- InChI
- InChI=1S/C10H8/c1-2-6-10-8-4-3-7-9(10)5-1/h1-8H
- InChI Key
- UFWIBTONFRDIAS-UHFFFAOYSA-N
- Formula
- C10H8
- SMILES
- c1ccc2ccccc2c1
- Molecular Weight1
- 128.17
- CAS
- 91-20-3
- Other Names
-
- Albocarbon
- Camphor tar
- Dezodorator
- Mighty 150
- Mighty RD1
- Moth balls
- Moth flakes
- NCI-C52904
- NSC 37565
- Naftalen
- Naphthalin
- Naphthaline
- Naphthene
- Rcra waste number U165
- Tar camphor
- UN 1334
- UN 2304
- White tar
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Psub : Sublimation pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- ΔsubS : Entropy of sublimation at a given temperature (J/mol×K).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| 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 |
| 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 | 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 | 151.10 | kJ/mol | KDB |
| ΔfH°gas | 150.60 ± 1.50 | kJ/mol | NIST |
| ΔfH°gas | 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 |
| ΔfusH° | [19.07; 19.55] | kJ/mol |
|
| ΔfusH° | 19.07 | kJ/mol | Odd eve... |
| ΔfusH° | 19.55 | kJ/mol | Solid l... |
| ΔfusH° | 19.55 | kJ/mol | Solid-L... |
| 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 | Aq. Sol... | |
| logPoct/wat | 2.840 | Crippen Calculated Property | |
| McVol | 108.540 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [4050.00; 4130.00] | kPa |
|
| Pc | 4050.00 | kPa | KDB |
| Pc | 4130.00 | kPa | Critica... |
| 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 |
| 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 | 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 | |
| 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 | |
| I | [1694.00; 1792.00] |
|
|
| I | 1707.00 | NIST | |
| I | 1762.00 | NIST | |
| I | 1709.00 | NIST | |
| I | Outlier 1791.00 | NIST | |
| I | 1743.00 | NIST | |
| I | 1731.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1719.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1715.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1764.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1740.00 | NIST | |
| I | 1751.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1718.00 | NIST | |
| I | 1762.00 | NIST | |
| I | 1727.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1754.00 | NIST | |
| I | 1707.00 | NIST | |
| I | 1749.00 | NIST | |
| I | Outlier 1792.00 | NIST | |
| I | 1706.00 | NIST | |
| I | 1703.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1750.00 | NIST | |
| I | 1712.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1724.00 | NIST | |
| I | Outlier 1789.00 | NIST | |
| I | 1698.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1769.00 | NIST | |
