HAVABLACK S2G BLACK OXIDE SALTS FOR IRON & STEEL

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BLACK OXIDE SALTS FOR IRON & STEEL produces a jet black ferro-ferric oxide (Fe304) film on ferrous alloys that when coated with oil, lacquer or waxes, provides moderate corrosion protection to 20% salt spray for indoor storage. does not produce hydrogen embrittlement of the ferrous alloys making it an excellent finish for springs and tools. coatings impart minimal dimensional changes to the part (av.10 millionths of an inch) has good wear resistance, excellent adhesion properties and will not flake off or chip even when parts are exposed to extreme deformation. is economical to run and lends itself to small part / high surface area throughput. surface luster is dependent only on the original surface appearance lending itself to satin or higher luster finishes without special operation in the coating process. OPERATING CONDITIONS: EQUIPMENT: Concentration 6.5 lbs/gal. (780 g/l) Temperature 285 300 o F (141 149 o C) Time 5-30 minutes processing tanks should be constructed of steel with the gauge of steel used being sufficient to hold a solution weighing 14 pounds/gallon and tank joints secured with double oxide free welds. Steam may be used for solution heat if 80 pounds/in 2 is available. The coil should be installed at one side or end of the tank and tank walls and bottom being insulated with one-inch magnesia insulation held on by steel casing. Steam coils should NOT be put on the bottom of the tank. If high-pressure steam is not available, gas pipe burners can be used. Tank walls should then be insulated on all four sides with one-inch magnesia insulation held together with steel casing, allowing 1-2 inches of spacing between tank wall and the insulation to allow heat to rise on the side of the tanks. (Note: It will take approximately 1700 BTU's to heat one gallon of solution from room temperature to 285 o F.) Page 1 of 5 Revised May 23, 2007 Approved: Graham M. Torr, CEF-3 Technical Service Manager Haviland Products Co. 421 Ann St. N.W. Grand Rapids, MI 49504-2075 (616) 361-6691 Fax (616) 361-9772

Page 2 of 5 EQUIPMENT (Cont.): Electrical immersion heaters may also be used to control temperature, with 100 gallons of solution requiring 60 KW to heat tank in one hour from room temperature to 285 o F. The electrical heater should be installed on one side of the tank and NOT on the bottom. Usually, heaters are designed for 220 or 440 volts to keep the required amperage down. PROCESSING EQUIPMENT: Work can be processed on racks, in baskets or in barrels. This processing equipment should be made of steel. There should be no copper, lead or other non-ferrous metals in contact with the solution. Racks should be agitated to assure solution contact on all areas. Bulk handling equipment, such as barrels, cylinders or baskets should be tumbled occasionally to assure contact areas are coated. SOLUTION MAKE-UP: 1. Clean tank of all debris, rust or loose scale. This is important since rust and scale can dissolve and redeposit on finished work, which will result in a reddish deposit or film. 2. Measure the tank volume to the operating level 6" from the top (divide cubic inch volume by 231 to obtain gallons). 3. Fill tank half full with cold water. 4. SLOWLY, add the required amount of to the water with constant stirring. The temperature will rise as the salts are added. An iron paddle should be used to stir the solution. CAUTION: There can be splattering, boil-over or caustic spray of this material as it is added. Therefore, personal protective equipment must be worn by the operator. If mist or is present consideration should be given to wearing a respirator. Refer to the MSDS for more information. 5. After all salts are dissolved (check bottom of tank with paddle), water should be added with constant stirring until the solution is 2" below the operating level. 6. Then, start heating the tank while stirring until the bath starts to boil. NOTE: Operating, boiling temperature should be 285-300 F. If the boiling temperature is below 285 o F, SLOWLY add salts until the boiling point of 285 o F is reached. If the boiling point exceeds 295 o F, add water until the boiling point is within range. The heat should then be lowered to provide a gentle roll.

