SOLVENT DISTILLATION

Revision Date: 12/00
Process Code: Navy/Marines: ID-24-00; Air Force: HW01; Army: CLD, VHM, DPT
Usage: Navy: High; Marines: High; Army: High; Air Force: High
Compliance Impact: Low
Alternative for: Single use of Methyl Ethyl Ketone, Methyl Chloroform, and CFC-based Solvents
Applicable EPCRA Targeted Constituents: Methyl Ethyl Ketone (CAS: 78-93-3), 1,1,1-Trichloroethane (CAS: 71-55-6), CFCs, Chlorinated Organic Compounds


Overview:

Solvent distillation as a means of recycling, is a viable alternative to the single use/disposal of solvents. It is environmentally benign and reduces the amount of solvent purchased and disposed. Solvent distillation is best suited for processing waste solvents that are not excessively contaminated.

Solvent distillation units process waste solvents in separate, stand-alone batch, on-line batch, or continuous systems. The distillation units heat the waste solvent to its boiling point. This causes the solvent to evaporate and the solvent vapors are then condensed in a separate container. The remaining contaminants in the process chamber are disposed. The basic components of a distillation unit are the process chamber or boiler, encapsulated heaters, a water-cooled chamber, and associated piping and instrumentation. Temperature sensors monitor the temperature and help maintain the required distillation temperature. Disposable vessel liners can be used to provide simple collection and disposal of still bottoms. Vacuum pumps that can distill high-boiling solvents at lower temperatures are also available.

Operating experience at Charleston AFB has shown recoveries of 90 to 95 percent for solvents recycled by batch vacuum distillation. Five-gallon batches of methyl ethyl ketone or paint thinner in nominal 5-gallon units typically require 3.5- to 3.75-hour cycles to complete evaporation.

According to Naval Aviation Depot, Cherry Point, solvent distillation rarely brings the designated material back to it's original requirement. At NADEP, both CFC-113 and P-D-680 are distilled in separate units. Generally, distillation processes result in a useable solvent product or a mixture that can be used to serve an alternate purpose. According to NADEP, an example of this is the solvent distillation for CFC-113 (Freon). NADEP procures CFC-113 with less than 2ppm of hydrocarbon contamination. After distillation, the Freon now contains less than 5 ppm of hydrocarbon contamination that, although still suitable for use, is not as pure as virgin material. In addition, excessive contamination adds to distillation cost because it generally requires more than one cycle.


Compliance Benefit: Use of a solvent distillation will decrease the amount of waste solvent disposed. The decrease in hazardous waste will help facilities meet the requirements of waste reduction under RCRA, 40 CFR 262, Appendix, and may also help facilities reduce their generator status and lessen the applicable regulatory (i.e., recordkeeping, reporting, inspections, transportation, accumulation time, emergency prevention and preparedness, emergency response) requirements 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:
Distillation equipment should be constructed of high-alloy stainless steel to prevent corrosion from degradation of solvents or the heating oil. The alloys also protect against iron contamination of the recovered solvent. Using a liner adds an extra layer of protection to the distillation unit’s boiling chamber and greatly simplifies cleaning. The liner containing the solvent residue is simply lifted out of the unit for proper disposal.


Safety and Health: Proper design, operation, and maintenance of the distillation equipment are required for its safe use.

Inhalation of solvent vapors can cause irritation to the respiratory tract and mucous membranes. Prolonged exposure may result in damage to the lungs and central nervous system. Contact with the skin can cause dryness, irritation, and possibly dermatitis. Use in well ventilated areas with proper personal protective equipment.

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


Benefits:
  • Less hazardous waste and hazardous air emissions are generated
  • Reduces hazardous waste disposal costs
  • Provides solvent cost savings
  • Reduces worker exposure to solvent, hazardous waste, and hazardous air emissions


Disadvantages:
  • Requires trained personnel to perform the recycling process and operate the process equipment
  • Equipment or recycling process may require permits from a local regulatory agency


Economic Analysis:

Solvent distillation systems need to be specific to the type of solvent, the contaminants being removed, the batch size or throughput, and the type of cleaning operation. These requirements lead to a wide range of costs. For instance, self-contained, batch-distillation units vary in price from $2,000 to more than $30,000. Costs of the units depend on the size, the materials of construction, and the options selected. Capacities typically range from 1- to 250-gallon batches. The following cost estimate is for the use of a 2-gallon capacity solvent distillation-recycling unit. The Freon procurement cost is based on information obtained through FEDLOG:

Assumptions:

  • Freon 113 usage (single use of solvent application): 500 gal/yr.
  • Freon 113 usage (with distillation unit): 100 gal/yr.
  • Freon procurement cost: $130-140/gal.
  • Waste solvent (single use of solvent application): 400 gal. or 640 lb/yr.
  • Distillation unit waste sludge (still bottoms): 250 lb./yr.
  • Waste solvent disposal cost: $1.40/lb.
  • Still bottoms disposal cost: $1.25/lb.
  • Labor required for disposal of waste solvent: 1 hr./wk. or 52 hr./yr.
  • Distillation unit electrical requirements: 480 kw-hr./yr.
  • Electricity: $0.08/kw-hr.
  • Labor rate: $45/hr.
  • Total labor requirements recycling unit operation: 2 hr./wk. or 104 hr./yr.
  • Solvent distillation unit cost (installation and training): $3,800

Annual Operating Cost Comparison for Solvent Distillation and Solvent Disposal

 

Solvent Distillation

Solvent Disposal

Operational Costs:

   

Material:

$13,500

$67,500

Labor:

$4,680

$2,340

Electricity:

$38

$0

Waste Disposal:

$313

$896

Total Operational Costs:

$18,531

$70,736

Total Recovered Income:

$0

$0

Net Annual Cost/Benefit:

-$18,531

-$70,736

Economic Analysis Summary

    Annual Savings for Solvent Distillation: $52,205
    Capital Cost for Diversion Equipment/Process: $3,800
    Payback Period for Investment in Equipment: < 1 year

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*
Solvent Reclaimer (distillation unit) 4940-01-395-9468 ea. (25 gal) $N/A  
Solvent Reclaimer (distillation unit) 4940-01-395-9469 ea. $N/A  
Solvent Reclaimer 4940-01-312-0765 ea. (5 gph) $5,441.42  

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


Points of Contact: Navy:
Ms. Stacey Luker
Naval Aviation Depot, Cherry Point
Cherry Point, NC
Phone: (252) 464-8142


Vendors: Detrex Corporation
322 International Parkway
Arlington,  TX   76011
Phone: (800) 525-1496 

  Finish-Thompson Inc.
921 Greengarden Road
Erie,  PA   16501-1591
Phone: (814) 455-4478 
FAX: (814) 455-8518

  PBR Industries
143 Cortland Street
Lindenhurst,  NY   11757
Phone: (516) 226-2930 
FAX: (516) 226-3125
URL: http://www.pbrind.com

Sources:

Ms. Stacey Luker, NAVDEP Cherry Point, December 1999.
John Hurley, Branson Ultrasonics Corporation, January 1998.
PA Technical Bulletin # 2791, August 94, Finish Thompson Inc. and PBR Industries product literature
Salvesen, Robert H., "On-Site Reuse and Recycle of Solvents," Solvent Waste Reduction; US Environmental Protection Agency, Cincinnati, OH; ICF Consulting Associates, Inc., Los Angeles, CA; pp. 78-89, 1990.



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