| I | 1732.00 | NIST | |
| I | 1733.00 | NIST | |
| I | 1706.00 | NIST | |
| I | 1707.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1755.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1731.00 | NIST | |
| I | 1757.00 | NIST | |
| I | 1698.00 | NIST | |
| I | 1698.00 | NIST | |
| I | 1728.00 | NIST | |
| I | 1745.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1699.00 | NIST | |
| I | 1694.00 | NIST | |
| I | 1713.00 | NIST | |
| I | 1729.00 | NIST | |
| I | 1724.00 | NIST | |
| I | 1701.00 | NIST | |
| I | 1714.00 | NIST | |
| I | 1714.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1723.00 | NIST | |
| I | 1734.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1762.00 | NIST | |
| I | 1739.00 | NIST | |
| I | 1722.00 | NIST | |
| I | 1739.00 | NIST | |
| I | 1709.00 | NIST | |
| I | 1720.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 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 | 491.14 | 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 | 748.40 | K | KDB |
| Tfus | [348.15; 356.90] | K |
|
| Tfus | 353.43 | K | Aq. Sol... |
| Tfus | 353.30 | K | KDB |
| Tfus | 353.40 | K | The use... |
| Tfus | Outlier 356.90 | K | Solubil... |
| 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 | [353.42; 355.04] | K |
|
| Ttriple | 353.42 | K | KDB |
| Ttriple | 355.04 | K | Thermod... |
| Vc | [0.407; 0.409] | m3/kmol |
|
| Vc | 0.407 | m3/kmol | KDB |
| Vc | 0.407 | m3/kmol | NIST |
| Vc | 0.409 ± 0.060 | m3/kmol | NIST |
| Zc | 0.2648980 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [201.60; 226.70] | J/mol×K | [451.00; 522.70] |
|
| Cp,gas | 201.60 ± 2.00 | J/mol×K | 451.00 | NIST |
| Cp,gas | 226.70 ± 2.30 | J/mol×K | 522.70 | NIST |
| Cp,liquid | 196.06 | J/mol×K | 298.15 | NIST |
| Cp,solid | [156.10; 213.00] | J/mol×K | [283.15; 342.00] |
|
| Cp,solid | 158.40 | J/mol×K | 283.15 | Crystal... |
| Cp,solid | 161.60 | J/mol×K | 288.15 | Crystal... |
| Cp,solid | 164.80 | J/mol×K | 293.15 | Crystal... |
| Cp,solid | 165.48 | J/mol×K | 294.68 | NIST |
| Cp,solid | 163.60 | J/mol×K | 295.10 | NIST |
| Cp,solid | 168.07 | J/mol×K | 297.60 | NIST |
| Cp,solid | 159.40 | J/mol×K | 298.00 | NIST |
| Cp,solid | 195.80 | J/mol×K | 298.10 | NIST |
| Cp,solid | 161.50 | J/mol×K | 298.10 | NIST |
| Cp,solid | 165.69 | J/mol×K | 298.15 | NIST |
| Cp,solid | 168.00 | J/mol×K | 298.15 | Crystal... |
| Cp,solid | 156.10 | J/mol×K | 298.15 | NIST |
| Cp,solid | 168.11 | J/mol×K | 301.58 | NIST |
| Cp,solid | 169.00 | J/mol×K | 303.00 | NIST |
| Cp,solid | 171.20 | J/mol×K | 303.15 | Crystal... |
| Cp,solid | 174.50 | J/mol×K | 308.15 | Crystal... |
