- InChI
- InChI=1S/C5H12O/c1-2-3-4-5-6/h6H,2-5H2,1H3
- InChI Key
- AMQJEAYHLZJPGS-UHFFFAOYSA-N
- Formula
- C5H12O
- SMILES
- CCCCCO
- Molecular Weight1
- 88.15
- CAS
- 71-41-0
- Other Names
-
- 1-Pentol
- 1-Pentyl alcohol
- Alcool amylique
- Amyl alcohol
- Amyl alcohol, n-
- Amyl alcohol, normal
- Amylol
- Butyl carbinol
- N-AMYL ALCOHOL
- N-PENTYL ALCOHOL
- NSC 5707
- Pentan-1-ol
- Pentanol
- Pentanol-1
- Pentasol
- Pentyl alcohol
- Primary amyl alcohol
- Primary-N-amyl alcohol
- UN 1105
- n-Amylalkohol
- n-Butylcarbinol
- n-C5H11OH
- n-Pentan-1-ol
- n-Pentanol
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- ν : Kinematic viscosity (m2/s).
- 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).
- 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.
- D*i : Self diffusion coefficient (m2/s).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- 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).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5790 | KDB | |
| PAff | 795.00 | kJ/mol | NIST |
| Tig | 633.15 | K | KDB |
| ΔcH°liquid | [-3330.91; -3324.00] | kJ/mol |
|
| ΔcH°liquid | -3330.91 ± 0.28 | kJ/mol | NIST |
| ΔcH°liquid | -3329.90 ± 0.67 | kJ/mol | NIST |
| ΔcH°liquid | -3329.96 ± 0.64 | kJ/mol | NIST |
| ΔcH°liquid | -3324.60 ± 0.40 | kJ/mol | NIST |
| ΔcH°liquid | -3324.00 | kJ/mol | NIST |
| Cp,liquid | 206.67 | J/mol×K | THERMOD... |
| μ | 1.70 | debye | KDB |
| LFL | 1.10 | % in Air | KDB |
| UFL | 7.50 | % in Air | KDB |
| Tflash,oc | 298.15 | K | KDB |
| ΔfG° | -146.10 | kJ/mol | KDB |
| ΔfH°gas | [-301.00; -294.70] | kJ/mol |
|
| ΔfH°gas | -298.90 | kJ/mol | KDB |
| ΔfH°gas | -294.70 | kJ/mol | NIST |
| ΔfH°gas | -294.70 ± 0.30 | kJ/mol | NIST |
| ΔfH°gas | -295.70 ± 0.70 | kJ/mol | NIST |
| ΔfH°gas | -295.63 ± 0.74 | kJ/mol | NIST |
| ΔfH°gas | -301.00 | kJ/mol | NIST |
| ΔfH°gas | -301.00 ± 0.50 | kJ/mol | NIST |
| ΔfH°gas | -300.60 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | [-358.40; -351.62] | kJ/mol |
|
| ΔfH°liquid | -351.62 ± 0.28 | kJ/mol | NIST |
| ΔfH°liquid | -352.60 ± 0.70 | kJ/mol | NIST |
| ΔfH°liquid | -352.57 ± 0.72 | kJ/mol | NIST |
| ΔfH°liquid | -357.90 ± 0.50 | kJ/mol | NIST |
| ΔfH°liquid | -358.40 ± 1.70 | kJ/mol | NIST |
| ΔfusH° | 10.51 | kJ/mol | Heat Ca... |
| ΔvapH° | [54.23; 57.80] | kJ/mol |
|
| ΔvapH° | 57.04 | kJ/mol | NIST |
| ΔvapH° | Outlier 54.23 | kJ/mol | NIST |
| ΔvapH° | 55.18 | kJ/mol | NIST |
| ΔvapH° | 55.40 | kJ/mol | NIST |
| ΔvapH° | 55.40 | kJ/mol | NIST |
| ΔvapH° | 57.80 | kJ/mol | NIST |
| ΔvapH° | 57.40 | kJ/mol | NIST |
| ΔvapH° | 56.94 ± 0.17 | kJ/mol | NIST |
| ΔvapH° | 56.90 | kJ/mol | NIST |
| ΔvapH° | 56.90 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 56.90 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 57.70 ± 1.10 | kJ/mol | NIST |
| ΔvapH° | 57.70 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 57.80 | kJ/mol | NIST |
| IE | [10.00; 10.42] | eV |
|
| IE | 10.00 | eV | NIST |
| IE | 10.38 | eV | NIST |
| IE | 10.42 ± 0.03 | eV | NIST |
| log10WS | [-0.60; -0.60] |
|
|
| log10WS | -0.60 | Aq. Sol... | |
| log10WS | -0.60 | Estimat... | |
| logPoct/wat | 1.169 | Crippen Calculated Property | |
| McVol | 87.180 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3868.00; 3920.00] | kPa |
