Treatment of spent caustic waste

Patent metadata

Field	Value
Publication number	US-9630867-B2
Application number	US-201414285572-A
Country	US
Kind code	B2
Filing date	May 22, 2014
Priority date	Sep 11, 2007
Publication date	Apr 25, 2017
Grant date	Apr 25, 2017

Abstract

Systems and methods are provided for the treatment of caustic wastewater. Specifically, systems and methods are provided for combining refinery spent caustic and ethylene spent caustic solutions and treating the combined spent caustic mixture using a wet air oxidation process.

First claim

What is claimed is:

1. A system for treating a waste stream comprising:
a source of a sulfidic spent caustic;
a source of refinery spent caustic;
a mixed caustic conduit having an inlet in communication with the source of sulfidic spent caustic and the source of refinery spent caustic; and
a wet air oxidation unit comprising an inlet and an effluent outlet, the inlet of the wet air oxidation unit in communication with an outlet of the mixed caustic conduit; and
a heat exchanger arranged to receive an oxidized effluent from the effluent outlet and a mixed caustic from the mixed caustic conduit, the heat exchanger effective to heat the mixed caustic with heat from the oxidized effluent.

2. The system of claim 1 , further comprising a source of a pH adjuster in fluid communication with the wet air oxidation unit.

3. The system of claim 2 , wherein the source of pH adjuster is a source of carbon dioxide.

4. The system of claim 2 , further comprising a biological treatment unit in fluid communication with the effluent outlet and downstream of the wet air oxidation unit.

5. The system of claim 4 , further comprising a source of a pH adjuster in fluid communication with the effluent and upstream of the biological treatment unit.

6. The system of claim 1 , wherein the mixed caustic comprises a COD concentration of from 20,000 to 125,000 mg/L.

7. The system of claim 6 , wherein the refinery spent caustic has a COD concentration of more than 100,000 mg/L, wherein the sulfidic spent caustic comprises an ethylene spent caustic, and wherein the ethylene spent caustic comprises a COD concentration of 30,000 mg/L or less.

8. A method for treating a waste stream comprising:
combining a sulfidic spent caustic comprising at least a first organic compound with a refinery spent caustic comprising at least a second organic compound in a ratio sufficient to produce a combined stream comprising a COD level below that which results in the precipitation of carbonate during a wet air oxidation of the combined stream and above a level which will allow the wet air oxidation reaction of the combined stream to be self sustaining; and
oxidizing by wet air oxidation the combined stream at an elevated temperature and a superatmospheric pressure sufficient to treat at least a portion of the second organic compound.

9. The method of claim 8 , wherein the combined stream COD level is between about 20,000 mg/L and 100,000 mg/L.

10. The method of claim 9 , further comprising heating the combined stream with an effluent from the wet air oxidation unit.

11. The method of claim 10 , further comprising treating at least a portion of the effluent in a biological treatment unit.

12. A system for treating a waste stream comprising:
a wet air oxidation unit comprising an inlet and an outlet;
a source of ethylene spent caustic comprising at least one oxidizable compound in fluid communication with the inlet of the wet air oxidation unit;
a source of refinery spent caustic comprising at least one organic compound in fluid communication with the inlet of the wet air oxidation unit;
a combined caustic stream comprising the ethylene spent caustic and the refinery spent caustic within the wet air oxidation unit, the combined caustic stream comprising a COD level below that which results in precipitation of carbonate upon wet air oxidation of the combined stream; and
a heat exchanger arranged to receive an oxidized effluent from the outlet of the wet air oxidation unit and the combined caustic stream upstream of the wet air oxidation unit, the heat exchanger effective to heat the combined caustic stream with heat from the oxidized effluent;
wherein the wet air oxidation unit is configured to oxidize the combined stream at an elevated temperature and a super-atmospheric pressure.

13. The system of claim 12 , further comprising a post-treatment unit in communication with the outlet of the wet air oxidation unit.

14. The system of claim 13 , further comprising: a pH sensor configured to detect a pH of an effluent of the wet air oxidation unit; a controller coupled to the pH sensor; and a source of pH adjuster coupled to the controller and in fluid communication with the wet air oxidation unit.

15. The system of claim 14 , wherein the source of pH adjuster is selected from the group consisting of an acid, a base, and carbon dioxide.

16. The system of claim 12 , wherein the combined caustic stream comprises a COD concentration of from 20,000 to 125,000 mg/L.

17. The system of claim 12 , wherein the refinery spent caustic has a COD concentration of more than 100,000 mg/L, and wherein the ethylene spent caustic further comprises a COD concentration of 30,000 mg/L or less.

18. A system for treating a waste stream comprising:
a source of a sulfidic spent caustic;
a source of refinery spent caustic;
a mixing vessel having one or more inlets in communication with the sources of ethylene and refinery spent caustics;
a mixed caustic conduit extending from and in communication with an outlet of the mixing vessel; and
a wet air oxidation unit comprising an inlet in communication with an outlet of the mixed caustic conduit; and
a heat exchanger arranged to receive an oxidized effluent from an outlet of the wet oxidation unit and a mixed caustic from the mixed caustic conduit, the heat exchanger effective to heat the mixed caustic with heat from the oxidized effluent.

19. The system of claim 18 , wherein the mixed caustic comprises a COD concentration of from 20,000 to 125,000 mg/L.

20. The system of 26 , wherein the refinery spent caustic has a COD concentration of more than 100,000 mg/L, wherein the sulfidic spent caustic comprises an ethylene spent caustic, and wherein the ethylene spent caustic further comprises a COD concentration of 30,000 mg/L or less.

Assignees

• Siemens Energy Inc

Inventors

• Kumfer Bryan J
• Felch Chad L
• Brandenburg Bruce L
• Lehmann Richard W

Classifications

• C02F2103/365

  from petrochemical industry (e.g. refineries) · CPC title

• C02F1/44

  by dialysis, osmosis or reverse osmosis {(general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268)} · CPC title

• C02F3/00

  Biological treatment of water, waste water, or sewage {(C02F1/006 takes precedence)} · CPC title

• C02F3/02

  Aerobic processes · CPC title

• C02F1/02

  by heating (methods of steam generation F22B; preheating boiler feed-water or accumulating preheated boiler feed-water F22D) · CPC title