| Cp,solid | 177.80 | J/mol×K | 313.15 | Crystal... |
| Cp,solid | 181.10 | J/mol×K | 318.15 | Crystal... |
| Cp,solid | 184.50 | J/mol×K | 323.15 | Crystal... |
| Cp,solid | 187.90 | J/mol×K | 328.15 | Crystal... |
| Cp,solid | 213.00 | J/mol×K | 330.00 | NIST |
| Cp,solid | 191.30 | J/mol×K | 333.15 | Crystal... |
| Cp,solid | 188.40 | J/mol×K | 342.00 | NIST |
| η | [0.0003173; 0.0017226] | Pa×s | [261.58; 473.86] |
|
| η | 0.0017226 | Pa×s | 261.58 | Joback Calculated Property |
| η | 0.0010984 | Pa×s | 296.96 | Joback Calculated Property |
| η | 0.0007708 | Pa×s | 332.34 | Joback Calculated Property |
| η | 0.0005791 | Pa×s | 367.72 | Joback Calculated Property |
| η | 0.0004574 | Pa×s | 403.10 | Joback Calculated Property |
| η | 0.0003754 | Pa×s | 438.48 | Joback Calculated Property |
| η | 0.0003173 | Pa×s | 473.86 | Joback Calculated Property |
| ΔfusH | [16.44; 19.55] | kJ/mol | [222.50; 354.70] |
|
| ΔfusH | 19.00 | kJ/mol | 222.50 | NIST |
| ΔfusH | 19.25 | kJ/mol | 353.00 | NIST |
| ΔfusH | 19.20 | kJ/mol | 353.00 | NIST |
| ΔfusH | 18.79 | kJ/mol | 353.00 | NIST |
| ΔfusH | 19.00 | kJ/mol | 353.10 | NIST |
| ΔfusH | 19.04 | kJ/mol | 353.40 | NIST |
| ΔfusH | 18.79 | kJ/mol | 353.40 | NIST |
| ΔfusH | 19.10 | kJ/mol | 353.40 | NIST |
| ΔfusH | 19.10 | kJ/mol | 353.40 | NIST |
| ΔfusH | 18.23 | kJ/mol | 353.43 | NIST |
| ΔfusH | 18.81 | kJ/mol | 353.44 | NIST |
| ΔfusH | 19.10 | kJ/mol | 353.50 | NIST |
| ΔfusH | 19.10 | kJ/mol | 353.50 | NIST |
| ΔfusH | 16.44 | kJ/mol | 353.80 | NIST |
| ΔfusH | 19.02 | kJ/mol | 354.10 | NIST |
| ΔfusH | 19.55 | kJ/mol | 354.70 | NIST |
| ΔfusH | 19.55 | kJ/mol | 354.70 | NIST |
| ΔsubH | [64.00; 88.00] | kJ/mol | [245.00; 363.00] |
|
| ΔsubH | 72.70 ± 0.30 | kJ/mol | 245.00 | NIST |
| ΔsubH | 76.60 | kJ/mol | 256.50 | NIST |
| ΔsubH | 73.70 ± 1.00 | kJ/mol | 258.00 | NIST |
| ΔsubH | 73.90 ± 0.20 | kJ/mol | 263.00 | NIST |
| ΔsubH | 74.80 ± 0.40 | kJ/mol | 263.00 | NIST |
| ΔsubH | 72.60 ± 0.60 | kJ/mol | 263.00 | NIST |
| ΔsubH | 69.20 | kJ/mol | 268.00 | NIST |
| ΔsubH | 72.80 ± 0.30 | kJ/mol | 278.00 | NIST |
| ΔsubH | 66.30 | kJ/mol | 279.50 | NIST |
| ΔsubH | 72.38 | kJ/mol | 279.70 | NIST |
| ΔsubH | 67.80 ± 3.50 | kJ/mol | 280.00 | NIST |
| ΔsubH | 66.53 ± 0.84 | kJ/mol | 283.00 | NIST |
| ΔsubH | 72.70 ± 1.70 | kJ/mol | 283.00 | NIST |
| ΔsubH | 88.00 ± 2.50 | kJ/mol | 285.00 | NIST |
| ΔsubH | 64.00 ± 0.50 | kJ/mol | 285.50 | NIST |
| ΔsubH | 72.40 | kJ/mol | 286.50 | NIST |
| ΔsubH | 72.10 | kJ/mol | 292.00 | NIST |
| ΔsubH | 71.30 | kJ/mol | 292.50 | NIST |
| ΔsubH | 65.80 | kJ/mol | 293.00 | NIST |
| ΔsubH | 82.00 | kJ/mol | 293.00 | NIST |
