#158 PURE SYNTHETIC COMPRESSOR OIL ISO 32 THROUGH ISO 220
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1 #8 PURE SYNTHETIC COMPRESSOR OIL ISO 2 THROUGH ISO 2 Pure Synthetic Compressor Oil is a full synthetic, non-detergent, ashless, non-zinc containing anti-wear, rust and oxidation inhibited premium quality oil that is specially formulated to satisfy the lubrication needs of oil flooded rotary vane and rotary screw compressors, screw type and reciprocating air compressors, pumps, vacuum pumps and blowers. Pure Synthetic is blended from the highest quality hydro-finished polyalphaolefin (PAO) synthetic base fluids available. These PAO base fluids provide Pure Synthetic Compressor Oil with the following advantages: 1. Excellent Resistance To Thermal Degradation Carbon, varnish and lacquer deposits due to high temperature operation are virtually eliminated. 2. Superior Oxidative Stability Any oil, as it is increasingly exposed to high temperature operation, undergoes the process of oxidation. This results in the oil s thickening and build-up of acidic components. Because of the PAO s uniform molecular structure, the process of oxidation is greatly reduced.. Extended Drain Intervals Because of the PAO s excellent resistance to thermal degradation and oxidation, Pure Synthetic Compressor Oil s service life is extended up to eight (8) times the normal service life of the conventional compressor oils. 4. Low Volatility The low volatility of the PAO s results in lower makeup requirements due to evaporation loss. 5. Less Oil Carry Over Due to its low volatility, there are fewer problems with the oil getting into air tools, instruments or even the production process. It also means there is less oil to remove in the air/oil separators and fewer air filter changes.. High Viscosity Index This results in a minimum change in viscosity with temperature. The adequate viscosity for proper bearing lubrication is provided regardless of temperature change.. Excellent Cold Temperature Starting and Pumpability. 8. Fire And Explosion Possibilities Are Greatly Reduced This is due to not only the PAO s extremely low carbon forming tendencies, but also to their relatively high flash, fire and auto ignition points. 9. Greater Hydrolytic Stability And Demulsibility Characteristics Since PAO s are non-polar; they absorb less water under high humidity conditions. They also separate condensed water much faster and more completely, thus resulting in the water being removed easily from the system. These properties result in extended bearing life, antiwear protection and improved rust and corrosion protection. 10. Excellent Operating Temperature Reduction PAO s have better specific heat valves (less available heat is absorbed) and better thermal conductivity that conventional air compressor oils. These combined properties help to reduce operating temperatures. 11. Compatibility With All Types Of Seals And Coatings Continued on Next Page TD-8 (Rev. 0/11)
2 Page 2 Combined with these polyalphaolefin synthetic base fluids is a highly specialized additive package which provides Pure Synthetic Compressor Oil with the following performance benefits: 1. Exceptional anti-wear protection 2. Extended compressor life. Extended bearing life 4. Enhanced thermal & oxidation stability 5. Superior hydrolytic stability. Excellent demulsibility characteristics. Excellent rust and corrosion protection 8. Excellent anti-foaming and air release properties 9. Reduced sludge, varnish and deposit formation 10. Enhanced fluid life 11. Enhanced seal life 12. Better heat transfer 1. Compatibility with zinc based fluids 14. Reduced system maintenance. Reduced downtime 1. Reduced power consumption Further blended into these polyalphaolefin synthetic base fluids and this highly specialized additive package is a proven frictional modifier, Micron Moly. Micron Moly is a liquid soluble type of moly that plates itself to the sliding and rubbing parts of the compressor. This plating action reduces friction between the moving parts, thus eliminating damaging frictional wear. This in turn also helps to reduce operating temperatures. Pure Synthetic Compressor Oil with its unique blend of polyalphaolefin base fluids, the highly specialized additive package and Micron Moly results in improved compressor efficiency. This improved compressor efficiency not only results in less downtime, reduced labor and material cost, but also in reduced energy consumption, which can further result in savings that could possibly represent many thousands of dollars each year per compressor. Pure Synthetic Compressor Oil meets and exceeds all the lubrication specifications of the various compressor manufacturers such as Joy, Ingersoll Rand, Quincy, Kaeser, Worthington, Atlas Copco, Gardner Denver and Sullair and meets the performance requirements for ISO-L-DAC, ISO-L-DAJ, ISO-L-DVA, and ISO-L-DVD CHANGE-OUT PROCEDURE WHEN SWITCHING FROM POLYALKYLENE GLYCOL AND POLYALKYLENE GLYCOL/POLYOL ESTER BLENDS COMPRESSOR FLUIDS This fluid procedure is designed for those compressors that are currently using a Polyalkylene Glycol or Polyalkylene Glycol/Polyol Ester blend such as Ingersoll Rand s SSR Ultra Coolant or Sullair s Sullube 2. This fluid procedure is designed for those compressors that are currently using a Polyalkylene Glycol or Polyalkylene Glycol/Polyol Ester blends are not compatible with petroleum or other type of synthetic base fluids, such as polyalphaolefin (PAO) and diester based compressor fluids. When petroleum based or synthetic based compressor fluids are mixed with a Polyalkylene Glycol or Polyalkylene Glycol/Polyol Ester blends the possibility of gelling of the products can occur.
