| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.3020; 0.3040] |
|
|
| ω | 0.3020 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.3024 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.3040 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.3020 | KDB | |
| PAff | [800.00; 802.90] | kJ/mol |
|
| PAff | 802.90 | kJ/mol | NIST |
| PAff | 800.00 | kJ/mol | NIST |
| Tig | 799.26 | K | KDB |
| BasG | [774.50; 779.40] | kJ/mol |
|
| BasG | 779.40 | kJ/mol | NIST |
| BasG | 774.50 | kJ/mol | NIST |
| ΔcH°solid | [-5182.70; -5141.61] | kJ/mol |
|
| ΔcH°solid | -5150.09 | kJ/mol | NIST |
| ΔcH°solid | -5153.90 ± 5.10 | kJ/mol | NIST |
| ΔcH°solid | -5165.50 ± 0.78 | kJ/mol | NIST |
| ΔcH°solid | -5156.40 ± 0.60 | kJ/mol | NIST |
| ΔcH°solid | -5156.15 ± 0.92 | kJ/mol | NIST |
| ΔcH°solid | -5147.20 ± 3.10 | kJ/mol | NIST |
| ΔcH°solid | -5156.90 ± 1.60 | kJ/mol | NIST |
| ΔcH°solid | -5143.18 | kJ/mol | NIST |
| ΔcH°solid | -5160.80 | kJ/mol | NIST |
| ΔcH°solid | -5141.61 | kJ/mol | NIST |
| ΔcH°solid | -5147.40 ± 1.50 | kJ/mol | NIST |
| ΔcH°solid | -5156.82 | kJ/mol | NIST |
| ΔcH°solid | -5152.72 | kJ/mol | NIST |
| ΔcH°solid | -5151.20 ± 0.20 | kJ/mol | NIST |
| ΔcH°solid | -5151.90 ± 0.20 | kJ/mol | NIST |
| ΔcH°solid | Outlier -5179.80 | kJ/mol | NIST |
| ΔcH°solid | -5166.80 ± 0.13 | kJ/mol | NIST |
| ΔcH°solid | Outlier -5182.70 | kJ/mol | NIST |
| μ | [0.00; 0.00] | debye |
|
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 0.00 | debye | KDB |
| EA | [-0.20; 0.15] | eV |
|
| EA | -0.20 | eV | NIST |
| EA | -0.18 | eV | NIST |
| EA | -0.20 ± 0.05 | eV | NIST |
| EA | -0.19 | eV | NIST |
| EA | 0.14 ± 0.05 | eV | NIST |
| EA | 0.13 ± 0.04 | eV | NIST |
| EA | 0.15 ± 0.01 | eV | NIST |
| LFL | 0.90 | % in Air | KDB |
| UFL | 5.90 | % in Air | KDB |
| Tflash,cc | 360.93 | K | KDB |
| Tflash,oc | 352.04 | K | KDB |
| ΔfG° | [223.70; 224.08] | kJ/mol |
|
| ΔfG° | 224.08 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 223.70 | kJ/mol | KDB |
| Δc,grossH | 5156.95 | kJ/mol | KDB |
| Δc,netH | 4980.885 | kJ/mol | KDB |
| ΔfH°gas | [141.60; 160.10] | kJ/mol |
|
| ΔfH°gas | 150.58 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | 151.10 | kJ/mol | KDB |
| ΔfH°gas | 150.60 ± 1.50 | kJ/mol | NIST |
| ΔfH°gas | Outlier 160.10 | kJ/mol | NIST |
| ΔfH°gas | 150.90 | kJ/mol | NIST |
| ΔfH°gas | 150.60 ± 1.10 | kJ/mol | NIST |
| ΔfH°gas | 141.60 | kJ/mol | NIST |
| ΔfH°gas | 151.70 ± 1.90 | kJ/mol | NIST |
| ΔfH°gas | 145.60 | kJ/mol | NIST |
| ΔfH°solid | [68.70; 87.20] | kJ/mol |
|
| ΔfH°solid | 78.00 ± 1.50 | kJ/mol | NIST |
| ΔfH°solid | 87.20 ± 1.50 | kJ/mol | NIST |
| ΔfH°solid | 78.00 ± 0.60 | kJ/mol | NIST |
| ΔfH°solid | 77.70 ± 1.00 | kJ/mol | NIST |
| ΔfH°solid | 68.70 ± 3.10 | kJ/mol | NIST |
| ΔfH°solid | 78.50 ± 1.60 | kJ/mol | NIST |
| ΔfH°solid | 72.72 | kJ/mol | NIST |
| ΔfusH° | [17.83; 19.55] | kJ/mol |
|
| ΔfusH° | 19.07 | kJ/mol | Odd even effect in melting properties of 12 alkane-a,x-diamides |
| ΔfusH° | 19.55 | kJ/mol | Solid liquid equilibria and purity determination for binary n-alkane + naphthalene systems |
| ΔfusH° | 19.55 | kJ/mol | Solid-Liquid Equilibria of Naphthalene + Alkanediamine Mixtures |
| ΔfusH° | 17.83 | kJ/mol | Measurement and Correlation for Solubilities of Naphthalene in Acetone, Toluene, Xylene, Ethanol, Heptane, and 1-Butanol |
| ΔsubH° | [64.00; 73.20] | kJ/mol |
|
| ΔsubH° | 72.60 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 70.40 | kJ/mol | NIST |
| ΔsubH° | 72.30 ± 0.40 | kJ/mol | NIST |
| ΔsubH° | 72.60 ± 0.10 | kJ/mol | NIST |
| ΔsubH° | 72.40 ± 0.70 | kJ/mol | NIST |
| ΔsubH° | 72.50 | kJ/mol | NIST |
| ΔsubH° | 73.00 ± 0.25 | kJ/mol | NIST |
| ΔsubH° | 73.00 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 72.00 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 72.10 ± 0.25 | kJ/mol | NIST |
| ΔsubH° | 72.90 | kJ/mol | NIST |
| ΔsubH° | 72.70 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 73.20 ± 3.10 | kJ/mol | NIST |