| ΔsubH | 65.70 | kJ/mol | 297.00 | NIST |
| ΔsubH | 72.32 | kJ/mol | 298.15 | NIST |
| ΔsubH | 75.80 ± 1.10 | kJ/mol | 303.00 | NIST |
| ΔsubH | 72.70 | kJ/mol | 303.00 | NIST |
| ΔsubH | 72.50 ± 0.30 | kJ/mol | 303.00 | NIST |
| ΔsubH | 72.30 ± 0.80 | kJ/mol | 312.00 | NIST |
| ΔsubH | 72.50 ± 0.10 | kJ/mol | 313.50 | NIST |
| ΔsubH | 73.40 | kJ/mol | 315.00 | NIST |
| ΔsubH | 74.40 ± 1.70 | kJ/mol | 316.00 | NIST |
| ΔsubH | 71.00 ± 4.00 | kJ/mol | 323.00 | NIST |
| ΔsubH | 72.80 | kJ/mol | 327.00 | NIST |
| ΔsubH | 71.70 | kJ/mol | 333.00 | NIST |
| ΔsubH | 78.00 ± 1.00 | kJ/mol | 344.50 | NIST |
| ΔsubH | 66.30 ± 2.30 | kJ/mol | 354.70 | NIST |
| ΔsubH | 69.90 | kJ/mol | 363.00 | NIST |
| ΔsubH | 76.00 ± 2.00 | kJ/mol | 363.00 | NIST |
| ΔvapH | [41.50; 71.00] | kJ/mol | [298.00; 705.50] |
|
| ΔvapH | 54.64 | kJ/mol | 298.00 | Enthalp... |
| ΔvapH | 70.85 | kJ/mol | 323.00 | NIST |
| ΔvapH | 71.00 | kJ/mol | 339.15 | Comment... |
| ΔvapH | 50.30 ± 0.20 | kJ/mol | 370.50 | NIST |
| ΔvapH | 48.30 | kJ/mol | 379.00 | NIST |
| ΔvapH | 56.10 | kJ/mol | 398.00 | NIST |
| ΔvapH | 48.70 ± 0.30 | kJ/mol | 400.00 | NIST |
| ΔvapH | 50.70 | kJ/mol | 403.50 | NIST |
| ΔvapH | 47.20 | kJ/mol | 423.00 | NIST |
| ΔvapH | 50.60 | kJ/mol | 426.00 | NIST |
| ΔvapH | 47.70 | kJ/mol | 427.00 | NIST |
| ΔvapH | 46.40 | kJ/mol | 440.00 | NIST |
| ΔvapH | 46.40 | kJ/mol | 441.00 | NIST |
| ΔvapH | 49.00 | kJ/mol | 445.00 | NIST |
| ΔvapH | 44.00 | kJ/mol | 480.00 | NIST |
| ΔvapH | 43.26 | kJ/mol | 491.10 | KDB |
| ΔvapH | 47.90 | kJ/mol | 515.50 | NIST |
| ΔvapH | 41.50 | kJ/mol | 520.00 | NIST |
| ΔvapH | 44.80 | kJ/mol | 528.00 | NIST |
| ΔvapH | 45.40 | kJ/mol | 553.50 | NIST |
| ΔvapH | 44.40 | kJ/mol | 563.00 | NIST |
| ΔvapH | 44.70 | kJ/mol | 584.00 | NIST |
| ΔvapH | 43.20 | kJ/mol | 613.00 | NIST |
| ΔvapH | 47.60 ± 1.80 | kJ/mol | 619.00 | NIST |
| ΔvapH | 43.30 | kJ/mol | 705.50 | NIST |
| Psub | [1.10e-04; 8000.00] | kPa | [258.48; 352.19] |
|
| Psub | 1.10e-04 | kPa | 258.48 | Recomme... |
| Psub | 1.10e-04 | kPa | 258.48 | Recomme... |
| Psub | 1.10e-04 | kPa | 258.48 | Recomme... |
| Psub | 1.10e-04 | kPa | 258.48 | Recomme... |
| Psub | 1.10e-04 | kPa | 258.49 | Recomme... |
| Psub | 1.10e-04 | kPa | 258.49 | Recomme... |
| Psub | 1.10e-04 | kPa | 258.49 | Recomme... |
| Psub | 1.10e-04 | kPa | 258.49 | Recomme... |
| Psub | 2.20e-04 | kPa | 263.48 | Recomme... |
| Psub | 2.20e-04 | kPa | 263.48 | Recomme... |
| Psub | 2.20e-04 | kPa | 263.48 | Recomme... |
| Psub | 2.20e-04 | kPa | 263.48 | Recomme... |
| Psub | 2.30e-04 | kPa | 263.49 | Recomme... |
| Psub | 2.30e-04 | kPa | 263.49 | Recomme... |
