Table 2 of § 1065.710 -Test Fuel Specifications for Neat (E0) Gasoline
Property | Unit | Specification | Reference procedure a | |
General testing | Low-temperature testing | |||
Distillation Range: | ||||
Evaporated initial boiling point | °C | 24-35b | 24-36 | ASTM D86. |
10% evaporated | °C | 49-57 | 37-48 | |
50% evaporated | °C | 93-110 | 82-101 | |
90% evaporated | °C | 149-163 | 158-174 | |
Evaporated final boiling point | °C | Maximum, 213 | Maximum, 212 | |
Total Aromatic Hydrocarbons | volume % | Maximum, 35 | Maximum, 30.4 | ASTM D1319 or ASTM D5769. |
Olefinsc | volume % | Maximum, 10 | Maximum, 17.5 | ASTM D1319 or ASTM D6550. |
Lead | g/liter | Maximum, 0.013 | Maximum, 0.013 | ASTM D3237. |
Phosphorous | g/liter | Maximum, 0.0013 | Maximum, 0.005 | ASTM D3231. |
Total sulfur | mg/kg | Maximum, 80 | Maximum, 80 | ASTM D2622. |
Dry vapor pressure equivalentd | kPa | 60.0-63.4 b e | 77.2-81.4 | ASTM D5191. |
a Incorporated by reference; see § 1065.1010 . See § 1065.701(d) for other allowed procedures.
b For testing at altitudes above 1219 m, the specified initial boiling point range is (23.9 to 40.6) °C and the specified volatility range is (52.0 to 55.2) kPa.
c 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 %.
d Calculate dry vapor pressure equivalent, DVPE, based on the measured total vapor pressure, pT, in kPa using the following equation: DVPE(kPa) = 0.956·pT - 2.39 or DVPE(psi) = 0.956·pT - 0.347. DVPE is intended to be equivalent to Reid Vapor Pressure using a different test method.
e For testing unrelated to evaporative emissions, the specified range is (55.2 to 63.4) kPa.
40 C.F.R. §1065.710