The composition and properties of fuels listed in the ECN database are given in the tables below. Table 2.5.1 shows three oxygenated fuels (T70, GE80, and BM88) and five hydrocarbon fuels (NHPT, CET, HMN, CN80 and D2). T70 was originally used as a low-sooting fuel with a similar ignition delay as a cetane number 42.5 diesel reference fuel in order to facilitate optical diagnostics in the Sandia/Cummins optical engine (Dec, 1997). Similarly, the oxygenated fuels GE80 and BM88 had the same ignition delay as CN80 (cetane number 80) (Mueller, 2003). Ignition delays were matched only after adding a significant portion of an ignition enhancer, EHN, to BM88.
The fuel temperature (Tf) and density (ρf) at the fuel injector orifice are included in Table 2.5.1. Note that experiments were conducted at two fuel temperatures for D2 and CN80. This is because a fuel injector cooler was added after the initial D2 tests were completed. Table 2.5.1 shows that fuel density tends to decrease as temperature increases and that the fuel density of CN80 at 373 K is actually closer to the fuel density of D2 at 436 K. The fuel density can be important because fuel jets with the similar fuel density and pressure drop across the orifice will have similar jet momentum, which ultimately affects the mixing of the fuel jet. However, the fuel temperature difference had little effect on the soot level and location, or on the lift-off length and ignition delay (Pickett, 2003).
Table 2.5.1
Fuel Properties | T70 | GE80 | BM88 | NHPT | CET | HMN | CN80 | D2 | ||
Composition (by volume) | 70% TEOPa30% HMNb | 80% TPGMEc20% HMNb | 88% DBMd7% nC16e5% EHNf | 100% n-heptane | 100% nC16e or cetane | 100% HMNb | 76.5% nC16e 23.5% HMNb | 33.8% aromatics 65% paraffins 1.2% olefins | ||
ρf g[kg/m3] | 808 | 858 | 907 | 613 | 673 | 689 | 724 | 682 | 767 | 712 |
Tf[K] | 373 | 373 | 373 | 373 | 436 | 436 | 373 | 436 | 373 | 436 |
O2 h[wt%] | 21.5 | 25.8 | 26.5 | 0 | 0 | 0 | 0 | 0 | ||
Ωf i[%] | 7.8 | 10.0 | 10.9 | 0 | 0 | 0 | 0 | 0 | ||
Cetane Number | – | – | – | 56 | 100 | 15 | 80 | 46 | ||
AtomicH/(C-O)Ratio | 2.84 | 3.15 | 2.49 | 2.29 | 2.13 | 2.13 | 2.13 | 1.8 | ||
LHV j[MJ/kg] | 32.6 | 30.5 | 28.7 | 44.6 | 43.9 | 43.9 | 43.9 | 42.8 | ||
(A/F)stk | 11.1 | 10.2 | 9.5 | 15.4 | 15.2 | 15.2 | 15.2 | 14.7 |
b 2,2,4,4,6,8,8 heptamethyl-nonane (C16H34)c tri-propylene-glycol-methyl-ether (C10H22O4)
d dibutyl-maleate (C12H20O4)
e normal-hexadecane (C16H34)
f 2-ethylhexyl-nitrate (C8H17NO3)
g Density at a fuel temperature, Tf, and atmospheric pressure. The uncertainty is ±2 kg/m3.
h Oxygen weight percent
i Oxygen ratio of the fuel. See SAE 2003-01-1791.
j Lower Heating Value
k Stoichiometric air-to-fuel ratio by mass of the given fuel mixing with simulated ambient at 21% O2, 6.1% CO2, 3.6% H2O, 69.3% N2.
Table 2.5.2
Fuel Properties | D2 | JC | JW | JS | JP | SRx23 | nC12 |
#2 Diesel | JP-8 Chevron | Jet-A World Average | JP-8 Syntroleum GTL | JP-8 Penn St CTL | JP-8 surrogate | normal dodecane | |
T10 [°C] | 211 | 170 | 180 | 167 | 192 | - | - |
T90 [°C] | 315 | 240 | 251 | 254 | 243 | - | - |
T100 [°C] | 350 | 266 | 274 | 276 | 270 | 216 | 216 |
Cetane Index | 47 | 39 | ? | ? | ? | - | - |
Cetane Number | 46 | 38 | 46 | 62 | 34 | - | 87 |
Low. Heat. Value [MJ/kg] | 42.975 | 43.228 | 43.2 | 44.138 | 42.801 | 43.33 | 44.17 |
Density at 15°C [kg/m3] | 843 | 812 | 806 | 755.9 | 870.2 | 775.3 | 752.1 |
Aromatics Vol. % | 27 | 11 | 19 | 0.4 | 1.9 | 23 | 0 |
H2 mass % | 13.28 | 13.9 | ? | 15.4 | 13.2 | - | 15.3 |
Sulfur [ppm] | 9 | 1 | 0 | 0 | 0 | 0 | 0 |
Kin. Visc. (-20°C) [mm2/s] | - | 4.465 | 5.2 | 4.6 | 7.5 | - | 4.7 |
Kin. Visc. (40°C) [mm2/s] | 2.35 | ~ 1.4 (est.) | - | - | - | - | 1.5 |
Freeze Point [°C] | - | -57 | -48 | -51 | -65 | - | -10 |
Flash Point [°C] | 73 | 47 | 51 | 45 | 61 | - | 83 |
Table 2.5.3
Fuel Properties | G15 | G33 | G50 | G50A | MD |
MW [g/mol] | 223 | 219 | 216 | 169 | 186 |
Density [g/cm3] | 800 | 835 | 869 | 859 | 871 |
Boiling pointa [oC] | 287 | 287 | 287 | 287 | 224 |
LHV [MJ/kg] | 41.5 | 38.5 | 35.8 | 35.5 | 37.5 |
DCN (FIT) | 108 | 110 | 112 | 88 | 48 |
O2 ratio (Ω) [%] | 1.9 | 4.3 | 6.5 | 5.0 | 6.1 |
(C/H)eff | 0.46 | 0.45 | 0.44 | 0.53 | 0.47 |
Please refer to Manin, 2014, "Effects of Oxygenated Fuels on Combustion and Soot Formation/Oxidation Processes" for a more detailed description of the fuels in Table 2.5.3.