| Psub | 2.30e-04 | kPa | 263.49 | Recomme... |
| Psub | 2.30e-04 | kPa | 263.49 | Recomme... |
| Psub | 4.30e-04 | kPa | 268.48 | Recomme... |
| Psub | 4.20e-04 | kPa | 268.48 | Recomme... |
| Psub | 4.10e-04 | kPa | 268.48 | Recomme... |
| Psub | 4.20e-04 | kPa | 268.48 | Recomme... |
| Psub | 7.80e-04 | kPa | 273.48 | Recomme... |
| Psub | 7.70e-04 | kPa | 273.48 | Recomme... |
| Psub | 7.80e-04 | kPa | 273.48 | Recomme... |
| Psub | 7.80e-04 | kPa | 273.48 | Recomme... |
| Psub | 7.80e-04 | kPa | 273.49 | Recomme... |
| Psub | 7.80e-04 | kPa | 273.49 | Recomme... |
| Psub | 7.80e-04 | kPa | 273.49 | Recomme... |
| Psub | 7.70e-04 | kPa | 273.49 | Recomme... |
| Psub | 8.10e-04 | kPa | 273.68 | Recomme... |
| Psub | 8.00e-04 | kPa | 273.68 | Recomme... |
| Psub | 8.00e-04 | kPa | 273.68 | Recomme... |
| Psub | 8.10e-04 | kPa | 273.68 | Recomme... |
| Psub | 8.00e-04 | kPa | 273.68 | Recomme... |
| Psub | 8.10e-04 | kPa | 273.68 | Recomme... |
| Psub | 1.37e-03 | kPa | 278.48 | Recomme... |
| Psub | 1.38e-03 | kPa | 278.48 | Recomme... |
| Psub | 1.37e-03 | kPa | 278.48 | Recomme... |
| Psub | 1.37e-03 | kPa | 278.48 | Recomme... |
| Psub | 1.37e-03 | kPa | 278.49 | Recomme... |
| Psub | 1.38e-03 | kPa | 278.49 | Recomme... |
| Psub | 1.38e-03 | kPa | 278.49 | Recomme... |
| Psub | 1.37e-03 | kPa | 278.49 | Recomme... |
| Psub | 1.36e-03 | kPa | 278.49 | Recomme... |
| Psub | 1.38e-03 | kPa | 278.49 | Recomme... |
| Psub | 1.39e-03 | kPa | 278.49 | Recomme... |
| Psub | 1.39e-03 | kPa | 278.49 | Recomme... |
| Psub | 1.38e-03 | kPa | 278.49 | Recomme... |
| Psub | 1.38e-03 | kPa | 278.49 | Recomme... |
| Psub | 2.41e-03 | kPa | 283.49 | Recomme... |
| Psub | 2.41e-03 | kPa | 283.49 | Recomme... |
| Psub | 2.41e-03 | kPa | 283.49 | Recomme... |
| Psub | 4.10e-03 | kPa | 288.49 | Recomme... |
| Psub | 4.11e-03 | kPa | 288.49 | Recomme... |
| Psub | 4.10e-03 | kPa | 288.49 | Recomme... |
| Psub | 6.88e-03 | kPa | 293.49 | Recomme... |
| Psub | 6.88e-03 | kPa | 293.49 | Recomme... |
| Psub | 6.88e-03 | kPa | 293.49 | Recomme... |
| Psub | 0.01 | kPa | 297.72 | Vapor p... |
| Psub | 0.01 | kPa | 298.49 | Recomme... |
| Psub | 0.01 | kPa | 298.49 | Recomme... |
| Psub | 0.01 | kPa | 298.49 | Recomme... |
| Psub | 0.01 | kPa | 298.49 | Recomme... |
| Psub | 0.01 | kPa | 298.49 | Recomme... |
| Psub | 0.01 | kPa | 300.06 | Vapor p... |
| Psub | 0.02 | kPa | 302.47 | Vapor p... |
| Psub | 0.02 | kPa | 303.50 | Recomme... |
| Psub | 0.02 | kPa | 303.50 | Recomme... |
| Psub | 0.02 | kPa | 303.50 | Recomme... |
| Psub | 0.02 | kPa | 303.50 | Recomme... |
| Psub | 0.02 | kPa | 303.50 | Recomme... |
| Psub | 0.02 | kPa | 304.88 | Vapor p... |