3 Page Because of this possibility Schaeffer Mfg recommends that if a compressor application is being changed over from a Polyalkylene Glycol or Polyalkylene Glycol/Polyol Ester blend compressor fluid to #8 Pure Synthetic Compressor Fluid that the following procedure be strictly followed: Procedure Steps 1. Drain the compressor as completely as possible. Disconnect the air and fluid lines as completely as possible. Remove all oil filters and air/oil separators. Wipe out the air/oil separator bowl with a clean rag to remove any fluid residue. 2. Reconnect the lines and replace all the oil filters and air/oil separators with new elements. Charge the compressor with an either an inexpensive or the #8 Moly Pure Synthetic Compressor Fluid in the proper ISO Viscosity Grade. Run the compressor for 1-hour only.. Drain the compressor as completely as possible. Disconnect the air and fluid lines as completely as possible. Remove all oil filters and air/oil separators. Wipe out the air/oil separator bowl with a clean rag to remove any fluid residue. 4. Reconnect the lines and replace all the oil filters and air/oil separators with new elements. Charge the compressor with an either an inexpensive or the #8 Pure Synthetic Compressor Fluid in the proper ISO Viscosity Grade. Run the compressor for 1-hour only. 5. Repeat Step.. With the oil drain plug removed, begin filling the compressor slowly with #8 Pure Synthetic Compressor Fluid in the appropriate ISO Viscosity Grade. Allow the new fluid to push any remaining fluid out of the compressor. When new oil is seen, replace the drain plug and fill the compressor.. Start the compressor and top off the oil level. For additional change-out procedures involving other types of compressor fluids see Technical Bulletin 0800 COMPRESSOR CHANGEOVER PROCEDURES FOR #112 HTC, #254 HTC SUPREME AND #8 PURE SYNTHETIC COMPRESSOR OIL Typical Properties on Next Page
4 Page 4 TYPICAL PROPERTIES ISO Grade Specific Gravity Viscosity 100 F SUS (ASTM D-445) Viscosity 40 C cst (ASTM D-445) Viscosity 100 C cst (ASTM D-445) Viscosity Index Flash Point F/ C (ASTM D-92) 455 /25 40 / /25 50 /2 50 /2 45 /24 Fire Point F/ C (ASTM D-92) 5 /2 55 / /2. 50 /. 50 /. 485 /252 Auto Ignition Temp F/ C (ASTM D 25) 0 /88 50 /99 50 /99 50 /99 50 /99 50 /99 Pour Point F/ C (ASTM D-9) -5 /-54-5 /-54-5 /54-40 /-40-5 /- - /-2 Total Acid Number (ASTM D-44) Rotary Pressure Vessel Oxidation Test, (ASTM D-222) Minutes Foam Test (ASTM D-892) Sequence I 0/0 0/0 0/0 0/0 0/0 0/0 Sequence II 0/0 0/0 0/0 0/0 0/0 0/0 Sequence III 0/0 0/0 0/0 0/0 0/0 0/0 Air Release (ASTM D-42) Time F) % Evaporation Loss F (ASTM D-92) % Evaporation 00 F/1 C (ASTM D-2889) Four Ball EP (ASTM D-28) Weld Point, kg LWI, kg Aniline Point F/ C (ASTM D-11) 25 /1 /12 / / / /142
5 Page 5 TYPICAL PROPERTIES (continued) ISO Grade Rust Test (ASTM D-5) Procedure A (Distilled Water) Pass Pass Pass Pass Pass Pass Procedure B (Salt Water) Pass Pass Pass Pass Pass Pass Four Ball Wear Test (ASTM D-42) (1hr 1 F, 00 RPM, 40 kg) Scar Diameter, mm Average Coefficient of Friction Four Ball Test (ASTM D-42) (1hr 10 F, 00 RPM, kg) Scar Diameter, mm Falex Continuous Load (ASTM D-2) Failure Load, lbs Conradson Carbon Residue (ASTM D-9) % Residue Demulsibility (ASTM D-1401) Oil, Water, Emulsion Time Hydrolytic Stability (ASTM D-219) Copper Wt Loss (mg/cm 2 ) Acidity of Water Copper Strip Corrosion (ASTM D-10) 1a 1a 1a 1a 1a 1a Oxidation Stability Test (ASTM D-94) Hrs. to TAN of 2 +10, , , , , ,000 Continued on Next Page
6 Page TYPICAL PROPERTIES (continued) ISO Grade Sludge Tendencies (ASTM D-410) Total sludging Total Copper, mg Total Iron, mg Neutralization Number Thermal Stability (ASTM D-0) (Cincinnati Milacron Method 18hrs./ C, copper, steel catalyst) Sludge (mg/100ml) Condition of Copper Rod Condition of Iron Rod Denison THC Hybrid Pump Test Vane, mgs. Weight Loss Pins, mgs. Weight Loss Total Pin & Vane, mgs Wt Loss Vickers Vane Pump 5VQ25 Run 1 Ring wt. Loss Vane wt. Loss Total wt. Loss Run 2 Ring wt. Loss Vane wt. Loss Total wt. Loss Run Ring wt. Loss Vane wt. Loss Total wt. Loss Continued on Next Page
7 Page TYPICAL PROPERTIES (continued) ISO Grade Denison Filterability TP A Without Water, seconds With 2% Water, seconds AFNOR Filterability NF48-90 and NF Dry Phase, minutes Wet Phase, minutes
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