| ΔsubH° | 73.20 | kJ/mol | NIST |
| ΔsubH° | Outlier 64.00 | kJ/mol | NIST |
| ΔsubH° | 66.50 ± 1.70 | kJ/mol | NIST |
| ΔsubH° | 67.00 ± 2.00 | kJ/mol | NIST |
| ΔvapH° | [53.40; 60.30] | kJ/mol |
|
| ΔvapH° | 54.60 | kJ/mol | NIST |
| ΔvapH° | 60.30 ± 1.10 | kJ/mol | NIST |
| ΔvapH° | 53.40 | kJ/mol | NIST |
| ΔvapH° | 56.60 | kJ/mol | NIST |
| IE | [8.08; 8.31] | eV |
|
| IE | 8.14 ± 0.00 | eV | NIST |
| IE | 8.12 ± 0.02 | eV | NIST |
| IE | 8.14 ± 0.00 | eV | NIST |
| IE | 8.12 ± 0.01 | eV | NIST |
| IE | 8.14 | eV | NIST |
| IE | 8.14 ± 0.00 | eV | NIST |
| IE | 8.08 ± 0.05 | eV | NIST |
| IE | 8.15 | eV | NIST |
| IE | 8.15 | eV | NIST |
| IE | 8.12 | eV | NIST |
| IE | 8.15 | eV | NIST |
| IE | 8.13 | eV | NIST |
| IE | 8.15 | eV | NIST |
| IE | 8.16 ± 0.03 | eV | NIST |
| IE | 8.11 ± 0.01 | eV | NIST |
| IE | 8.15 ± 0.01 | eV | NIST |
| IE | 8.13 | eV | NIST |
| IE | 8.14 | eV | NIST |
| IE | 8.12 ± 0.05 | eV | NIST |
| IE | 8.14 ± 0.01 | eV | NIST |
| IE | Outlier 8.25 ± 0.01 | eV | NIST |
| IE | 8.15 | eV | NIST |
| IE | 8.16 | eV | NIST |
| IE | 8.08 | eV | NIST |
| IE | 8.10 | eV | NIST |
| IE | 8.10 | eV | NIST |
| IE | 8.12 ± 0.01 | eV | NIST |
| IE | 8.14 ± 0.02 | eV | NIST |
| IE | 8.09 | eV | NIST |
| IE | 8.15 | eV | NIST |
| IE | 8.15 ± 0.02 | eV | NIST |
| IE | 8.18 ± 0.03 | eV | NIST |
| IE | 8.15 | eV | NIST |
| IE | Outlier 8.31 ± 0.03 | eV | NIST |
| IE | 8.15 | eV | NIST |
| IE | 8.15 | eV | NIST |
| log10WS | [-3.62; -3.60] |
|
|
| log10WS | -3.62 | Aq. Solubility Prediction | |
| log10WS | -3.60 | Estimated Solubility | |
| logPoct/wat | 2.840 | Crippen Calculated Property | |
| McVol | 108.540 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [3961.81; 4590.50] | kPa |
|
| Pc | 4130.00 | kPa | Critical Point and Vapor Pressure Measurements for Seven Compounds by a Low Residence Time Flow Method |
| Pc | 4050.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value |
| Pc | 4053.00 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4050.67 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 4050.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 4050.00 | kPa | KDB |
| Pc | 4050.00 ± 50.00 | kPa | NIST |
| Pc | 4105.00 ± 80.00 | kPa | NIST |
| Pc | 4097.60 ± 0.40 | kPa | NIST |
| Pc | 4064.50 ± 0.40 | kPa | NIST |
| Pc | 4064.50 ± 0.40 | kPa | NIST |
| Pc | Outlier 4590.50 ± 0.45 | kPa | NIST |
| Pc | 4051.00 ± 6.00 | kPa | NIST |
| Pc | 4120.00 ± 98.07 | kPa | NIST |
| Pc | 3961.81 ± 101.32 | kPa | NIST |
| Pc | 3985.11 ± 101.32 | kPa | NIST |
| Pc | 3978.02 ± 101.32 | kPa | NIST |
| Ptriple | [0.99; 1.00] | kPa |
|
| Ptriple | 0.99 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 1.00 | kPa | KDB |
| ρc | [314.02; 320.04] | kg/m3 |
|
| ρc | 315.30 ± 6.41 | kg/m3 | NIST |
| ρc | 320.04 ± 10.00 | kg/m3 | NIST |
| ρc | 314.02 ± 5.13 | kg/m3 | NIST |
| ρc | 314.79 ± 5.13 | kg/m3 | NIST |
| ρc | 320.04 ± 10.00 | kg/m3 | NIST |
| Inp | [1137.00; 1225.00] |
|
|
| Inp | 1194.25 | NIST | |
| Inp | Outlier 1210.48 | NIST | |
| Inp | 1189.91 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1180.61 | NIST | |
| Inp | 1159.62 | NIST | |
| Inp | 1160.84 | NIST | |
| Inp | 1161.23 | NIST | |
| Inp | 1160.72 | NIST | |
| Inp | Outlier 1214.10 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1171.80 | NIST | |
| Inp | 1162.56 | NIST | |
| Inp | 1167.07 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1196.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1204.00 | NIST | |
| Inp | Outlier 1213.70 | NIST | |
| Inp | 1139.00 | NIST | |
| Inp | 1139.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1167.40 | NIST | |
| Inp | 1153.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1183.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1188.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | Outlier 1219.00 | NIST | |
| Inp | 1145.00 | NIST | |