| Psub | 0.03 | kPa | 307.27 | Vapor p... |
| Psub | 0.03 | kPa | 308.51 | Recomme... |
| Psub | 0.03 | kPa | 308.51 | Recomme... |
| Psub | 0.03 | kPa | 308.51 | Recomme... |
| Psub | 0.03 | kPa | 308.51 | Recomme... |
| Psub | 0.03 | kPa | 309.69 | Vapor p... |
| Psub | 0.04 | kPa | 312.20 | Apparat... |
| Psub | 0.04 | kPa | 312.20 | Apparat... |
| Psub | 0.04 | kPa | 312.35 | Vapor p... |
| Psub | 0.05 | kPa | 313.52 | Recomme... |
| Psub | 0.05 | kPa | 313.52 | Recomme... |
| Psub | 0.05 | kPa | 313.52 | Recomme... |
| Psub | 0.05 | kPa | 313.52 | Recomme... |
| Psub | 0.05 | kPa | 314.78 | Vapor p... |
| Psub | 0.06 | kPa | 317.21 | Apparat... |
| Psub | 0.06 | kPa | 317.21 | Vapor p... |
| Psub | 0.08 | kPa | 319.66 | Vapor p... |
| Psub | 0.09 | kPa | 322.08 | Vapor p... |
| Psub | 0.10 | kPa | 322.21 | Apparat... |
| Psub | 0.12 | kPa | 324.51 | Vapor p... |
| Psub | 0.14 | kPa | 326.97 | Vapor p... |
| Psub | 0.14 | kPa | 327.21 | Apparat... |
| Psub | 0.22 | kPa | 332.21 | Apparat... |
| Psub | 0.32 | kPa | 337.21 | Apparat... |
| Psub | 0.32 | kPa | 337.21 | Apparat... |
| Psub | 8000.00 | kPa | 337.80 | Solid l... |
| Psub | 6000.00 | kPa | 341.40 | Solid l... |
| Psub | 0.46 | kPa | 342.19 | Apparat... |
| Psub | 3000.00 | kPa | 345.70 | Solid l... |
| Psub | 0.65 | kPa | 347.19 | Apparat... |
| Psub | 0.65 | kPa | 347.19 | Apparat... |
| Psub | 100.00 | kPa | 351.40 | Solid l... |
| Psub | 0.92 | kPa | 352.19 | Apparat... |
| n0 | 1.58980 | 298.15 | KDB | |
| ρl | 971.00 | kg/m3 | 363.00 | KDB |
| ΔfusS | [51.57; 55.00] | J/mol×K | [353.00; 354.10] |
|
| ΔfusS | 54.40 | J/mol×K | 353.00 | NIST |
| ΔfusS | 55.00 | J/mol×K | 353.00 | NIST |
| ΔfusS | 53.20 | J/mol×K | 353.00 | NIST |
| ΔfusS | 53.80 | J/mol×K | 353.10 | NIST |
| ΔfusS | 53.90 | J/mol×K | 353.40 | NIST |
| ΔfusS | 53.20 | J/mol×K | 353.40 | NIST |
| ΔfusS | 51.57 | J/mol×K | 353.43 | NIST |
| ΔfusS | 54.00 | J/mol×K | 353.50 | NIST |
| ΔfusS | 53.70 | J/mol×K | 354.10 | NIST |
| γ | 0.03 | N/m | 413.20 | KDB |
| ΔsubS | 242.60 | J/mol×K | 298.15 | NIST |
| ΔvapS | 219.30 | J/mol×K | 323.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.61; 202.64] | kPa | [353.43; 520.99] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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 | [1.01; 3962.19] | kPa | [353.43; 748.35] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.88881e+01 | |||
| Coefficient B | -8.56370e+03 | |||
| Coefficient C | -7.67060e+00 | |||
| Coefficient D | 2.86217e-06 | |||
| 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 |
Similar Compounds
Find more compounds similar to Naphthalene.
