Table 1 of § 86.513 -Gasoline Test Fuel Specifications
Item | Value | Procedure 1 |
Distillation Range: | ||
1. Initial boiling point, °C | 23.9-35.02 | ASTM D86 |
2. 10% point, °C | 48.9-57.2 | |
3. 50% point, °C | 93.3-110.0 | |
4. 90% point, °C | 148.9-162.8 | |
5. End point, °C | 212.8 maximum | |
Total aromatic hydrocarbon, volume % | 35 maximum | ASTM D1319 or ASTM D5769 |
Olefins, volume % 3 | 10 maximum | ASTM D1319 or ASTM D6550 |
Lead (organic), g/liter | 0.013 maximum | ASTM D3237 |
Phosphorous, g/liter | 0.0013 maximum | ASTM D3231 |
Sulfur, weight % | 0.008 maximum | ASTM D2622 |
Dry Vapor Pressure Equivalent (DVPE), kPa | 55.2 to 63.4 4 | ASTM D5191 |
1 Incorporated by reference, see § 86.1 .
2 For testing at altitudes above 1,219 m, the specified initial boiling point range is (23.9 to 40.6) °C.
3 ASTM D6550 prescribes measurement of olefin concentration in mass %. Multiply this result by 0.857 and round to the first decimal place to determine the olefin concentration in volume %.
4 For testing at altitudes above 1,219 m, the specified volatility range is 52 to 55 kPa. Calculate dry vapor pressure equivalent, DVPE, based on the measured total vapor pressure, pT, using the following equation:DVPE (kPa) = 0.956 ·pT-2.39 (orDVPE (psi) = 0.956 ·pT-0.347).DVPE is intended to be equivalent to Reid Vapor Pressure using a different test method.
Table 2 of § 86.513 -Natural Gas Test Fuel Specifications
Item | Value1 |
Methane, CH4 | Minimum, 89.0 mole percent. |
Ethane, C2H6 | Maximum, 4.5 mole percent. |
C3 and higher | Maximum, 2.3 mole percent. |
C6 and higher | Maximum, 0.2 mole percent. |
Oxygen | Maximum, 0.6 mole percent. |
Inert gases (sum of CO2 and N2) | Maximum, 4.0 mole percent. |
1 All parameters are based on the reference procedures in ASTM D1945 (incorporated by reference in § 86.1 ).
40 C.F.R. §86.513