| Inp | 1183.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1151.80 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1161.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1151.80 | NIST | |
| Inp | 1196.00 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1139.40 | NIST | |
| Inp | 1142.10 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1209.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1158.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | Outlier 1225.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Inp | 1190.90 | NIST | |
| Inp | 1196.00 | NIST | |
| Inp | 1199.20 | NIST | |
| Inp | 1199.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1172.40 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1171.50 | NIST | |
| Inp | 1179.70 | NIST | |
| Inp | 1183.40 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1203.20 | NIST | |
| Inp | 1183.00 | NIST | |
| Inp | Outlier 1218.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1195.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1177.30 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1163.00 | NIST | |
| Inp | 1148.00 | NIST | |
| Inp | 1161.60 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1171.50 | NIST | |
| Inp | 1179.70 | NIST | |
| Inp | 1183.40 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1158.51 | NIST | |
| Inp | 1160.26 | NIST | |
| Inp | 1158.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1187.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1144.00 | NIST | |
| Inp | 1146.97 | NIST | |
| Inp | 1155.82 | NIST | |
| Inp | 1161.44 | NIST | |
| Inp | 1178.80 | NIST | |
| Inp | 1188.47 | NIST | |
| Inp | 1194.63 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1199.00 | NIST | |
| Inp | 1155.10 | NIST | |
| Inp | 1156.84 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1157.10 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1168.74 | NIST | |
| Inp | 1166.21 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | Outlier 1211.00 | NIST | |
| Inp | 1159.35 | NIST | |
| Inp | 1184.04 | NIST | |
| Inp | 1179.60 | NIST | |
| Inp | 1199.00 | NIST | |
| Inp | 1207.00 | NIST | |
| Inp | 1183.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1165.73 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1161.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1188.00 | NIST | |
| Inp | 1187.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1196.00 | NIST | |
| Inp | 1153.00 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1182.60 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1200.00 | NIST | |
| Inp | 1196.00 | NIST | |
| Inp | 1183.00 | NIST | |
| Inp | 1183.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1187.00 | NIST | |
| Inp | 1158.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1187.87 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1142.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1153.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1163.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1210.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1187.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1158.00 | NIST | |
| Inp | 1183.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1139.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | Outlier 1137.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | Outlier 1215.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | Outlier 1212.00 | NIST | |
| Inp | 1139.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | Outlier 1222.00 | NIST | |
| Inp | 1139.00 | NIST | |
| Inp | 1210.00 | NIST | |
| Inp | Outlier 1220.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1183.70 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1188.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1161.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1179.70 | NIST | |
| Inp | Outlier 1218.00 | NIST | |
| Inp | 1195.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1161.60 | NIST | |