|
| Pc | 3897.00 | kPa | KDB |
| Pc | 3900.00 ± 20.00 | kPa | NIST |
| Pc | 3920.00 ± 40.00 | kPa | NIST |
| Pc | 3868.00 ± 20.00 | kPa | NIST |
| Pc | 3868.00 ± 20.00 | kPa | NIST |
| Pc | 3909.00 | kPa | NIST |
| Pc | 3909.00 | kPa | NIST |
| ρc | [269.73; 273.26] | kg/m3 |
|
| ρc | 269.73 ± 1.76 | kg/m3 | NIST |
| ρc | 269.73 | kg/m3 | NIST |
| ρc | 273.26 ± 17.63 | kg/m3 | NIST |
| Inp | [722.00; 801.00] |
|
|
| Inp | Outlier 791.40 | NIST | |
| Inp | Outlier 793.10 | NIST | |
| Inp | 775.50 | NIST | |
| Inp | 771.90 | NIST | |
| Inp | 766.50 | NIST | |
| Inp | 762.30 | NIST | |
| Inp | 757.90 | NIST | |
| Inp | 757.18 | NIST | |
| Inp | 754.60 | NIST | |
| Inp | 753.50 | NIST | |
| Inp | 752.70 | NIST | |
| Inp | 752.20 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 763.40 | NIST | |
| Inp | 761.50 | NIST | |
| Inp | 754.60 | NIST | |
| Inp | 753.50 | NIST | |
| Inp | 752.70 | NIST | |
| Inp | 752.20 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 763.40 | NIST | |
| Inp | 761.50 | NIST | |
| Inp | Outlier 730.20 | NIST | |
| Inp | Outlier 734.70 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | Outlier 789.00 | NIST | |
| Inp | 746.40 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | Outlier 728.00 | NIST | |
| Inp | Outlier 731.00 | NIST | |
| Inp | Outlier 730.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | Outlier 730.00 | NIST | |
| Inp | Outlier 722.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 773.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 779.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 744.10 | NIST | |
| Inp | 760.40 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 769.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 748.30 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 751.90 | NIST | |
| Inp | 751.90 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 778.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 776.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | Outlier 800.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | Outlier 801.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 773.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 776.00 | NIST | |
| Inp | 779.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 776.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 752.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 769.00 | NIST | |
| Inp | 769.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 769.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 751.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | Outlier 787.00 | NIST | |
| Inp | Outlier 730.00 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | Outlier 723.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 744.10 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 773.00 | NIST | |
| Inp | 770.00 | NIST | |
| I | [1200.00; 1294.00] |
|
|
| I | 1256.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1263.00 | NIST | |
| I | Outlier 1288.00 | NIST | |
| I | Outlier 1210.00 | NIST | |
| I | 1241.00 | NIST | |
| I | Outlier 1208.00 | NIST | |
| I | 1226.00 | NIST | |
| I | 1222.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1218.00 | NIST | |
