| Feature | Description |
|---|---|
| Dual-phase operation | Operates in both liquid and vapor phase for flexible system design |
| High thermal stability | Excellent thermal stability up to 400°C (750°F) |
| Manageable vapor pressure | Atmospheric boiling point 257.1°C (494.8°F) — controllable pressure in vapor-phase systems |
| Low viscosity at low temperature | Easy start-up and pumping (viscosity ≈ 5.00 mPa·s at 15°C) |
| Near-azeotropic behavior | Stable composition, easier maintenance |
| Clear to light-yellow synthetic fluid | Compatible with common system metals per Dow engineering guidance |
| Property | SI Units | English Units |
|---|---|---|
| Composition | Diphenyl Oxide / Biphenyl Blend | Diphenyl Oxide / Biphenyl Blend |
| Color | Clear to light yellow | Clear to light yellow |
| Freeze Point | 12.0°C | 53.6°F |
| Atmospheric Boiling Point | 257.1°C | 494.8°F |
| Flash Point¹ | 113°C | 236°F |
| Fire Point² | 118°C | 245°F |
| Autoignition Temperature³ | 599°C | 1110°F |
| Density at 25°C (75°F) | 1056 kg/m³ | 66.0 lb./ft.³ |
| Average Molecular Weight | 166.0 | 166.0 |
| Estimated Critical Temperature | 497°C | 927°F |
| Estimated Critical Pressure | 31.34 bar | 30.93 atm |
| Temperature | Specific Heat | Density | Thermal Conductivity | Viscosity |
|---|---|---|---|---|
| 15°C / 60°F | 1.558 kJ/kg·K | 1063.5 kg/m³ | 0.1395 W/m·K | 5.00 mPa·s |
| 205°C / 400°F | 2.093 kJ/kg·K | 902.5 kg/m³ | 0.1091 W/m·K | 0.38 mPa·s |
| 355°C / 670°F | 2.527 kJ/kg·K | 742.3 kg/m³ | 0.0851 W/m·K | 0.16 mPa·s |
| Temperature | Vapor Pressure | Latent Heat | Vapor Density |
|---|---|---|---|
| 255°C / 495°F | 0.97 bar | 297.4 kJ/kg | 3.831 kg/m³ |
| 405°C / 760°F | 11.32 bar | 201.7 kJ/kg | 45.17 kg/m³ |
| Operating Mode | Temperature Range |
|---|---|
| Liquid Phase | 15°C to 400°C (60°F to 750°F) |
| Vapor Phase | 257°C to 400°C (495°F to 750°F) |
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