| Inp | 1183.40 | NIST | |
| Inp | 1158.51 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1146.97 | NIST | |
| Inp | 1194.63 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1166.21 | NIST | |
| Ip | [1694.00; 1792.00] |
|
|
| Ip | 1707.00 | NIST | |
| Ip | 1762.00 | NIST | |
| Ip | 1709.00 | NIST | |
| Ip | Outlier 1791.00 | NIST | |
| Ip | 1743.00 | NIST | |
| Ip | 1731.00 | NIST | |
| Ip | 1749.00 | NIST | |
| Ip | 1765.00 | NIST | |
| Ip | 1719.00 | NIST | |
| Ip | 1749.00 | NIST | |
| Ip | 1747.00 | NIST | |
| Ip | 1747.00 | NIST | |
| Ip | 1715.00 | NIST | |
| Ip | 1748.00 | NIST | |
| Ip | 1764.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1748.00 | NIST | |
| Ip | 1748.00 | NIST | |
| Ip | 1740.00 | NIST | |
| Ip | 1751.00 | NIST | |
| Ip | 1749.00 | NIST | |
| Ip | 1718.00 | NIST | |
| Ip | 1762.00 | NIST | |
| Ip | 1727.00 | NIST | |
| Ip | 1748.00 | NIST | |
| Ip | 1754.00 | NIST | |
| Ip | 1707.00 | NIST | |
| Ip | 1749.00 | NIST | |
| Ip | Outlier 1792.00 | NIST | |
| Ip | 1706.00 | NIST | |
| Ip | 1703.00 | NIST | |
| Ip | 1730.00 | NIST | |
| Ip | 1750.00 | NIST | |
| Ip | 1712.00 | NIST | |
| Ip | 1749.00 | NIST | |
| Ip | 1724.00 | NIST | |
| Ip | Outlier 1789.00 | NIST | |
| Ip | 1698.00 | NIST | |
| Ip | 1749.00 | NIST | |
| Ip | 1769.00 | NIST | |
| Ip | 1732.00 | NIST | |
| Ip | 1733.00 | NIST | |
| Ip | 1706.00 | NIST | |
| Ip | 1707.00 | NIST | |
| Ip | 1748.00 | NIST | |
| Ip | 1755.00 | NIST | |
| Ip | 1765.00 | NIST | |
| Ip | 1765.00 | NIST | |
| Ip | 1731.00 | NIST | |
| Ip | 1757.00 | NIST | |
| Ip | 1698.00 | NIST | |
| Ip | 1698.00 | NIST | |
| Ip | 1728.00 | NIST | |
| Ip | 1745.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1765.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1699.00 | NIST | |
| Ip | 1694.00 | NIST | |
| Ip | 1713.00 | NIST | |
| Ip | 1729.00 | NIST | |
| Ip | 1724.00 | NIST | |
| Ip | 1701.00 | NIST | |
| Ip | 1714.00 | NIST | |
| Ip | 1714.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1723.00 | NIST | |
| Ip | 1734.00 | NIST | |
| Ip | 1765.00 | NIST | |
| Ip | 1730.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1763.00 | NIST | |
| Ip | 1765.00 | NIST | |
| Ip | 1765.00 | NIST | |
| Ip | 1765.00 | NIST | |
| Ip | 1762.00 | NIST | |
| Ip | 1739.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1739.00 | NIST | |
| Ip | 1709.00 | NIST | |
| Ip | 1720.00 | NIST | |
| Ip | 1749.00 | NIST | |
| Ip | 1750.00 | NIST | |
| S°liquid | 217.59 | J/mol×K | NIST |
| S°solid,1 bar | [162.84; 167.40] | J/mol×K |
|
| S°solid,1 bar | 167.40 | J/mol×K | NIST |
| S°solid,1 bar | 162.84 | J/mol×K | NIST |
| S°solid,1 bar | 166.86 | J/mol×K | NIST |
| S°solid,1 bar | 166.90 | J/mol×K | NIST |
| Tboil | [396.15; 492.23] | K |
|
| Tboil | 491.16 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 491.14 | K | KDB |
| Tboil | 491.20 | K | NIST |
| Tboil | 491.15 ± 0.50 | K | NIST |
| Tboil | 491.15 ± 0.60 | K | NIST |
| Tboil | 491.15 ± 0.30 | K | NIST |
| Tboil | Outlier 396.15 ± 8.00 | K | NIST |
| Tboil | 491.05 ± 1.00 | K | NIST |
| Tboil | 491.11 ± 0.25 | K | NIST |
| Tboil | 492.23 ± 0.25 | K | NIST |
| Tboil | 491.20 ± 0.50 | K | NIST |
| Tboil | 491.20 ± 0.60 | K | NIST |
| Tboil | 483.15 ± 8.33 | K | NIST |
| Tc | [741.35; 784.85] | K |
|
| Tc | 748.40 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value |
| Tc | 748.40 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 748.43 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 748.40 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 748.40 | K | KDB |
| Tc | 748.40 ± 0.50 | K | NIST |
| Tc | 748.40 ± 0.50 | K | NIST |
| Tc | 749.45 ± 0.07 | K | NIST |
| Tc | 748.85 ± 0.07 | K | NIST |
| Tc | 746.55 ± 0.07 | K | NIST |
| Tc | Outlier 784.85 ± 0.07 | K | NIST |
| Tc | 748.35 ± 0.15 | K | NIST |
| Tc | 746.60 ± 2.00 | K | NIST |
| Tc | 748.00 ± 0.30 | K | NIST |
| Tc | 748.35 ± 0.30 | K | NIST |
| Tc | 753.20 ± 6.00 | K | NIST |
