FLUIDIZED BED PAINT STRIPPER

Revision Date: 8/01
Process Code: Navy/Marines: ID-03-99; Air Force: ST01; Army: DPT
Usage: Navy: Medium; Marines: Low; Army: Low; Air Force: Low
Alternative for: Chemical Paint Stripping and Degreasing
Applicable EPCRA Targeted Constituents: Cadmium (CAS: 7440-43-9), Chromium (CAS: 7440-47-3), Lead (CAS: 7439-92-1), Zinc (CAS: 7440-66-6)

Overview: The fluidized bed paint removal process is an alternative method to chemical paint stripping and degreasing of non-aluminum and non-heat-sensitive metal parts. The most notable pollution prevention benefit of this process is that it produces no solvent wastes. The fluidized bed paint stripper (FBPS) can be used for forged steel, but not aluminum or aluminum alloys.

The FBPS process removes paint or other organic coatings by heating the part too greater than 650 degrees F to cause pyrolysis and decomposition of the organic portion of the paint. The FBPS typically consists of the following four components: 1) fluidized-bed furnace or retort, 2) fluidized-bed cooling system, 3) off-gas treatment system consisting of a cyclone, afterburner and scrubber, and 4) low energy shot-blast unit. The fluidized-bed furnace or hot bed is where pyrolysis of the coatings takes place. A granular material, aluminum oxide (alumina) in most cases, is used as a heat transfer medium. Air passing through the bed keeps the media fluidized. Parts to be cleaned are lowered into the fluidized bed, which quickly heats the part and its surface coatings (paint, grease, oil, etc.) to a temperature at which organic components of the surface material
pyrolyze into carbon oxides, other gaseous combustion products, and char. The fluidized-bed cooling system or cold bed is used to cool the parts after the organics have been pyrolyzed. Carbon monoxide and volatile organic compounds (VOCs) generated during pyrolysis are burned in the afterburner. The thermal decomposition of paint leaves some carbon and inorganic char on the part. Most of the char may be removed in the fluidized bed; however, most parts require further cleaning before they can be repainted. The shot-blast unit is used to remove the inorganic coatings and char to prepare the parts for repainting.

This process removes and destroys paint and grease from non-aluminum or non-heat sensitive materials. Waste streams from this process include spent heat transfer medium, spent blast media, exhaust air from the afterburner and scrubber, water discharge from the scrubber, and dust from the cyclone separator. The heat transfer medium, blast media, and cyclone dust will contain metals from the stripped paint.

Field demonstrations of the FBPS have been performed at two Army Depots: Letterkenny, PA and Red River, TX. The findings and conclusions of these demonstration projects noted specific limitations of the FBPS process.

The Air Force does not have many rework facilities where the components are primarily steel and can be heated to the temperatures required by this process. Consequently, it will be difficult to find sufficient workload suited to this process and to justify the capital investment. It is an excellent process and it would be recommended where appropriate and after engineering approval.


Compliance Benefit:

Use of a fluidized bed paint stripper will help a facility decrease the amounts of solvents used and stored on site and therefore, decreases the possibility that a facility will meet reporting thresholds for solvents under 40 CFR 355, 370 and EO 12856.

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:

The FBPS process is not suitable for use with aluminum and aluminum alloy parts because these materials lose essentially all of their hardness or temper when exposed to the 700 to 800 degree F process temperatures.


Safety and Health:

Inhalation of lead and zinc chromate paints can lead to irritation of the respiratory tract. Some lead compounds are carcinogenic. Solvent-based paints can irritate the lungs and mucous membranes. Prolonged exposure can affect respiration and the central nervous system. Proper personal protective equipment should be used.

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


Benefits:
  • Leaves almost no waste paint residue, thus eliminating significant waste sludge disposal costs as well as avoiding the future liability associated with the hazardous components of the paint sludge 
  • Uses an inert medium to clean parts of any shape, size, or geometry and coated with any type of paint. The rapid changes in coating technology do not affect the performance of the system 
  • Provides cleaning to the bare metal


Disadvantages:
  • FBPS is not suitable for removal of paint from aluminum and aluminum alloy parts. 
  • The fluidized bed media may be regulated as a RCRA characteristic hazardous waste because of toxicity. 
  • The FBPS process is not suitable for parts with crevices, channels, or cavities (e.g. engine blocks) that would retain FBPS media and be difficult to clean after treatment. 
  • The FBPS process has little or no effect on corrosion removal. 
  • Parts may require secondary cleaning to remove char and inorganic coatings. 
  • The amount of waste generated by the FBPS system may exceed the volume of wastes generated by a caustic stripping system. 
  • The FBPS workers and any workers in the buildings containing the system may be subject to Occupational Safety and Health Act (OSHA)
    requirements for employees exposed to lead under 29 CFR 1910.1025.


