the scrubber effluent in a thermal oxidizer to form the gaseous treated scrubber effluent, and wherein the scrubber effluent is heated prior to being oxidized.