| Tc | 749.70 ± 2.00 | K | NIST |
| Tc | 741.35 ± 1.00 | K | NIST |
| Tc | 741.35 ± 1.00 | K | NIST |
| Tfus | [348.15; 356.90] | K |
|
| Tfus | 352.30 | K | Vaporization enthalpy and vapor pressure of (-) Ambroxide and Galaxolide by correlation gas chromatography |
| Tfus | 353.40 | K | The use of organic calibration standards in the enthalpy calibration of differential scanning calorimeters |
| Tfus | Outlier 356.90 | K | Solubility of Naphthalene in Isobutyl Acetate, n-Butyric Acid, Ethyl Acetate, N-Methyl Pyrrolidone, N,N-Dimethylformamide, and Tetrahydrofuran |
| Tfus | 353.35 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 353.43 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 353.30 | K | KDB |
| Tfus | 353.43 | K | Aq. Solubility Prediction |
| Tfus | 353.15 ± 1.00 | K | NIST |
| Tfus | 353.65 ± 0.20 | K | NIST |
| Tfus | 353.25 ± 0.50 | K | NIST |
| Tfus | 353.55 ± 0.30 | K | NIST |
| Tfus | 353.30 ± 0.30 | K | NIST |
| Tfus | 353.43 ± 0.01 | K | NIST |
| Tfus | 353.40 ± 0.30 | K | NIST |
| Tfus | 354.00 ± 0.10 | K | NIST |
| Tfus | 353.80 ± 0.20 | K | NIST |
| Tfus | 352.20 ± 0.80 | K | NIST |
| Tfus | 353.35 ± 0.30 | K | NIST |
| Tfus | 353.45 ± 0.30 | K | NIST |
| Tfus | 353.25 ± 0.05 | K | NIST |
| Tfus | 353.45 ± 0.30 | K | NIST |
| Tfus | 353.43 ± 0.05 | K | NIST |
| Tfus | 353.44 ± 0.01 | K | NIST |
| Tfus | 353.35 ± 0.30 | K | NIST |
| Tfus | 353.43 ± 0.03 | K | NIST |
| Tfus | 353.10 ± 0.80 | K | NIST |
| Tfus | 353.41 ± 0.03 | K | NIST |
| Tfus | 353.41 ± 0.03 | K | NIST |
| Tfus | 353.44 ± 0.02 | K | NIST |
| Tfus | 353.42 ± 0.03 | K | NIST |
| Tfus | 353.44 ± 0.02 | K | NIST |
| Tfus | 353.00 ± 2.00 | K | NIST |
| Tfus | 353.15 ± 0.50 | K | NIST |
| Tfus | 353.00 ± 1.00 | K | NIST |
| Tfus | 353.00 ± 1.50 | K | NIST |
| Tfus | Outlier 348.15 ± 2.00 | K | NIST |
| Tfus | 353.20 ± 0.30 | K | NIST |
| Tfus | 353.00 ± 1.00 | K | NIST |
| Tfus | 353.27 ± 0.05 | K | NIST |
| Tfus | 353.40 ± 0.20 | K | NIST |
| Tfus | 354.55 ± 1.00 | K | NIST |
| Tfus | 353.00 ± 2.00 | K | NIST |
| Tfus | 353.40 ± 0.20 | K | NIST |
| Tfus | 353.20 ± 0.15 | K | NIST |
| Tfus | 353.00 ± 1.50 | K | NIST |
| Tfus | 352.55 ± 0.30 | K | NIST |
| Tfus | 352.65 ± 0.30 | K | NIST |
| Tfus | 352.55 ± 0.30 | K | NIST |
| Tfus | 352.45 ± 0.30 | K | NIST |
| Tfus | 352.55 ± 0.30 | K | NIST |
| Tfus | 353.05 ± 0.30 | K | NIST |
| Tfus | 353.00 ± 1.00 | K | NIST |
| Tfus | 353.15 ± 0.20 | K | NIST |
| Tfus | 353.21 ± 0.15 | K | NIST |
| Tfus | 353.20 ± 1.00 | K | NIST |
| Tfus | 353.21 ± 0.03 | K | NIST |
| Tfus | 353.20 ± 0.03 | K | NIST |
| Tfus | 353.24 ± 0.03 | K | NIST |
| Tfus | 353.13 ± 0.20 | K | NIST |
| Tfus | 353.25 ± 0.30 | K | NIST |
| Tfus | 353.24 ± 0.15 | K | NIST |
| Tfus | 352.55 ± 0.30 | K | NIST |
| Tfus | 353.10 ± 0.25 | K | NIST |
| Tfus | 352.59 ± 5.55 | K | NIST |
| Ttriple | [353.30; 355.04] | K |
|
| Ttriple | Outlier 355.04 | K | Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K |
| Ttriple | 353.43 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 353.42 | K | KDB |
| Ttriple | 353.40 ± 0.02 | K | NIST |
| Ttriple | 353.30 ± 0.01 | K | NIST |
| Ttriple | 353.37 ± 0.01 | K | NIST |
| Ttriple | 353.41 ± 0.01 | K | NIST |
| Ttriple | 353.42 ± 0.07 | K | NIST |
| Ttriple | 353.43 ± 0.05 | K | NIST |
| UQi | 3.37 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.92 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.407; 0.410] | m3/kmol |
|
| Vc | 0.407 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value |
| Vc | 0.410 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.407 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.407 | m3/kmol | KDB |
| Vc | 0.407 | m3/kmol | NIST |
| Vc | 0.409 ± 0.060 | m3/kmol | NIST |
| Zc | [0.2648980; 0.2650000] |
|
|
| Zc | 0.2650000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value | |
| Zc | 0.2650000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2648980 | KDB | |