Mixtures
- 2-Pyrrolidinone, 1-methyl- + Naphthalene
- Carbon dioxide + Biphenyl + Naphthalene
- Cyclohexane + Naphthalene
- Heptane + Naphthalene
- Carbon dioxide + Naphthalene
- Eicosane + Naphthalene
- Pentacosane + Naphthalene
- Hexatriacontane + Naphthalene
- Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Naphthalene
- Octane + Naphthalene
- Dodecane + Naphthalene
- Methylene chloride + Naphthalene
- Trichloromethane + Naphthalene
- Carbon Tetrachloride + Naphthalene
- Ethane, 1,2-dichloro- + Naphthalene
- Benzene, 1,2-dichloro- + Naphthalene
- 1-Octanol + Naphthalene
- 2-Octanone + Naphthalene
- Methyl Isobutyl Ketone + Naphthalene
- Benzene + Naphthalene
Find more mixtures with Naphthalene.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Measurements of solid solubilities and volumetric properties of naphthalene + carbon dioxide mixtures with a new assembly taking advantage of a vibrating tube densitometer
- High pressure vapor liquid equilibrium measurements of carbon dioxide with naphthalene and benzoic acid
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- High-pressure phase behavior of the ternary system CO2 + ionic liquid [bmim][PF6] + naphthalene
- Solid liquid gas equilibrium of the naphthalene biphenyl CO2 system: Measurement and modeling
- Solubility determination of organometallic complexes in supercritical carbon dioxide by chromatographic impulse response method
- Vapor pressures and vaporization enthalpies of 5-nonanone, linalool and 6-methyl-5-hepten-2-one. Data evaluation
- Measurement and correlation of solid-liquid equilibria for three binaries, ethanol-antipyrine, chloroform-antipyrine, and dimethyl ether-antipyrine
- Odd even effect in melting properties of 12 alkane-a,x-diamides
- High-pressure phase diagram of the drug mitotane in compressed and/or supercritical CO2
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Crystal structure and thermodynamic properties of myclobutanil
- Solid liquid equilibria and purity determination for binary n-alkane + naphthalene systems
- Combined experiments to measure low sublimation pressures and diffusion coefficients of organometallic compounds
- The use of organic calibration standards in the enthalpy calibration of differential scanning calorimeters
- Experimental measurement and phase equilibria calculation for ternary systems of carbon dioxide+ toluene + naphthalene and carbon dioxide+ ethanol + acridine, applicable for fine particle production in GAS process
- Apparatus to measure the vapor pressure of slowly decomposing compounds from 1 Pa to 105 Pa
- Comment on Studies on Thermodynamic Properties of FOX-7 and Its Five Closed-Loop Derivatives
- Elimination of Tar in Biomass Gasification Process: Liquid Liquid Equilibrium of Ternary Systems {Water + Solvent (p-Xylene and Methyl Hexadecanoate) + Model Molecules of Tar (Thiophene, Pyridine, Naphthalene, Phenathrene, and Anthracene)}
- Solubilities of Palmitic Acid + Capsaicin in Supercritical Carbon Dioxide
- Measurement and Correlation of the Solubilities of Azoxystrobin, Flutriafol, and Tebuconazole in Subcritical 1,1,1,2-Tetrafluoroethane
- Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
- High -Pressure Phase Diagrams of Propane + Decahydronaphthalene and Propane + Naphthalene Mixtures
- Recommended Vapor Pressure of Solid Naphthalene
- Solid-Liquid Equilibria of Naphthalene + Alkanediamine Mixtures
- Solubility of Solid Polycyclic Aromatic Hydrocarbons in Pressurized Hot Water at Temperatures from 313 K to the Melting Point
- Critical Point and Vapor Pressure Measurements for Seven Compounds by a Low Residence Time Flow Method
- Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
- Determination of Henry's Law Constant Using Diffusion in Air and Water Boundary Layers
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Measurement and Correlation of Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Alkane and Cycloalkane Solvents
- Naphthalene Solubility in Binary Solvent Mixtures of 2,2,4-Trimethylpentane + Alcohols at 298.15 K
- Infinite Dilution Binary Diffusion Coefficients of Hydrotreating Compounds in Tetradecane in the Temperature Range from (310 to 475) K
- Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
- Diffusion of Benzonitrile in CO2-Expanded Ethanol
- Solubility of Naphthalene in Isobutyl Acetate, n-Butyric Acid, Ethyl Acetate, N-Methyl Pyrrolidone, N,N-Dimethylformamide, and Tetrahydrofuran
- Solubility of Maleic Acid in Supercritical Carbon Dioxide
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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