Economic Analysis: The cost elements of the FBPS are compared to stripping using Water Blast Plus. The following economic analysis shows the FBPS to have a lower annual cost than Water Blast Plus. Water Blast Plus was chosen as the comparison technique instead of chemical stripping since it has a lower annual cost than chemical stripping. Fluidized bed paint strippers can range from $7,000 for a small parts stripper to $800,000 for an industrial scale stripper.

Assumptions:

  • 350 lbs. paint per load. 
  • 2 hours per load. 
  • Cost of media grit: $1.08/lb. 
  • Amount of media grit used: 6,200 lbs. 
  • 10 percent of the paint is converted to dry ash (hazardous waste): 70,000 lb/yr. 
  • Electricity and gas costs for FBPS: $21,400/month. 
  • Electricity costs for Water Blast Plus: $7,800/month. 
  • Disposal cost of sludge and ash: $2/lb. 
  • Operator (one per shift): $30/hr. 
  • Water cost: $1.60/1000 gal. 
  • Water use: 100 gpm (24,000,000 gallons/year). 
  • Maintenance costs FBPS: $625/month. 
  • Maintenance costs Water Blast Plus: $20,800/month. 
  • Amount of sludge generated from Water Blast Plus: 700,000 lb/yr. 
  • The annual costs are based on the operation of 2 shifts/day, 5 days/week, 50 weeks/year.

Annual Operating Cost Comparison for Paint Stripping by FBPS and Water Blast Plus

 

FBPS

Water Blast Plus

Operational Costs:

   

Labor:

$120,000

$120,000

Shot & Fluid Bed Media:

$6,700

$0

Utilities:

$256,800

$93,600

Water:

$0

$38,400

Maintenance Labor & Parts:

$7,500

$249,600

Disposal Cost:

$140,000

$1,400,000

Total Operational Costs:

$531,000

$1,901,600

Total Recovered Income:

$0

$0

Net Annual Cost/Benefit:

-$531,000

-$1,901,600

Economic Analysis Summary

Annual Savings for FBPS: $1,370,600
Capital Cost for Diversion Equipment/Process: $800,000
Payback Period for Investment in Equipment/Process: < 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:

Due to the low potential application of this process within the Air Force, technical guidance for this process will not be provided by the Air Force Corrosion Program Office. Any implementation of this process will require approval of the engineering authority for specific Weapon System Managers and Equipment Item managers.


NSN/MSDS:

None identified.


Points of Contact:

Air Force:
Air Force Corrosion Prevention and Control Office
AFRL/MLS-OLR (Bldg. 165)
325 Richard Ray Boulevard
Robins AFB, GA 31098-1640
Phone: (478) 926-3284 
DSN: 468-3284
Email:  AFCORR@ROBINS.MIL

Navy:
Dave Piatkowski
NAWCAD Lakehurst
Lakehurst, NJ
Phone: (732) 323-2716 
DSN: 624-2716 
FAX: (732) 323-1988 
Email: piatkowskidm@navair.navy.mil


Vendors:

Segers Better Technology
3114 Emery Circle
Austell, GA 30168
Phone: (770) 739-4205 
FAX: (770) 739-0117

This is not meant to be a complete list, as there may be other suppliers of this type of equipment.


Sources:

Technical Report No.TR-FBS-86-01 dated January 16, 1986 by Procedyne Corporation. 
Final Report: Engineering Test Report Paint Waste Reduction Fluidized Bed Process Demonstration at Letterkenny Army Depot, Chambersburg, Pennsylvania (July 1991). Contract No. DAAA15-88-D-0001, Task Order 0007
Final Report: Evaluation of a Fluidized - Bet Paint Stripper Red River Army Depot, Texarkana, Texas (April 1992). Contract No. DAAA 1S-88-D-001, Task Order 0005. Point of Contact (E. Hanna).


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