| Zra | 0.26 | ChemSep v8.3 pure component data Compiled value |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [83.85; 374.06] | J/mol×K | [200.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 4.98310e+01 | |||
| Coefficient B | -5.47920e+02 | |||
| Coefficient C | 6.29324e+00 | |||
| Coefficient D | -1.39990e-04 | |||
| Coefficient E | 2.82080e-08 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 83.85 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 155.22 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 215.63 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 260.60 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 293.78 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 318.64 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 337.65 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 352.51 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 364.37 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 374.06 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [218.19; 287.73] | J/mol×K | [353.43; 491.14] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.49170e+02 | |||
| Coefficient B | 5.79650e+02 | |||
| Coefficient C | -3.09256e+00 | |||
| Coefficient D | 2.16240e-02 | |||
| Coefficient E | -1.56570e-05 | |||
| Temperature range, min. | 353.43 | |||
| Temperature range, max. | 491.14 | |||
| Cp,liquid | 218.19 | J/mol×K | 353.43 | Calculated Property |
| Cp,liquid | 224.67 | J/mol×K | 368.73 | Calculated Property |
| Cp,liquid | 231.61 | J/mol×K | 384.03 | Calculated Property |
| Cp,liquid | 238.95 | J/mol×K | 399.33 | Calculated Property |
| Cp,liquid | 246.66 | J/mol×K | 414.63 | Calculated Property |
| Cp,liquid | 254.65 | J/mol×K | 429.94 | Calculated Property |
| Cp,liquid | 262.85 | J/mol×K | 445.24 | Calculated Property |
| Cp,liquid | 271.16 | J/mol×K | 460.54 | Calculated Property |
| Cp,liquid | 279.50 | J/mol×K | 475.84 | Calculated Property |
| Cp,liquid | 287.73 | J/mol×K | 491.14 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0009202; 0.0001751] | Pa×s | [353.15; 673.56] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -8.21510e+00 | |||
| Coefficient B | 1.33820e+03 | |||
| Coefficient C | -4.65920e-01 | |||
| Coefficient D | 1.35000e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 353.15 | |||
| Temperature range, max. | 673.56 | |||
| η | 0.0009202 | Pa×s | 353.15 | Calculated Property |
| η | 0.0006445 | Pa×s | 388.75 | Calculated Property |
| η | 0.0004820 | Pa×s | 424.35 | Calculated Property |
| η | 0.0003795 | Pa×s | 459.95 | Calculated Property |
| η | 0.0003114 | Pa×s | 495.55 | Calculated Property |
| η | 0.0002643 | Pa×s | 531.16 | Calculated Property |
| η | 0.0002307 | Pa×s | 566.76 | Calculated Property |
| η | 0.0002063 | Pa×s | 602.36 | Calculated Property |
| η | 0.0001884 | Pa×s | 637.96 | Calculated Property |
| η | 0.0001751 | Pa×s | 673.56 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [51.19; 0.00] | kJ/mol | [353.43; 748.40] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 7.73282e+01 | |||
| Coefficient B | 1.11662e+00 | |||
| Coefficient C | -1.31357e+00 | |||
| Coefficient D | 6.72121e-01 | |||
| Coefficient E | -5.84514e-03 | |||
| Critical temperature, Tc (K) | 7.48400e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 749.42 K. | |||
| Temperature range, min. | 353.43 | |||
| Temperature range, max. | 748.40 | |||
| ΔvapH | 51.19 | kJ/mol | 353.43 | Calculated Property |
| ΔvapH | 48.81 | kJ/mol | 397.32 | Calculated Property |
| ΔvapH | 46.36 | kJ/mol | 441.20 | Calculated Property |
| ΔvapH | 43.72 | kJ/mol | 485.09 | Calculated Property |
| ΔvapH | 40.76 | kJ/mol | 528.97 | Calculated Property |
| ΔvapH | 37.32 | kJ/mol | 572.86 | Calculated Property |
| ΔvapH | 33.16 | kJ/mol | 616.74 | Calculated Property |
| ΔvapH | 27.83 | kJ/mol | 660.63 | Calculated Property |