Table 2.5.4
Fuel Properties | Soy methyl ester (SME) |
Density at 288 K (kg.m-3) | 877 |
Density expected @ 373 K (kg.m-3) | 823 |
Kinematic viscosity at 313 K (mm2.s-1) | 3.98 |
Lower heating value (MJ.kg-1) | 37.4 |
Aromatics (Volume %) | 0 |
C/H and C/O mass ratios | 6.48/7.05 |
Cetane number | 51 |
Zstoich (15% O>sub>2) | 0.054 |
Zsoota | 0.105 |
Please refer to Nerva, 2012 for a more detailed description of the fuels in Table 2.5.4.
Table 2.5.5
Constituent name | Constituent abbreviation | Chemical formula | % |
Methyl palmitate | C16:0 | C17H34O2 | 11 |
Methyl stearate | C18:0 | C19H38O2 | 4.0 |
Methyl oleate | C18:1 | C19H36O2 | 25 |
Methyl linoleate | C18:2 | C19H34O2 | 53 |
Methyl linolenate | C18:3 | C19H32O2 | 7 |
Please refer to Nerva, 2012 for a more detailed description of the fuels in Table 2.5.5.
Table 2.5.6
Fuel Properties | Oxymethylene Ethers (OME) |
Density (kg/m3 (T = 15 °C)) | 1057.10 |
Viscosity (mm2/s (T = 40 °C)) | 1.08 |
Cetane Number | 68.6 |
Lubricity (μm) | 320 |
Flash Point (°C) | 65 |
Lower Heating Value (MJ/kg) | 19.26 |
Initial Boiling Point (°C) | 144.40 |
Final Boiling Point (°C) | 242.4 |
Total Contaminations (mg/kg) | <1 |
Carbon Content (% [m/m]) | 43 |
Hydrogen Content (% [m/m]) | 8.53 |
Oxygen Content (% [m/m]) | 46.4 |
(A/F)st at 21% of O2 | 5.89:1 |
(A/F)st at 15% of O2 | 8.18:1 |
Please refer to Wiesmann, 2022 for a more detailed description of the OME fuel in Table 2.5.6.
Table 2.5.7
Molecule | Content [wt %] |
OME1 | 0.01 |
OME2 | <0.01 |
OME3 | 57.90 |
OME4 | 28.87 |
OME5 | 10.07 |
OME6 | 1.91 |
Please refer to Wiesmann, 2022 for a more detailed description of the OME fuel in Table 2.5.7.
Spray G Fuels:
Gasoline Fuels Used with Spray G - Composites
Composite Fuels: | Composition by Volume: | Research Octane Number [RON]: | Ethanol Content [Vol. %]: | Distillation, 10% [°C]: | Distillation, 90% [°C]: | Aromatic Content [Vol. %]: | Olefin Content [Vol. %]: | Density @ 15.56 °C [KG/L]: | Net Heat of Combustion [MJ/KG]: | H/C Ratio [Mole/Mole]: | O/C Ratio [Mole/Mole]: |
E00 | 36% n-pentane, 46% iso-octane, 18% n-undecane | - | - | - | - | - | - | - | - | - | - |
E20 | 80% E00, 20% ethanol | - | - | - | - | - | - | - | - | - | - |
E85 | 15% E00, 85% ethanol | - | - | - | - | - | - | - | - | - | - |
RD-587 | - | 92.0 | 9.88 | 57.8 | 157.9 | 19.6 | 5.0 | 0.748 | 41.61 | 2.086 | 0.033 |
HF2021 | - | 91.2 | 9.9 | 53.2 | 158.9 | 23.3 | - (5.0 Weight %) | 0.7461 | 41.884 | 1.974 | - |
Gasoline Fuels Used with Spray G - Pure
Pure Fuels: | Chemical Formula: | Density [kg/m3]: | Normal Boiling Point [°C]: | Enthalpy of Vaporization [kJ/kg]: | Octane Number [RON]: |
iso-octane | C8H18 | 690.3 | 99.2 | 308.4 | 100 |
n-pentane | C5H12 | 621.7 | 36.1 | 365.1 | 61.7 |
n-undecane | C11H24 | 737.6 | 195.9 | 364.2 | - |
ethanol | C2H6O | 789.1 | 78.9 | 838 | 113 |