Page 3 of 5 CAUTIONARY NOTES: Water additions to the tank can create splattering, eruptions or boil-over due to the high temperature. There are two methods that can be used to control water content in the bath, which determines the boiling point and concentration. Usually, the boiling point increases due to evaporation. 1. Automatic Method: Use a Bristol automatic temperature controller, an electric, lock-in relay, and a 1/2 hp motor-operated valve on a 1/2 water line. 2. Manual Method: Use a dial thermometer for easy observation by operator and a hand-operated water valve on a 1/2" water line. The water pipe should be 1/2" black iron and extend to a point just above the normal solution level and the pipe should be capped with a 1/8" hole drilled on the side that faces the tank wall. A shield should be constructed to prevent splattering toward the operator. The pipe and splash shield should be located on the backside of the tank away from the operator or loading end of the tank. Water should be added while the solution is heated to the boiling point. This will provide agitation to get water mixed into solution. If agitation is not maintained while water is being added, other methods of agitation must be provided. Note: The water, otherwise, may not mix and can form a layer on top of the solution. This can result in an eruption that could cause boil-over of the solution from the tank. PROCESSING PARTS (TYPICAL CYCLE): 1. Clean in alkaline cleaner, CLEANER SSP-140, 8 oz/gal (60 g/l), 180-200 o F (82-93 o C), to remove soils. 2. Cold water rinse. 3. OPTIONAL: Acid pickle or immerse in an alkaline deoxidizing bath such as HP ACIDSALT FLWET. 4. Cold water rinse. 5. Blackening bath:, 6.5 lbs/gal. (780 g/l), 285-300 o F (141-149 o C), 5-30 minutes. 6. Rinse in cold, running water. 7. OPTIONAL: For lacquering, paints or phenolic varnishes, dip for 3-5 minutes in 0.5-1.0 oz/gal. (3.8-7.5 g/l) chromic acid solution. 8. Cold water rinse.

Page 4 of 5 TYPICAL CYCLE (CONT.): 9. Dip in hot water to dry parts prior to lacquering or applying wax or oil finishes. 10. Immerse in DIS-PRO-TEC or HAVASOL EC-73 for 1-5 minutes. Agitate parts to aid in displacement of water from the surface of parts. This may be accomplished by raising and lowering baskets loaded with parts, rotation of barrels loaded with parts, while in the DIS-PRO-TEC / EC-73 etc. 10b. Immerse dry parts in water based lacquer, HP HAVA-LAC. Do not heat the solution. Allow parts to drip dry. SOLUTION REPLENISHMENT: Salts are lost by drag-out and water is lost by evaporation. Salts are added only to raise level of tank and boiling point. If solution level falls below working level, add water until solution boiling point is 285-290 F. Then add salts SLOWLY with stirring and maintain at a gentle boil or roll. TROUBLESHOOTING: Failure to Blacken: 1. Work has passivated in solutions that were not up to operating temperature. To correct, remove parts and rinse; dip in hydrochloric acid or sulfuric acid; rinse and re-blacken at proper temperature. 2. Steel can contain chrome or nickel, causing passive surfaces that do not blacken. 3. If solution is boiling and parts do not coat, check temperature with another thermometer since thermometers often get out of adjustment. 4. If work turns yellow or yellow-red in color, the solution is too high in temperature and concentration. Water should be added to lower the boiling point. 5. A yellow or yellow-red color can also be caused by improper rinsing of steel that has previously been pickled. An immersion in HP ACID SALT FLWET will remove the rust or iron residue from the parts. 6. If the bath becomes contaminated by iron salts from pickling, the resulting coating can have a reddish smut. For corrective action, refer to Purification Procedures below. 7. Contamination of the solution with copper causes work to turn a red color. For corrective action refer to the section of Purification Procedures below.

Page 5 of 5 PURIFICATION PROCEDURES: 1. Transfer solution to a separate tank and dilute to 50% strength with water. The iron contamination will precipitate out. 2. Add 1.0-1.5 pounds of sodium sulfide/1000 gallons of the 50% strength solution. Dissolve the sodium sulfide in water before additions. Copper sulfide will form as a black precipitate. 3. Allow to settle for 4-8 hours before transferring the top one-half of the solution back to the working tank. Clean the working tank of all sludge, scale and parts before returning solution. 4. Bring the working tank back to operating strength with fresh salts. The remaining CLEAR solution can be used as replenishing solution. This will reduce the salts consumed in purification to a minimum. ADDITIONAL AUXILIARY PRODUCTS: Havablack BOL Rectifier: (Iron, copper, and zinc control) Controls red smut due to metal build-up in aged baths. Havablack Wetting Agent: Improved drainage on parts from bath, improved rinsing. Havablack BOL Defoamer: Controls foam. Hydrochloric Acid or HP ACID SALT FLWET: For pickling or descaling, if needed. Havasol EC-73: Water soluble oil for parts. Dry Wax: Dry film corrosion inhibitor. WASTE DISPOSAL: Wastes must be tested using methods described in 40 CFR Part 261. It is the generator s responsibility to determine if the waste meets applicable definitions of hazardous wastes. Dispose of waste material according to Local, State, Federal, and Provincial Environmental Regulations. When empty, containers may still be hazardous because of product residue. All labeled hazard precautions must be observed. NON-WARRANTY: The data contained in this bulletin is believed by Haviland Products Company to be true, accurate and complete. However, since final methods of use for this product are in the hands of the customer and beyond our control, we cannot guarantee that the customer will obtain the results described in this bulletin. Haviland Products Company cannot assume any responsibility for the use of this product by the customer in any process, that may infringe the patents of third parties.