| ΔvapH | 20.34 | kJ/mol | 704.51 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 748.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.61; 202.64] | kPa | [353.43; 520.99] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39385e+01 | |||
| Coefficient B | -3.59507e+03 | |||
| Coefficient C | -1.04271e+02 | |||
| Temperature range, min. | 353.43 | |||
| Temperature range, max. | 520.99 | |||
| Pvap | 0.61 | kPa | 353.43 | Calculated Property |
| Pvap | 1.67 | kPa | 372.05 | Calculated Property |
| Pvap | 4.00 | kPa | 390.67 | Calculated Property |
| Pvap | 8.60 | kPa | 409.28 | Calculated Property |
| Pvap | 16.94 | kPa | 427.90 | Calculated Property |
| Pvap | 31.01 | kPa | 446.52 | Calculated Property |
| Pvap | 53.31 | kPa | 465.14 | Calculated Property |
| Pvap | 86.92 | kPa | 483.75 | Calculated Property |
| Pvap | 135.37 | kPa | 502.37 | Calculated Property |
| Pvap | 202.64 | kPa | 520.99 | Calculated Property |
| Pvap | [0.97; 4017.07] | kPa | [353.15; 748.40] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.62517e+01 | |||
| Coefficient B | -9.44806e+03 | |||
| Coefficient C | -1.02384e+01 | |||
| Coefficient D | 4.33545e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 353.15 | |||
| Temperature range, max. | 748.40 | |||
| Pvap | 0.97 | kPa | 353.15 | Calculated Property |
| Pvap | 6.51 | kPa | 397.07 | Calculated Property |
| Pvap | 27.88 | kPa | 440.98 | Calculated Property |
| Pvap | 87.59 | kPa | 484.90 | Calculated Property |
| Pvap | 220.54 | kPa | 528.82 | Calculated Property |
| Pvap | 472.96 | kPa | 572.73 | Calculated Property |
| Pvap | 901.34 | kPa | 616.65 | Calculated Property |
| Pvap | 1573.92 | kPa | 660.57 | Calculated Property |
| Pvap | 2575.61 | kPa | 704.48 | Calculated Property |
| Pvap | 4017.07 | kPa | 748.40 | Calculated Property |
| Pvap | [1.01; 3962.19] | kPa | [353.43; 748.35] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 6.88881e+01 | |||
| Coefficient B | -8.56370e+03 | |||
| Coefficient C | -7.67060e+00 | |||
| Coefficient D | 2.86217e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 353.43 | |||
| Temperature range, max. | 748.35 | |||
| Pvap | 1.01 | kPa | 353.43 | Calculated Property |
| Pvap | 6.55 | kPa | 397.31 | Calculated Property |
| Pvap | 27.80 | kPa | 441.19 | Calculated Property |
| Pvap | 87.34 | kPa | 485.07 | Calculated Property |
| Pvap | 220.84 | kPa | 528.95 | Calculated Property |
| Pvap | 475.65 | kPa | 572.83 | Calculated Property |
| Pvap | 908.34 | kPa | 616.71 | Calculated Property |
| Pvap | 1583.18 | kPa | 660.59 | Calculated Property |
| Pvap | 2572.92 | kPa | 704.47 | Calculated Property |
| Pvap | 3962.19 | kPa | 748.35 | Calculated Property |
| Pvap | [1.00; 38.59] | kPa | [353.48; 452.30] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44399e+01 | |||
| Coefficient B | -4.21735e+03 | |||
| Coefficient C | -6.13290e+01 | |||
| Reference | Fowler, Trump, et al., 1968 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 353.48 | |||
| Temperature range, max. | 452.30 | |||
| Pvap | 1.00 | kPa | 353.48 | Calculated Property |
| Pvap | 1.69 | kPa | 364.46 | Calculated Property |
| Pvap | 2.76 | kPa | 375.44 | Calculated Property |
| Pvap | 4.34 | kPa | 386.42 | Calculated Property |
| Pvap | 6.63 | kPa | 397.40 | Calculated Property |
| Pvap | 9.85 | kPa | 408.38 | Calculated Property |
| Pvap | 14.31 | kPa | 419.36 | Calculated Property |
| Pvap | 20.31 | kPa | 430.34 | Calculated Property |
| Pvap | 28.26 | kPa | 441.32 | Calculated Property |
| Pvap | 38.59 | kPa | 452.30 | Calculated Property |
| Pvap | [7.03; 102.90] | kPa | [399.47; 491.79] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37480e+01 | |||
| Coefficient B | -3.69917e+03 | |||
| Coefficient C | -8.59230e+01 | |||
| Reference | Camin and Rossini, 1955 | |||
| Temperature range, min. | 399.47 | |||
| Temperature range, max. | 491.79 | |||
| Pvap | 7.03 | kPa | 399.47 | Calculated Property |
| Pvap | 10.22 | kPa | 409.73 | Calculated Property |
| Pvap | 14.51 | kPa | 419.99 | Calculated Property |
