- 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).
- ΔcH°solid : Standard solid enthalpy of combustion (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).
- ΔfH°solid : Solid phase 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 standard conditions (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 |
| 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 | 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 |
| 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 | Aq. Solubility Prediction | |
| 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 | 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 | 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 | |
| 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 | [741.35; 784.85] | K |
|
| 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 | 353.30 | 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 | 353.42 | 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 |
| 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
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.61; 202.64] | kPa | [353.43; 520.99] |
The Yaws Handbook of Vapor Pressure
|
| 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 Vapor Pressure Data
|
| 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
![Benzo[tuv]naphtho[2,1-b]picene.](data:image/png;base64,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)
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)
![Dibenzo[a,c]naphthacene.](data:image/png;base64,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)
Find more compounds similar to Naphthalene.
Mixtures
- Acetonitrile + Naphthalene
- Acetone + Naphthalene
- 1,2-Ethanediol + Naphthalene
- Ethanol + Naphthalene
- Benzene + Naphthalene
- Cyclohexane + Naphthalene
- Methyl Alcohol + Naphthalene
- Naphthalene + Water
- Eicosane + Naphthalene
- Pentacosane + Naphthalene
- n-Hexatriacontane + Naphthalene
- Carbon dioxide + Naphthalene
- 2-Pyrrolidinone, 1-methyl- + Naphthalene
- Formamide, N-methyl- + Naphthalene
- Toluene + Carbon dioxide + Naphthalene
- Formamide + Naphthalene
- Heptane + Naphthalene
- Carbon dioxide + Biphenyl + Naphthalene
- Nitrogen + Naphthalene
- helium + Naphthalene
Find more mixtures with Naphthalene.
Sources
- 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
- Enthalpies of solution, partial molar volumes and isentropic compressibilities of polycyclic aromatic hydrocarbons in 1-methyl-2-pyrrolidone at 298.15K
- 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
- Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
- 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
- Thermodynamic properties of solvation of aromatic compounds in cyclohexane, heptane, benzene, 1,4-dioxane, and chloroform at 298.15 K
- High-pressure phase diagram of the drug mitotane in compressed and/or supercritical CO2
- Thermodynamics of solvation and solvophobic effect in formamide
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Crystal structure and thermodynamic properties of myclobutanil
- Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
- Vaporization enthalpy and vapor pressure of (-) Ambroxide and Galaxolide by correlation gas chromatography
- 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
- Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
- Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
- Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
- Enthalpies of solution, enthalpies of fusion and enthalpies of solvation of polyaromatic hydrocarbons: Instruments for determination of sublimation enthalpy at 298.15 K
- Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
- 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
- Thermochemical properties of mono- and di-cyano-aromatic compounds at 298.15 K
- 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
- New Static Apparatus for Vapor Pressure Measurements: Reconciled Thermophysical Data for Benzophenone
- 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
- Ionic Liquids/Water Distribution Ratios of Some Polycyclic Aromatic Hydrocarbons
- 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
- New Static Apparatus and Vapor Pressure of Reference Materials: Naphthalene, Benzoic Acid, Benzophenone, and Ferrocene
- 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
- Limiting Partition Coefficients of Sulfur-Containing Aromatics in a Biphasic [bmim][MeSO4]-Supercritical CO2 System
- Solute Partitioning Between 1-n-Butyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid and Supercritical CO2
- 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
- Measurement and Correlation for Solubilities of Naphthalene in Acetone, Toluene, Xylene, Ethanol, Heptane, and 1-Butanol
- 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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