- InChI
- InChI=1S/C8H10O/c9-7-6-8-4-2-1-3-5-8/h1-5,9H,6-7H2
- InChI Key
- WRMNZCZEMHIOCP-UHFFFAOYSA-N
- Formula
- C8H10O
- SMILES
- OCCc1ccccc1
- Molecular Weight1
- 122.16
- CAS
- 60-12-8
- Other Names
-
- .beta.-phenylethyl alcohol
- 1-Phenyl-2-ethanol
- 1-phenyl-2-ethanol («beta»-phenylethanol)
- 2-PEA
- 2-Phenethanol
- 2-Phenethyl alcohol
- 2-PhenyIethanol
- 2-Phenylethyl alcohol
- 2-phenylethanol
- Benzeneethanol
- Benzeneethanol (2-Phenylethanol)
- Beta-phenylethyl alcohol
- Ethanol, 2-phenyl-
- Hydroxyethylbenzene
- Mellol
- Methanol, benzyl-
- PEA
- Phenethanol
- Phenylethanol
- Phenylethyl, beta- alcohol
- benzenethanol
- benzyl carbinol
- phenethyl alcohol
- «beta»-Fenethylalkohol
- «beta»-Fenylethanol
- «beta»-Hydroxyethylbenzene
- «beta»-P.E.A.
- «beta»-PEA
- «beta»-Phenethanol
- «beta»-Phenethyl alcohol
- «beta»-Phenylethanol
- «beta»-Phenylethyl alcohol
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (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).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6124 | Relay (1.0) Calculated Property | |
| ΔfG° | -7.93 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -127.26 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 14.61 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [64.90; 73.40] | kJ/mol |
|
| ΔvapH° | 66.70 | kJ/mol | NIST |
| ΔvapH° | 68.40 | kJ/mol | NIST |
| ΔvapH° | 73.40 ± 1.50 | kJ/mol | NIST |
| ΔvapH° | 69.70 ± 1.60 | kJ/mol | NIST |
| ΔvapH° | 64.90 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 68.00 | kJ/mol | NIST |
| IE | 8.83 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.74 | Aq. Solubility Prediction | |
| logPoct/wat | 1.221 | Crippen Calculated Property | |
| McVol | 105.690 | ml/mol | McGowan Calculated Property |
| Pc | [3850.00; 3990.00] | kPa |
|
| Pc | 3990.00 | kPa | Critical Point and Vapor Pressure Measurements for Seven Compounds by a Low Residence Time Flow Method |
| Pc | 3850.00 | kPa | Vapor-Liquid Critical Properties of Phenol and (C8 to C10) Phenylalkanols |
| Inp | [195.30; 1159.00] |
|
|
| Inp | 1085.50 | NIST | |
| Inp | 1088.47 | NIST | |
| Inp | 1091.65 | NIST | |
| Inp | 1095.04 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1073.43 | NIST | |
| Inp | 1074.60 | NIST | |
| Inp | 1076.16 | NIST | |
| Inp | 1078.09 | NIST | |
| Inp | 1080.29 | NIST | |
| Inp | 1082.78 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1128.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1121.00 | NIST | |
| Inp | 1124.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1139.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1082.40 | NIST | |
| Inp | 1083.70 | NIST | |
| Inp | 1144.00 | NIST | |
| Inp | 1149.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1118.40 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1129.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1139.00 | NIST | |
| Inp | 1135.00 | NIST | |
| Inp | 1116.30 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1115.10 | NIST | |
| Inp | 1116.20 | NIST | |
| Inp | 1116.80 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1076.20 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1121.00 | NIST | |
| Inp | 1069.11 | NIST | |
| Inp | 1069.74 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1079.80 | NIST | |
| Inp | 1080.40 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1119.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1136.00 | NIST | |
| Inp | 1140.00 | NIST | |
| Inp | 1121.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1122.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1132.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1129.00 | NIST | |
| Inp | 1129.00 | NIST | |
| Inp | 1129.00 | NIST | |
| Inp | 1122.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1137.00 | NIST | |
| Inp | 1117.10 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1137.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1129.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1119.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1140.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1084.90 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1085.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1121.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1119.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1101.00 | NIST | |
| Inp | 1101.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1136.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1119.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1122.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1126.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1124.00 | NIST | |
| Inp | 1124.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1132.00 | NIST | |
| Inp | 1126.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1119.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1148.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | Outlier 195.30 | NIST | |