| Pvap | 20.18 | kPa | 430.24 | Calculated Property |
| Pvap | 27.53 | kPa | 440.50 | Calculated Property |
| Pvap | 36.92 | kPa | 450.76 | Calculated Property |
| Pvap | 48.71 | kPa | 461.02 | Calculated Property |
| Pvap | 63.34 | kPa | 471.27 | Calculated Property |
| Pvap | 81.24 | kPa | 481.53 | Calculated Property |
| Pvap | 102.90 | kPa | 491.79 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [991.95; 311.00] | kg/m3 | [333.15; 748.35] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 5.80382e+01 | |||
| Coefficient B | 2.19530e-01 | |||
| Coefficient C | 7.48400e+02 | |||
| Coefficient D | 2.32360e-01 | |||
| Temperature range, min. | 333.15 | |||
| Temperature range, max. | 748.35 | |||
| ρl | 991.95 | kg/m3 | 333.15 | Calculated Property |
| ρl | 957.17 | kg/m3 | 379.28 | Calculated Property |
| ρl | 920.28 | kg/m3 | 425.42 | Calculated Property |
| ρl | 880.77 | kg/m3 | 471.55 | Calculated Property |
| ρl | 837.89 | kg/m3 | 517.68 | Calculated Property |
| ρl | 790.46 | kg/m3 | 563.82 | Calculated Property |
| ρl | 736.44 | kg/m3 | 609.95 | Calculated Property |
| ρl | 671.66 | kg/m3 | 656.08 | Calculated Property |
| ρl | 584.73 | kg/m3 | 702.22 | Calculated Property |
| ρl | 311.00 | kg/m3 | 748.35 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 4.80e-04] | N/m | [353.43; 727.61] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -7.45010e-03 | |||
| Coefficient B | 9.41100e+01 | |||
| Coefficient C | -3.42170e+00 | |||
| Coefficient D | 1.86020e-03 | |||
| Coefficient E | -5.47450e-06 | |||
| Temperature range, min. | 353.43 | |||
| Temperature range, max. | 727.61 | |||
| γ | 0.03 | N/m | 353.43 | Calculated Property |
| γ | 0.03 | N/m | 395.01 | Calculated Property |
| γ | 0.02 | N/m | 436.58 | Calculated Property |
| γ | 0.02 | N/m | 478.16 | Calculated Property |
| γ | 0.02 | N/m | 519.73 | Calculated Property |
| γ | 0.01 | N/m | 561.31 | Calculated Property |
| γ | 0.01 | N/m | 602.88 | Calculated Property |
| γ | 0.01 | N/m | 644.46 | Calculated Property |
| γ | 0.00 | N/m | 686.03 | Calculated Property |
| γ | 4.80e-04 | N/m | 727.61 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.07] | W/m×K | [353.43; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 1.77540e-05 | |||
| Coefficient B | 1.21230e+00 | |||
| Coefficient C | 6.97590e+01 | |||
| Coefficient D | 7.85170e+04 | |||
| Temperature range, min. | 353.43 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 353.43 | Calculated Property |
| λgas | 0.02 | W/m×K | 425.27 | Calculated Property |
| λgas | 0.02 | W/m×K | 497.11 | Calculated Property |
| λgas | 0.03 | W/m×K | 568.95 | Calculated Property |
| λgas | 0.03 | W/m×K | 640.79 | Calculated Property |
| λgas | 0.04 | W/m×K | 712.64 | Calculated Property |
| λgas | 0.05 | W/m×K | 784.48 | Calculated Property |
| λgas | 0.05 | W/m×K | 856.32 | Calculated Property |
| λgas | 0.06 | W/m×K | 928.16 | Calculated Property |
| λgas | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.13; 0.10] | W/m×K | [353.43; 694.96] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 3.32140e-02 | |||
| Coefficient B | -3.61890e+02 | |||
| Coefficient C | -1.28180e-02 | |||
| Coefficient D | -4.02360e-03 | |||
| Coefficient E | 1.27820e-06 | |||
| Temperature range, min. | 353.43 | |||
| Temperature range, max. | 694.96 | |||
| λliquid | 0.13 | W/m×K | 353.43 | Calculated Property |
| λliquid | 0.13 | W/m×K | 391.38 | Calculated Property |
| λliquid | 0.13 | W/m×K | 429.33 | Calculated Property |
| λliquid | 0.12 | W/m×K | 467.27 | Calculated Property |
| λliquid | 0.12 | W/m×K | 505.22 | Calculated Property |
| λliquid | 0.12 | W/m×K | 543.17 | Calculated Property |
| λliquid | 0.11 | W/m×K | 581.12 | Calculated Property |
| λliquid | 0.11 | W/m×K | 619.06 | Calculated Property |
| λliquid | 0.10 | W/m×K | 657.01 | Calculated Property |
| λliquid | 0.10 | W/m×K | 694.96 | Calculated Property |
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