WET AIR OXIDATION FOR WASTEWATER TREATMENT

Revision Date: 9/01
Process Code: Navy/Marines: SR-15-99; Air Force: FA09; Army: N/A
Usage: Navy: Low; Marines: Low; Army: Low; Air Force: Low
Compliance Impact: Low
Alternative for: Incineration or Other Hazardous Waste Treatment
Applicable EPCRA Targeted Constituents: Ammonia (CAS: 7664-41-7), Cyanide (CAS: 57-12-5), Toluene (CAS: 108-88-3), Aliphatic Hydrocarbons, Aromatic Hydrocarbons

Overview: Wet air oxidation (WAO) destroys toxics in industrial wastewater by breaking down complex molecular structures into simpler components such as water and carbon dioxide. The process is based on the discovery that organics will oxidize in water, at relatively low temperatures, as long as oxygen is present and the proper operating pressure is maintained. Hazardous waste is oxidized in the liquid phase at high temperatures (150-325°C) and pressures (300-3000 psi). Research indicates that most organic constituents will be oxidized under these conditions. At these elevated temperatures and pressures, the solubility of oxygen in water is dramatically increased, thus providing a strong driving force for the oxidation. The WAO process generally involves a number of oxidation and hydrolysis reactions in series that degrade the initial compound into a series of compounds of simpler structure. Complete WAO results in converting of hazardous organic compounds into carbon dioxide, water vapor and ammonia (for nitrogen containing wastes), sulfate (for sulfur containing wastes) and halogen acids (for halogenated wastes). Partial degradation products may remain in treated wastewaters from WAO and may be given subsequent treatment before being discharged.

Wet air oxidation is applicable to industrial wastewaters containing organics and oxidizable inorganics such as cyanide. The process is typically used to oxidize sewage sludge, regenerate spent activated carbon, and treat process wastewaters. Wastewaters treated using this technology include pesticide wastes, petrochemical process wastes, cyanide containing metal finishing wastes, spent caustic wastewaters containing phenolic compounds and some organic chemical production wastewaters. WAO can be used to treat wastewaters that have higher organic concentrations than are normally handled by biological treatment, carbon adsorption and chemical oxidation, but may be too dilute to be effectively treated by thermal processes such as incineration. WAO is most applicable for waste streams containing dissolved or suspended organics in the 500 to 15,000 mg/l range. Below 500 mg/l, the rates of WAO of most organic constituents are too slow for efficient application of this technology. WAO can be applied to wastes that have significant concentrations of metals (approximately 2 %) whereas biological treatment, carbon adsorption, and chemical oxidation may have difficulty treating such wastes.

WAO proceeds as a series of reaction steps and the intermediate processes are not always as readily oxidized as are the original constituents. Therefore the process does not always achieve complete oxidation of the organic constituents. As a result it is important to evaluate the process to assess the potential products of incomplete oxidation prior to implementing the technology.

WAO technology is well-developed and demonstrated for treating several hazardous wastes such as spent non-halogenated solvents and still bottoms, sludges from electroplating operations, and spent cyanide bath solutions. Successful bench scale WAO studies have been conducted on energetics [hydrazine based rocket fuel wastewater and OTTO fuel (used in torpedo propellant) wastewater], chemical agent surrogates and TNT red water. In addition, the EPA recommends WAO as the "Best Demonstrated Available Technology" for a variety of hazardous wastes.

Typical results of wet air oxidation of organic compounds in industrial wastewaters are presented in the following table:

Wet Air Oxidation of Organic Compounds In Industrial Wastewater*
Concentration, mg/l

Compound Influent Effluent % Removal
COD 56,000 7,200 87.1
Methylene Chloride 734 0.08 >99.9
Xylene 109 0.11 99.9
MEK 3,937 2.3 99.9
Benzene 8.0 0.03 99.6
Carbon Tetrachloride 2,450 2 99.9

* wet air oxidation temperature = 495°F, pressure >700 psi, residence time = 83 minutes.

The U.S. Army Construction Engineering Research Laboratories (USACERL) has completed WAO batch studies on TNT red water which is the wastewater from the manufacturing of trinitrotoluene. Major pollutants in red water include the products formed during the sellite purification of crude TNT and other by-products formed during various stages of the production process. The U.S. Environmental Protection Agency (EPA) classifies TNT red water as RCRA hazardous waste K047 due to its reactivity. The lack of a cost-effective, environmentally acceptable treatment for red water impairs the Army's mission readiness for TNT production. Results indicate that WAO can be used for successfully treating red water. Information on waste destruction rates and other performance evaluation parameters has been obtained. Toxicity of the WAO-treated red water to activated sludge and other bacteria have also been evaluated. A USACERL technical report on the feasibility, kinetics, and toxicity studies is available.


Compliance Benefit:

The use of a wet air oxidation system can help facilities meet pretreatment standards for discharges of industrial wastewater to a POTW (40 CFR 403) or meet effluent limits of a NPDES permit (40 CFR 122). A WAO system may also decrease the amount of hazardous waste generated which helps facilities meet the requirements of waste reduction under RCRA, 40 CFR 262, Appendix. It may also help facilities lessen the amount of regulations they must comply with for the management of hazardous waste (i.e., recordkeeping, reporting, inspections, transportation, accumulation) under RCRA, 40 CFR 262.

The compliance benefits listed here are only meant to be used as a general guideline and are not meant to be strictly interpreted. Actual compliance benefits will vary depending on the factors involved, e.g. the amount of workload involved.


Materials Compatibility:
Wastewater with low pH may cause corrosion damage to the metals used in the WAO equipment. Wastewater pH adjustment could provide better materials compatibility results.


Safety and Health: Care should be taken when handling wastewater. Wastewater can be toxic and/or corrosive. Proper personal protection equipment is, therefore, highly recommended.

Consult your local Industrial Health specialist, your local health and safety personnel, and the appropriate MSDS prior to implementing any of these technologies.


Benefits:
  • A variety of chemical compounds can be treated at the same time in the one step process.
  • Wastes are destroyed in liquid phase. As a result, the problems associated with air pollution are reduced.
  • The process is less energy intensive than incineration and is less likely to produce oxides of nitrogen as by-product air pollutants.


Disadvantages:
  • Waste must be in the liquid phase.
  • Limited to wastewaters containing oxidizable organic and inorganic compounds. For example, WAO cannot destroy PCBs, some halogenated aromatics and some pesticides.


Economic Analysis: Capital costs for wet air oxidation systems depend on the capacity of the system, oxygen demand reduction of the wastewater, severity of the oxidation conditions required to meet the treatment objectives, and the materials of construction of the wet oxidation system. The following analysis provides costs associated with a WAO system which would treat TNT red water. The operation and maintenance costs for the WAO system are based on estimates from the U.S. Army Construction Engineering Research Laboratories and is based on redwater at 3.2 MG/year.

Assumptions:

  • WAO System for treating TNT red water costs $12 million for a 16,000 gallon per day system.
  • Operation and maintenance costs $974,000 per year.
  • WAO system runs 200 days per year.
  • Disposal of hazardous waste costs $1.17 per gallon.
  • Labor of 100 man-hours a year for disposal of hazardous waste at $45 per hour.
  • WAO system runs at 340°C and 1 hour contact time.

Cost Comparison for WAO System vs. Disposal of Wastewater

  WAO Disposal
Capital and Installation: $12,000,000 $0
Operation and Maintenance Costs: $974,000 $4,500
Waste Disposal: $0 $3,744,000
Annual Total (w/o capital): $974,000 $3,748,500

Economic Analysis Summary

    Annual Savings for WAO: $2,774,500
    Capital Cost for Diversion Equipment/Process: $12,000,000
    Payback Period for Investment in Equipment/Process: 4.3 years

Click Here to view an Active Spreadsheet for this Economic Analysis and Enter Your Own Values. To return from the Active Spreadsheet, click the reverse arrow in the Tool Bar.


Approving Authority: Approval is controlled locally and should be implemented only after engineering approval has been granted. Major claimant approval is not required.


NSN/MSDS:
Product NSN Unit Size Cost MSDS*
None Identified     $  


*There are multiple MSDSs for most NSNs.
The MSDS (if shown above) is only meant to serve as an example.


Points of Contact: Army:
Dr. Stephen Maloney
USACERL
ATTN: CECER-CN-D
P.O. Box 9005
Champaign, IL 61821-9005
Phone: (217) 373-3482 or (800) USA-CERL
FAX: (217) 373-3430
Email:  s-maloney@cecer.army.mil


Vendors: This is not meant to be a complete list, as there are other manufacturers of this type of equipment.

US Filter, Zimpro Division, Inc.
301 W. Military Road
Rothschild,  WI   54474
Phone: (715) 359-7211 


Sources: Dr. Stephen Maloney, Ph.D., USACERL, November 1999.
Mr. William Copa, Ph.D., U.S. Filter/Zimpro, Rothschild Wisconsin, July 1997.
"Wet Air Oxidation of Hazardous Waste, U.S. Filter/Zimpro.
"Wet Air Oxidation, A "rediscovered technology"," Reactor, May 1989.
"Wet Air Oxidation (WAO) of TNT Red Water," USACERL Fact Sheet, February 1996.
S.W. Maloney, V.M. Boddu, K.K. Phull and O.J.Hao, "TNT Red Water Treatment by Wet Air Oxidation," USACERL Technical Report EP-95/01, November 1994.



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