| Inp | Outlier 195.30 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1083.70 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1129.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1119.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1116.00 | NIST | |
| I | [1856.00; 1955.90] |
|
|
| I | 1931.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1892.00 | NIST | |
| I | 1904.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1914.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1912.00 | NIST | |
| I | 1912.00 | NIST | |
| I | 1904.00 | NIST | |
| I | 1922.00 | NIST | |
| I | 1923.00 | NIST | |
| I | 1919.00 | NIST | |
| I | 1923.00 | NIST | |
| I | Outlier 1858.00 | NIST | |
| I | 1876.00 | NIST | |
| I | Outlier 1859.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1901.00 | NIST | |
| I | 1915.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1920.00 | NIST | |
| I | 1925.00 | NIST | |
| I | 1924.00 | NIST | |
| I | Outlier 1858.00 | NIST | |
| I | 1914.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1900.00 | NIST | |
| I | 1935.00 | NIST | |
| I | 1900.00 | NIST | |
| I | 1915.00 | NIST | |
| I | 1920.00 | NIST | |
| I | 1920.00 | NIST | |
| I | 1946.00 | NIST | |
| I | 1921.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1895.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1944.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1946.00 | NIST | |
| I | Outlier 1952.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1883.00 | NIST | |
| I | 1892.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1901.00 | NIST | |
| I | 1911.00 | NIST | |
| I | 1914.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1901.00 | NIST | |
| I | 1915.00 | NIST | |
| I | 1885.00 | NIST | |
| I | 1939.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1919.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1897.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1879.00 | NIST | |
| I | 1873.30 | NIST | |
| I | 1888.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1925.00 | NIST | |
| I | 1917.00 | NIST | |
| I | 1933.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1924.00 | NIST | |
| I | 1917.00 | NIST | |
| I | 1912.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1946.00 | NIST | |
| I | Outlier 1856.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1923.00 | NIST | |
| I | 1924.00 | NIST | |
| I | 1923.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1903.00 | NIST | |
| I | 1932.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1903.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1907.80 | NIST | |
| I | 1910.50 | NIST | |
| I | 1899.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1923.00 | NIST | |
| I | 1925.00 | NIST | |
| I | 1901.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1907.00 | NIST | |
| I | 1909.00 | NIST | |
| I | 1919.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1939.00 | NIST | |
| I | 1909.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1925.00 | NIST | |
| I | 1910.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1944.00 | NIST | |
| I | 1911.00 | NIST | |
| I | 1909.00 | NIST | |
| I | 1936.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1948.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1918.00 | NIST | |
| I | 1918.00 | NIST | |
| I | 1918.00 | NIST | |
| I | 1909.00 | NIST | |
| I | Outlier 1952.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1911.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1889.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1911.00 | NIST | |
| I | 1914.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1883.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1932.00 | NIST | |
| I | 1915.00 | NIST | |
| I | 1920.00 | NIST | |
| I | 1915.00 | NIST | |
| I | Outlier 1955.90 | NIST | |
| I | 1898.00 | NIST | |
| I | Outlier 1953.00 | NIST | |
| I | 1921.00 | NIST | |
| I | 1926.00 | NIST | |
| I | 1903.00 | NIST | |
| I | 1944.00 | NIST | |
| I | 1947.00 | NIST | |
| I | 1947.00 | NIST | |
| I | 1921.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1911.00 | NIST | |
| I | 1911.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1932.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1918.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1910.00 | NIST | |
| I | 1941.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1928.00 | NIST | |
| I | 1925.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1937.00 | NIST | |
| I | 1918.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1936.00 | NIST | |
| I | 1926.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1907.00 | NIST | |
| I | 1938.00 | NIST | |
| I | 1936.00 | NIST | |
| I | 1917.00 | NIST | |
| I | Outlier 1857.00 | NIST | |
| I | 1943.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1950.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1892.00 | NIST | |
| I | 1926.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1927.00 | NIST | |
| I | 1940.00 | NIST | |
| I | 1916.00 | NIST | |
| I | 1932.00 | NIST | |
| I | 1944.00 | NIST | |
| I | 1910.00 | NIST | |
| I | 1909.00 | NIST | |
| I | 1938.00 | NIST | |
| I | 1907.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1916.00 | NIST | |
| I | 1917.00 | NIST | |
| I | 1919.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1947.00 | NIST | |
| I | 1947.00 | NIST | |
| I | 1944.00 | NIST | |
| I | 1942.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1910.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1909.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1928.00 | NIST | |
| I | 1912.00 | NIST | |
| I | 1901.00 | NIST | |
| I | Outlier 1859.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1913.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1929.00 | NIST | |
| I | Outlier 1859.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1909.00 | NIST | |
| I | 1907.00 | NIST | |
| I | 1926.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1892.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1943.00 | NIST | |
| I | 1930.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1883.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1863.00 | NIST | |
| I | Outlier 1859.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1942.00 | NIST | |
| I | 1901.00 | NIST | |
| I | 1889.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1942.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1920.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1915.00 | NIST | |
| I | 1921.00 | NIST | |
| I | 1913.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1928.00 | NIST | |
| I | 1919.00 | NIST | |
| I | 1933.00 | NIST | |
| I | 1898.00 | NIST | |
| I | 1900.00 | NIST | |
| I | 1939.00 | NIST | |
| I | 1939.00 | NIST | |
| I | 1925.00 | NIST | |
| I | 1907.00 | NIST | |
| I | 1935.00 | NIST | |
| I | 1921.00 | NIST | |
| I | 1927.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1916.00 | NIST | |
| I | 1933.00 | NIST | |
| I | 1922.00 | NIST | |
| I | 1919.00 | NIST | |
| I | 1921.00 | NIST | |
| I | 1923.00 | NIST | |
| I | 1939.00 | NIST | |
| I | 1925.00 | NIST | |
| I | 1916.00 | NIST | |
| I | 1892.00 | NIST | |
| I | 1903.00 | NIST | |
| I | 1913.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1884.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1911.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1897.00 | NIST | |
| I | 1909.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1926.00 | NIST | |
| I | 1931.00 | NIST | |
| I | 1939.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1921.00 | NIST | |
| I | 1921.00 | NIST | |
| I | 1889.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1907.00 | NIST | |
| I | Outlier 1860.00 | NIST | |
| I | 1942.00 | NIST | |
| I | 1912.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1937.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1915.00 | NIST | |
| I | 1941.00 | NIST | |
| I | 1922.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1937.00 | NIST | |
| I | 1937.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1905.00 | NIST | |
| I | Outlier 1860.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1951.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1904.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1887.00 | NIST | |
| I | 1937.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1933.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1929.00 | NIST | |
| I | 1895.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1889.00 | NIST | |
| I | 1910.00 | NIST | |
| I | 1915.00 | NIST | |
| I | 1915.00 | NIST | |
| I | 1910.00 | NIST | |
| I | Outlier 1859.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1916.00 | NIST | |
| I | 1925.00 | NIST | |
| I | 1933.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1868.00 | NIST | |
| I | Outlier 1859.00 | NIST | |
| I | 1939.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1918.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1915.00 | NIST | |
| I | 1926.00 | NIST | |
| I | 1901.00 | NIST | |
| I | Outlier 1858.00 | NIST | |
| I | 1900.00 | NIST | |
| I | 1921.00 | NIST | |
| I | Outlier 1952.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1906.00 | NIST | |
| I | 1924.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1923.00 | NIST | |
| I | 1932.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1910.50 | NIST | |
| I | 1925.00 | NIST | |
| I | 1909.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1912.00 | NIST | |
| I | 1919.00 | NIST | |
| Tboil | [491.40; 492.90] | K |
|
| Tboil | 491.40 | K | NIST |
| Tboil | 492.55 ± 0.40 | K | NIST |
| Tboil | 492.90 ± 0.30 | K | NIST |
| Tc | 733.38 | K | Relay (1.0) Calculated Property |
| Tfus | [246.00; 254.00] | K |
|
| Tfus | 246.00 | K | Phase equilibrium in binary systems of ionic liquids, or deep eutectic solvents with 2-phenylethanol (PEA), or water |
| Tfus | 254.00 ± 2.00 | K | NIST |
| Vc | 0.364 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 493.20 | K | 100.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [130.44; 332.20] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -3.29980e+01 | |||
| Coefficient B | 7.18900e-01 | |||
| Coefficient C | -4.73000e-04 | |||
| Coefficient D | 1.19300e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 130.44 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 167.42 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 199.87 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 228.19 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 252.74 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 273.90 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 292.05 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 307.56 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 320.82 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 332.20 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0414739; 0.0001677] | Pa×s | [250.00; 489.34] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.44496e+01 | |||
| Coefficient B | 2.81673e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 250.00 | |||
| Temperature range, max. | 489.34 | |||
| η | 0.0414739 | Pa×s | 250.00 | Calculated Property |
| η | 0.0140383 | Pa×s | 276.59 | Calculated Property |
| η | 0.0057462 | Pa×s | 303.19 | Calculated Property |
| η | 0.0027166 | Pa×s | 329.78 | Calculated Property |
| η | 0.0014362 | Pa×s | 356.37 | Calculated Property |
| η | 0.0008296 | Pa×s | 382.97 | Calculated Property |
| η | 0.0005146 | Pa×s | 409.56 | Calculated Property |
| η | 0.0003383 | Pa×s | 436.15 | Calculated Property |
| η | 0.0002334 | Pa×s | 462.75 | Calculated Property |
| η | 0.0001677 | Pa×s | 489.34 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [373.34; 518.37] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.70642e+01 | |||
| Coefficient B | -5.69212e+03 | |||
| Coefficient C | -3.40500e+01 | |||
| Temperature range, min. | 373.34 | |||
| Temperature range, max. | 518.37 | |||
| Pvap | 1.33 | kPa | 373.34 | Calculated Property |
| Pvap | 2.85 | kPa | 389.45 | Calculated Property |
| Pvap | 5.71 | kPa | 405.57 | Calculated Property |
| Pvap | 10.80 | kPa | 421.68 | Calculated Property |
| Pvap | 19.41 | kPa | 437.80 | Calculated Property |
| Pvap | 33.35 | kPa | 453.91 | Calculated Property |
| Pvap | 55.05 | kPa | 470.03 | Calculated Property |
| Pvap | 87.67 | kPa | 486.14 | Calculated Property |
| Pvap | 135.22 | kPa | 502.26 | Calculated Property |
| Pvap | 202.63 | kPa | 518.37 | Calculated Property |
| Pvap | [6.36e-05; 3766.05] | kPa | [247.00; 684.00] |
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 | 7.90388e+01 | |||
| Coefficient B | -9.76816e+03 | |||
| Coefficient C | -8.96993e+00 | |||
| Coefficient D | 4.34164e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 247.00 | |||
| Temperature range, max. | 684.00 | |||
| Pvap | 6.36e-05 | kPa | 247.00 | Calculated Property |
| Pvap | 9.46e-03 | kPa | 295.56 | Calculated Property |
| Pvap | 0.29 | kPa | 344.11 | Calculated Property |
| Pvap | 3.51 | kPa | 392.67 | Calculated Property |
| Pvap | 22.70 | kPa | 441.22 | Calculated Property |
| Pvap | 97.21 | kPa | 489.78 | Calculated Property |
| Pvap | 312.50 | kPa | 538.33 | Calculated Property |
| Pvap | 819.27 | kPa | 586.89 | Calculated Property |
| Pvap | 1853.59 | kPa | 635.44 | Calculated Property |
| Pvap | 3766.05 | kPa | 684.00 | Calculated Property |
| Pvap | [6.33; 101.60] | kPa | [406.20; 492.10] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.32336e+01 | |||
| Coefficient B | -3.03513e+03 | |||
| Coefficient C | -1.39694e+02 | |||
| Reference | Dreisbach and Shrader, 1949 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 406.20 | |||
| Temperature range, max. | 492.10 | |||
| Pvap | 6.33 | kPa | 406.20 | Calculated Property |
| Pvap | 9.38 | kPa | 415.74 | Calculated Property |
| Pvap | 13.55 | kPa | 425.29 | Calculated Property |
| Pvap | 19.10 | kPa | 434.83 | Calculated Property |
| Pvap | 26.36 | kPa | 444.38 | Calculated Property |
| Pvap | 35.68 | kPa | 453.92 | Calculated Property |
| Pvap | 47.43 | kPa | 463.47 | Calculated Property |
| Pvap | 62.04 | kPa | 473.01 | Calculated Property |
| Pvap | 79.94 | kPa | 482.56 | Calculated Property |
| Pvap | 101.60 | kPa | 492.10 | Calculated Property |
| Pvap | [0.13; 100.47] | kPa | [331.40; 492.70] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.69629e+01 | |||
| Coefficient B | -5.70943e+03 | |||
| Coefficient C | -3.05100e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 331.40 | |||
| Temperature range, max. | 492.70 | |||
| Pvap | 0.13 | kPa | 331.40 | Calculated Property |
| Pvap | 0.39 | kPa | 349.32 | Calculated Property |
| Pvap | 1.01 | kPa | 367.24 | Calculated Property |
| Pvap | 2.37 | kPa | 385.17 | Calculated Property |
| Pvap | 5.15 | kPa | 403.09 | Calculated Property |
| Pvap | 10.40 | kPa | 421.01 | Calculated Property |
| Pvap | 19.76 | kPa | 438.93 | Calculated Property |
| Pvap | 35.56 | kPa | 456.86 | Calculated Property |
| Pvap | 61.04 | kPa | 474.78 | Calculated Property |
| Pvap | 100.47 | kPa | 492.70 | Calculated Property |
Similar Compounds
Find more compounds similar to Phenylethyl Alcohol.
Mixtures
- Phenylethyl Alcohol + Water
- Phenylethyl Alcohol + m-Chloroaniline
- 1-Propanol + Phenylethyl Alcohol
- 2-Propanol + Phenylethyl Alcohol
- Carbonic acid, dimethyl ester + Phenylethyl Alcohol
- Diethyl carbonate + Phenylethyl Alcohol
- 1,3-Dioxolan-2-one, 4-methyl- + Phenylethyl Alcohol
- Octane + Phenylethyl Alcohol
- Decane + Phenylethyl Alcohol
- Dodecane + Phenylethyl Alcohol
- Phenylethyl Alcohol + Tetradecane
- Pentane, 2,2,4-trimethyl- + Phenylethyl Alcohol
- Anisole + Phenylethyl Alcohol
- Benzene, ethoxy- + Phenylethyl Alcohol
- Dimethyl Sulfoxide + Phenylethyl Alcohol
- Benzyl alcohol + Phenylethyl Alcohol
- 2-Pyrrolidinone, 1-methyl- + Phenylethyl Alcohol
- Phenylethyl Alcohol + Water + Tetradonium Bromide
- 1,2-Ethanediol + Phenylethyl Alcohol
- Propylene Glycol + Phenylethyl Alcohol
Find more mixtures with Phenylethyl Alcohol.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
- Phase equilibrium in binary systems of ionic liquids, or deep eutectic solvents with 2-phenylethanol (PEA), or water
- Separation of 2-phenylethanol (PEA) from water using ionic liquids
- Partial molar volumes of organic solutes in water. XI. Phenylmethanol and 2-phenylethanol at T=(298 to 573) K and at pressures up to 30 MPa
- Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
- Solubility of ionic liquids in water and octan-1-ol and octan-1-ol/water, or 2-phenylethanol/water partition coefficients
- Volumetric, acoustic and spectroscopic properties of 3-chloroaniline with substituted ethanols at various temperatures
- Phase equilibrium investigation with ionic liquids and selectivity in separation of 2-phenylethanol from water
- Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
- High Pressure Phase Equilibrium of CO2 + 2-Phenylethanol and CO2 + 3-Methyl-1-butanol
- Excess Properties of Binary Mixtures of Esters of Carbonic Acid + Three Aryl Alcohols at 308.15 K
- Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Glycols or Poly(Ethylene Glycols) and 2-Phenylethyl Alcohol at 308.15 K and Atmospheric Pressure
- Enthalpies of Mixing, Densities, and Refractive Indices for Binary Mixtures of (Anisole or Phenetole) + Three Aryl Alcohols at 308.15 K and at Atmospheric Pressure
- Limiting Separation Factors and Limiting Activity Coefficients for 2-Phenylethanol and 2-Phenylethanal in Water at 100 C
- Excess Enthalpies, Heat Capacities, Densities, Viscosities and Refractive Indices of Dimethyl Sulfoxide + Three Aryl Alcohols at 308.15 K and Atmospheric Pressure
- Critical Point and Vapor Pressure Measurements for Seven Compounds by a Low Residence Time Flow Method
- Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
- Vapor-Liquid Critical Properties of Phenol and (C8 to C10) Phenylalkanols
- Solute Partitioning Between 1-n-Butyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid and Supercritical CO2
- Activity Coefficients and Excess Gibbs Energies for Binary Mixtures of N-Methyl-2-pyrrolidone with Some Substituted Ethanols
- Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
- Solubilities of Hexanal, Benzaldehyde, 2-Furfural, 2-Phenylethanol, Phenylethanal, and c-Nonalactone in Water at Temperatures between (50 and 100) deg C
- Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary Mixtures of 2-Propanol + Benzyl Alcohol, + 2-Phenylethanol and Benzyl Alcohol + 2-Phenylethanol at T ) (298.15, 308.15, and 318.15) K
- Densities, Viscosities, Refractive Indices, and Surface Tensions for the Ternary Mixtures of 2-Propanol + Benzyl Alcohol + 2-Phenylethanol at T = 308.15 K
- Partitioning of Phenylalkanols between Micelles and Water Studied by Limiting Interdiffusion Coefficients in Water and Tetradecyltrimethylammonium Bromide Solutions
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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