| I | 1237.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1257.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1242.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1217.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1230.00 | NIST | |
| I | 1271.00 | NIST | |
| I | 1261.00 | NIST | |
| I | Outlier 1213.00 | NIST | |
| I | Outlier 1214.00 | NIST | |
| I | 1220.00 | NIST | |
| I | 1236.00 | NIST | |
| I | 1230.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1244.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1254.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1242.00 | NIST | |
| I | 1220.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1232.00 | NIST | |
| I | 1261.00 | NIST | |
| I | 1239.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1233.00 | NIST | |
| I | 1251.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1251.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1239.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1251.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1233.00 | NIST | |
| I | 1264.00 | NIST | |
| I | Outlier 1294.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1248.00 | NIST | |
| I | Outlier 1292.00 | NIST | |
| I | 1235.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1246.00 | NIST | |
| I | 1236.00 | NIST | |
| I | Outlier 1206.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1236.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1251.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1236.00 | NIST | |
| I | Outlier 1216.00 | NIST | |
| I | 1228.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1253.00 | NIST | |
| I | 1261.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1232.00 | NIST | |
| I | 1242.00 | NIST | |
| I | 1240.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1240.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1240.00 | NIST | |
| I | Outlier 1280.00 | NIST | |
| I | 1231.00 | NIST | |
| I | 1230.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1240.00 | NIST | |
| I | 1253.00 | NIST | |
| I | 1237.00 | NIST | |
| I | 1260.00 | NIST | |
| I | Outlier 1206.00 | NIST | |
| I | 1233.00 | NIST | |
| I | 1244.00 | NIST | |
| I | 1254.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1237.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1257.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1268.00 | NIST | |
| I | 1268.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1244.00 | NIST | |
| I | 1241.00 | NIST | |
| I | Outlier 1213.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1248.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1238.00 | NIST | |
| I | 1253.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1248.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1253.00 | NIST | |
| I | 1251.00 | NIST | |
| I | 1244.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1233.00 | NIST | |
| I | Outlier 1285.00 | NIST | |
| I | 1217.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1235.00 | NIST | |
| I | 1246.00 | NIST | |
| I | Outlier 1210.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1246.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1228.00 | NIST | |
| I | 1246.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1230.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1244.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1257.00 | NIST | |
| I | 1244.00 | NIST | |
| I | 1231.00 | NIST | |
| I | 1242.00 | NIST | |
| I | 1243.00 | NIST | |
| I | 1229.00 | NIST | |
| I | 1231.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1232.00 | NIST | |
| I | 1231.00 | NIST | |
| I | 1238.00 | NIST | |
| I | Outlier 1213.00 | NIST | |
| I | 1247.00 | NIST | |
| I | 1247.00 | NIST | |
| I | 1271.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1223.00 | NIST | |
| I | 1224.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1223.00 | NIST | |
| I | 1224.00 | NIST | |
| I | 1236.00 | NIST | |
| I | 1230.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1231.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1244.00 | NIST | |
| I | 1242.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1261.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1224.00 | NIST | |
| I | 1253.00 | NIST | |
| I | 1253.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1253.00 | NIST | |
| I | 1248.00 | NIST | |
| I | 1239.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1253.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1240.00 | NIST | |
| I | 1253.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1248.00 | NIST | |
| I | 1230.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1266.00 | NIST | |
| I | Outlier 1213.00 | NIST | |
| I | 1243.00 | NIST | |
| I | 1233.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1252.00 | NIST | |
| I | Outlier 1200.00 | NIST | |
| I | 1236.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1247.00 | NIST | |
| I | Outlier 1213.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1264.00 | NIST | |
| I | Outlier 1213.00 | NIST | |
| I | 1248.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1244.00 | NIST | |
| I | 1276.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1242.00 | NIST | |
| I | 1232.00 | NIST | |
| I | 1247.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1230.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1257.00 | NIST | |
| I | 1237.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1251.00 | NIST | |
| I | Outlier 1206.00 | NIST | |
| I | 1258.00 | NIST | |
| I | 1236.00 | NIST | |
| S°gas | 401.30 | J/mol×K | NIST |
| S°liquid | [254.80; 258.90] | J/mol×K |
|
| S°liquid | 258.90 | J/mol×K | NIST |
| S°liquid | 254.80 | J/mol×K | NIST |
| Tboil | [273.28; 684.20] | K |
|
| Tboil | 411.13 | K | KDB |
| Tboil | 411.15 | K | Excess ... |
| Tboil | 410.95 | K | Liquid-... |
| Tboil | 411.11 | K | Isobari... |
| Tboil | 410.78 | K | Vapor-L... |
| Tboil | 410.85 | K | Vapor-L... |
| Tboil | 411.10 | K | Isobari... |
| Tboil | Outlier 684.20 ± 0.40 | K | NIST |
| Tboil | 410.90 ± 0.30 | K | NIST |
| Tboil | 410.20 | K | NIST |
| Tboil | 410.15 ± 0.40 | K | NIST |
| Tboil | 411.20 | K | NIST |
| Tboil | 392.40 | K | NIST |
| Tboil | 411.00 ± 0.30 | K | NIST |
| Tboil | 411.10 ± 0.08 | K | NIST |
| Tboil | 411.00 ± 0.50 | K | NIST |
| Tboil | Outlier 273.28 ± 0.10 | K | NIST |
| Tboil | 410.80 ± 0.40 | K | NIST |
| Tboil | 411.20 ± 0.50 | K | NIST |
| Tboil | 411.20 ± 0.40 | K | NIST |
| Tboil | 411.15 | K | NIST |
| Tboil | 409.15 ± 3.00 | K | NIST |
| Tboil | 411.65 ± 0.50 | K | NIST |
| Tboil | 410.65 ± 3.00 | K | NIST |
| Tboil | 410.65 ± 0.50 | K | NIST |
| Tboil | 411.15 ± 0.50 | K | NIST |
| Tboil | 411.00 ± 0.50 | K | NIST |
| Tboil | 410.15 ± 0.70 | K | NIST |
| Tboil | 408.65 ± 2.00 | K | NIST |
| Tboil | 411.07 ± 0.20 | K | NIST |
| Tboil | 409.65 ± 1.00 | K | NIST |
| Tboil | 406.65 ± 3.00 | K | NIST |
| Tboil | 410.65 ± 0.50 | K | NIST |
| Tboil | 411.15 ± 0.50 | K | NIST |
| Tboil | 411.35 ± 0.50 | K | NIST |
| Tboil | 411.05 ± 1.00 | K | NIST |
| Tboil | 411.15 ± 0.50 | K | NIST |
| Tboil | 410.15 ± 1.00 | K | NIST |
| Tboil | 410.15 ± 1.00 | K | NIST |
| Tboil | 411.40 ± 0.50 | K | NIST |
| Tboil | 411.35 ± 0.50 | K | NIST |
| Tboil | 411.15 ± 0.50 | K | NIST |
| Tboil | 409.15 ± 3.00 | K | NIST |
| Tboil | 410.90 ± 0.50 | K | NIST |
| Tboil | 411.15 ± 1.00 | K | NIST |
| Tboil | 410.95 ± 0.50 | K | NIST |
| Tboil | 411.10 ± 0.50 | K | NIST |
| Tboil | 407.15 ± 3.00 | K | NIST |
| Tboil | 411.21 ± 0.05 | K | NIST |
| Tboil | 410.80 ± 0.20 | K | NIST |
| Tboil | 411.10 ± 0.10 | K | NIST |
| Tboil | 409.85 ± 0.50 | K | NIST |
| Tboil | 410.95 ± 0.30 | K | NIST |
| Tboil | 411.40 ± 0.10 | K | NIST |
| Tboil | 408.90 ± 1.50 | K | NIST |
| Tboil | 410.95 ± 0.30 | K | NIST |
| Tboil | 410.95 ± 0.50 | K | NIST |
| Tboil | 411.15 ± 0.07 | K | NIST |
| Tboil | 410.40 ± 0.30 | K | NIST |
| Tboil | 409.15 ± 2.00 | K | NIST |
| Tboil | 411.20 ± 0.20 | K | NIST |
| Tboil | 411.00 ± 0.50 | K | NIST |
| Tboil | 410.65 ± 1.00 | K | NIST |
| Tboil | 411.15 ± 1.00 | K | NIST |
| Tboil | 411.10 ± 0.20 | K | NIST |
| Tboil | 411.10 ± 0.10 | K | NIST |
| Tboil | 402.20 ± 0.50 | K | NIST |
| Tboil | 404.15 ± 4.00 | K | NIST |
| Tboil | 410.00 ± 3.00 | K | NIST |
| Tboil | 404.75 ± 3.00 | K | NIST |
| Tboil | 411.00 ± 1.00 | K | NIST |
| Tboil | 402.90 ± 1.00 | K | NIST |
| Tboil | 404.15 ± 3.00 | K | NIST |
| Tboil | 404.25 ± 3.00 | K | NIST |
| Tc | [551.60; 588.50] | K |
|
| Tc | 588.10 | K | KDB |
| Tc | 588.10 ± 0.50 | K | NIST |
| Tc | 588.00 ± 0.40 | K | NIST |
| Tc | 588.20 ± 0.50 | K | NIST |
| Tc | 588.50 ± 0.60 | K | NIST |
| Tc | 588.50 ± 0.60 | K | NIST |
| Tc | 588.00 | K | NIST |
| Tc | 587.70 ± 0.20 | K | NIST |
| Tc | 588.20 | K | NIST |
| Tc | Outlier 551.60 | K | NIST |
| Tc | 588.11 | K | NIST |
| Tfus | [194.20; 194.95] | K |
|
| Tfus | 194.20 | K | KDB |
| Tfus | 194.68 | K | Aq. Sol... |
| Tfus | 194.95 | K | NIST |
| Tfus | 194.35 ± 0.30 | K | NIST |
| Tfus | 194.65 ± 0.50 | K | NIST |
| Tfus | 194.65 ± 0.50 | K | NIST |
| Ttriple | [194.20; 195.56] | K |
|
| Ttriple | 195.56 | K | KDB |
| Ttriple | 195.56 ± 0.02 | K | NIST |
| Ttriple | 194.20 ± 0.20 | K | NIST |
| Vc | [0.326; 0.326] | m3/kmol |
|
| Vc | 0.326 | m3/kmol | KDB |
| Vc | 0.326 | m3/kmol | NIST |
| Zc | 0.2598130 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [167.91; 221.40] | J/mol×K | [403.49; 573.95] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 170 180 190 200 210 220 400 450 500 550 | ||||
| Cp,gas | 167.91 | J/mol×K | 403.49 | NIST |
| Cp,gas | 177.70 ± 1.40 | J/mol×K | 418.95 | NIST |
| Cp,gas | 178.20 ± 1.40 | J/mol×K | 420.75 | NIST |
| Cp,gas | 174.58 | J/mol×K | 423.32 | NIST |
| Cp,gas | 179.70 ± 1.40 | J/mol×K | 426.15 | NIST |
| Cp,gas | 181.70 ± 1.40 | J/mol×K | 433.45 | NIST |
| Cp,gas | 179.33 | J/mol×K | 438.26 | NIST |
| Cp,gas | 184.40 ± 1.40 | J/mol×K | 442.85 | NIST |
| Cp,gas | 184.80 ± 1.40 | J/mol×K | 444.35 | NIST |
| Cp,gas | 184.35 | J/mol×K | 453.45 | NIST |
| Cp,gas | 192.90 ± 1.40 | J/mol×K | 472.85 | NIST |
| Cp,gas | 190.44 | J/mol×K | 473.19 | NIST |
| Cp,gas | 195.50 ± 1.40 | J/mol×K | 482.25 | NIST |
| Cp,gas | 209.30 ± 1.40 | J/mol×K | 531.25 | NIST |
| Cp,gas | 215.80 ± 1.40 | J/mol×K | 554.15 | NIST |
| Cp,gas | 221.40 ± 1.40 | J/mol×K | 573.95 | NIST |
| Cp,liquid | [183.30; 240.60] | J/mol×K | [293.15; 313.20] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 180 190 200 210 220 230 240 295 300 305 310 | ||||
| Cp,liquid | 205.60 | J/mol×K | 293.15 | NIST |
| Cp,liquid | 209.12 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 183.30 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 207.45 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 207.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 208.98 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 208.19 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 208.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 207.45 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 208.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 212.30 | J/mol×K | 301.26 | NIST |
| Cp,liquid | 201.70 | J/mol×K | 302.40 | NIST |
| Cp,liquid | 240.60 | J/mol×K | 313.20 | NIST |
| η | [0.0006470; 0.0054170] | Pa×s | [283.15; 373.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 300 320 340 360 | ||||
| η | 0.0054170 | Pa×s | 283.15 | Density... |
| η | 0.0046820 | Pa×s | 288.15 | Densiti... |
| η | 0.0040601 | Pa×s | 293.15 | Densiti... |
| η | 0.0040290 | Pa×s | 293.15 | Densiti... |
| η | 0.0039740 | Pa×s | 293.15 | Density... |
| η | 0.0040300 | Pa×s | 293.15 | Density... |
| η | 0.0040250 | Pa×s | 293.15 | Densiti... |
| η | 0.0041170 | Pa×s | 293.15 | Density... |
| η | 0.0034580 | Pa×s | 298.15 | Densiti... |
| η | 0.0034940 | Pa×s | 298.15 | Densiti... |
| η | 0.0035344 | Pa×s | 298.15 | Densiti... |
| η | 0.0035560 | Pa×s | 298.15 | Density... |
| η | 0.0034970 | Pa×s | 298.15 | Densiti... |
| η | 0.0034800 | Pa×s | 298.15 | Density... |
| η | 0.0034410 | Pa×s | 298.15 | Density... |
| η | 0.0030600 | Pa×s | 303.15 | Density... |
| η | 0.0030582 | Pa×s | 303.15 | Densiti... |
| η | 0.0030200 | Pa×s | 303.15 | Density... |
| η | 0.0030220 | Pa×s | 303.15 | Densiti... |
| η | 0.0030070 | Pa×s | 303.15 | Densiti... |
| η | 0.0029900 | Pa×s | 303.15 | Density... |
| η | 0.0026250 | Pa×s | 308.15 | Densiti... |
| η | 0.0022995 | Pa×s | 313.15 | Densiti... |
| η | 0.0023120 | Pa×s | 313.15 | Densiti... |
| η | 0.0023320 | Pa×s | 313.15 | Density... |
| η | 0.0022630 | Pa×s | 313.15 | Density... |
| η | 0.0023170 | Pa×s | 313.15 | Densiti... |
| η | 0.0023150 | Pa×s | 313.15 | Density... |
| η | 0.0020290 | Pa×s | 318.15 | Densiti... |
| η | 0.0018010 | Pa×s | 323.15 | Density... |
| η | 0.0018220 | Pa×s | 323.15 | Density... |
| η | 0.0017950 | Pa×s | 323.15 | Densiti... |
| η | 0.0014250 | Pa×s | 333.15 | Density... |
| η | 0.0014400 | Pa×s | 333.15 | Density... |
| η | 0.0011460 | Pa×s | 343.15 | Density... |
| η | 0.0011460 | Pa×s | 343.15 | Density... |
| η | 0.0009310 | Pa×s | 353.15 | Density... |
| η | 0.0009350 | Pa×s | 353.15 | Density... |
| η | 0.0007670 | Pa×s | 363.15 | Density... |
| η | 0.0007720 | Pa×s | 363.15 | Density... |
| η | 0.0006470 | Pa×s | 373.15 | Density... |
| ΔfusH | [9.83; 10.51] | kJ/mol | [194.20; 195.60] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 9.8 9.9 10 10.1 10.2 10.3 10.4 10.5 194.5 195 195.5 | ||||
| ΔfusH | 9.83 | kJ/mol | 194.20 | NIST |
| ΔfusH | 10.50 | kJ/mol | 195.56 | NIST |
| ΔfusH | 10.51 | kJ/mol | 195.60 | NIST |
| ΔfusH | 10.50 | kJ/mol | 195.60 | NIST |
| ΔfusH | 10.50 | kJ/mol | 195.60 | NIST |
| ΔvapH | [7.10; 56.20] | kJ/mol | [313.00; 586.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 10 20 30 40 50 60 400 500 | ||||
| ΔvapH | 55.70 ± 0.20 | kJ/mol | 313.00 | NIST |
| ΔvapH | 54.40 ± 0.20 | kJ/mol | 328.00 | NIST |
| ΔvapH | 53.00 ± 0.20 | kJ/mol | 343.00 | NIST |
| ΔvapH | 51.20 ± 0.20 | kJ/mol | 358.00 | NIST |
| ΔvapH | 56.20 | kJ/mol | 359.00 | NIST |
| ΔvapH | 55.00 | kJ/mol | 360.50 | NIST |
| ΔvapH | 50.50 ± 0.10 | kJ/mol | 362.00 | NIST |
| ΔvapH | 54.30 | kJ/mol | 368.50 | NIST |
| ΔvapH | 51.50 | kJ/mol | 372.50 | NIST |
| ΔvapH | 49.20 ± 0.10 | kJ/mol | 374.00 | NIST |
| ΔvapH | 51.60 | kJ/mol | 388.00 | NIST |
| ΔvapH | 47.00 ± 0.10 | kJ/mol | 392.00 | NIST |
| ΔvapH | 41.40 | kJ/mol | 392.40 | NIST |
| ΔvapH | 47.20 | kJ/mol | 404.00 | NIST |
| ΔvapH | 44.35 | kJ/mol | 410.90 | KDB |
| ΔvapH | 44.40 ± 0.10 | kJ/mol | 411.00 | NIST |
| ΔvapH | 44.40 | kJ/mol | 411.00 | NIST |
| ΔvapH | 44.36 | kJ/mol | 411.20 | NIST |
| ΔvapH | 45.40 | kJ/mol | 424.50 | NIST |
| ΔvapH | 40.10 | kJ/mol | 448.00 | NIST |
| ΔvapH | 36.10 | kJ/mol | 473.00 | NIST |
| ΔvapH | 31.70 | kJ/mol | 498.00 | NIST |
| ΔvapH | 26.40 | kJ/mol | 523.00 | NIST |
| ΔvapH | 22.00 | kJ/mol | 548.00 | NIST |
| ΔvapH | 14.10 | kJ/mol | 573.00 | NIST |
| ΔvapH | 7.10 | kJ/mol | 586.00 | NIST |
| ν | [0.0000029; 0.0000050] | m2/s | [293.15; 313.15] |
|
|
T(K) Kinematic viscosity (m2/s) 3.00e-6 3.50e-6 4.00e-6 4.50e-6 5.00e-6 295 300 305 310 | ||||
| ν | 0.0000050 | m2/s | 293.15 | Densiti... |
| ν | 0.0000044 | m2/s | 295.15 | Densiti... |
| ν | 0.0000042 | m2/s | 298.15 | Densiti... |
| ν | 0.0000039 | m2/s | 300.15 | Densiti... |
| ν | 0.0000036 | m2/s | 303.15 | Densiti... |
| ν | 0.0000037 | m2/s | 303.15 | Densiti... |
| ν | 0.0000035 | m2/s | 305.15 | Densiti... |
| ν | 0.0000031 | m2/s | 308.15 | Densiti... |
| ν | 0.0000029 | m2/s | 313.15 | Densiti... |
| Pvap | [0.34; 113.30] | kPa | [298.15; 414.65] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 120 300 350 400 | ||||
| Pvap | 0.34 | kPa | 298.15 | Vapor P... |
| Pvap | 0.49 | kPa | 303.15 | Vapor P... |
| Pvap | 0.69 | kPa | 308.15 | Vapor P... |
| Pvap | 0.91 | kPa | 313.15 | Charact... |
| Pvap | 0.97 | kPa | 313.15 | Vapor P... |
| Pvap | 0.90 | kPa | 313.15 | Vapour-... |
| Pvap | 1.36 | kPa | 318.15 | Vapor P... |
| Pvap | 1.87 | kPa | 323.15 | Vapor P... |
| Pvap | 2.53 | kPa | 328.15 | Vapor P... |
| Pvap | 3.38 | kPa | 333.15 | Vapor P... |
| Pvap | 4.47 | kPa | 338.15 | Vapor P... |
| