BILGE AND OILY WASTEWATER TREATMENT SYSTEM (BOWTS)

Revision Date: 01/04
Process Code: Navy/Marines: SER-015-99, ID-25-02; Air Force: FA09; Army: N/A
Usage List: Navy: Medium; Marines: Low; Army: None; Air Force: Low
Alternative For: Treatment using ferrous sulfate, aluminum, and polymers to break emulsions, in conjunction with an oil water separator for free oil removal, and calcium hydroxide for metal removal.
Compliance Impact: Low
Applicable EPCRA Targeted Constituents and CAS Numbers: Benzene (CAS: 71-43-2), Antimony (CAS: 7440-36-0), Arsenic (CAS: 7440-38-2), Cadmium (CAS: 7440-43-9), Chromium (CAS: 7440-47-3), Copper (CAS: 7440-50-8), Lead (CAS: 7439-92-1), Mercury (CAS: 7439-97-6), Nickel (CAS: 7440-02-0), Selenium (CAS: 7782-49-2), Silver (CAS: 7440-22-4), Thallium (CAS: 7440-28-0), Zinc (CAS: 7440-66-6), Pesticides, Polychlorinated Biphenyls (CAS: 1336-36-3), and Phenolic Compounds (No CAS)

Overview: The Naval Facilities Engineering Service Center (NFESC) has developed a shore-side system for treating bilge and other oily wastewaters in addition to designing a 50-gpm mobile system. The Bilge and Oily Wastewater Treatment System (BOWTS) separates oil, grease, and heavy metals found in bilge and oily waters. BOWTS has the capability to lower the contaminant levels to less than the permissible limits for discharge into publicly owned treatment works (POTWs).

The BOWTS shore-side systems have successfully operated at Naval Shipyard Long Beach, Naval Air Station Alameda, California; Fleet Industrial Support Center Oakland, California; Naval Station Pearl Harbor, Hawaii; Naval Station Guantanamo Bay, Cuba; Naval Station Guam; Naval Station San Diego, California; Submarine Base San Diego, California; Naval Construction Battalion Center, Port Hueneme, California; and the Naval Station Roosevelt Roads, Puerto Rico. Mobile systems also were shipped to Yokosuka and Sasebo Japan in September 1999.

The ship's bilge water is transferred to a large load equalization tank, equipped with a skimmer for removal of bulk free product. After sufficient residence time, the water fraction is selectively removed and fed through a plate coalescer for mechanical removal of free oil. The water then passes through mixing chambers where chemical treatment is performed.

Three chemical metering pumps feed a reverse emulsion breaker, sodium hydroxide, and anionic polymer into the mixing chambers to breakdown the emulsion, precipitate the heavy metals, and floc the solids. The effluent is then pumped into an induced-air flotation unit, where all the solids generated by the process are removed. Two slop oil tanks are provided for collecting the free oil separated in the load equalization tank and the oil/water separator, and a sludge tank is provided for holding the sludges collected in the oil/water separator and the induced-air flotation device. The water fraction leaving the system will be of sufficient quality to be discharged directly into the sanitary sewer.

Although the pollutants found in ships' bilges and other oily wastewaters vary from ship to ship, NFESC applied a strategy to categorize and quantify the principal pollutants. The data collected were used in designing the basic BOWTS. Additional process units could be added where local discharge requirements indicate the need for more rigorous treatment than is available from the basic system design.


Compliance Benefit: The use of a bilge and oily wastewater treatment system can help facilities meet pretreatment standards for discharges of wastewater to a POTW (40 CFR 403) or meet the effluent limits of an NPDES permit (40 CFR 122). In addition, this treatment process may help facilities meet the requirements of waste reduction under RCRA (40 CFR 262) and Executive Order 13148. It may also help facilities reduce the amount of regulations they must comply with for the management of hazardous waste (i.e., recordkeeping, reporting, inspections, transportation, and accumulation) under RCRA (40 CFR 262).

The compliance benefits listed here are only meant to be used as general guidelines 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: No materials compatibility issues were identified.


Safety and Health: BOWTS chemicals are irritants to skin, eyes, and mucous membranes. Inhalation of these fumes can be dangerous. Proper personal protection equipment is recommended.

Consult your local industrial health specialist, your local health and safety personnel, and the appropriate MSDS prior to implementing this technology.


Benefits:
  • BOWTS can recover oil for recycling.
  • BOWTS is a proven off-the-shelf technology.
  • The system is sufficiently flexible to accommodate a wide range of concentrations and flow ranges; each system can be tailored to site-specific requirements (e.g., configuration and modifications).
  • The BOWTS requires only one or two people to operate and monitor the process.


Disadvantages:
  • Not an economical alternative for activities generating less than one million gallons of ship’s bilge and oily wastewater annually.


Economic Analysis: The BOWTS design is unique for each activity and reflects selection of hundreds of component parts designed for automatic operation within the activity’s infrastructure. The following analysis is based on data provided by Naval Station San Diego.

Assumptions:

  • The system processes 15 million gallons of wastewater annually.
  • Traditional methods require transport of large volumes of oily wastewater for treatment/disposal at a cost of $0.24/gallon.
  • Cost figures for the BOWTS system are actual budgetary allocations for each activity provided by Naval Station San Diego.

Table 1. Cost Comparison for BOWTS System vs. a Traditional Disposal System

 

Traditional System

BOWTS

Capital and Installation Costs: $0 $1,400,000
Operational Costs:    
Operation and Maintenance Costs: $0 $300,000
Waste Treatment and Disposal Costs: $3,600,000 $77,000
Utility Costs (electricity, sewer): $0 $140,000
Permitting and Lab Analysis Costs: $0 $24,000
Total Costs (not including capital and installation costs): $3,600,000 $540,000
Total Income: $0 $0
Annual Benefit: - $3,600,000 -$540,000

Economic Analysis Summary:

  • Annual Savings for BOWTS: $3,060,000
  • Capital Cost for Diversion Equipment/Process: $1,400,000
  • Payback Period for Investment in Equipment/Process: < 6 months

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


NSN/MSDS: None identified.


Approving Authority: Appropriate authority for making process changes should always be sought prior to procuring or implementing any of the technologies identified herein.


Points of Contact:


Vendors: NFESC is the system developer.


Related Links: Mobile Bilge Cleaning System


Sources: Mr. James Sanfedele, Naval Station San Diego, January 2000.
Mr. Tom Torres, Naval Facilities Engineering Service Center, February 1999.


Supplemental: Picture of Bilge and Oily Wastewater Treatment System (BOWTS)
Picture of  Bilge and Oily Wastewater Treatment System (BOWTS)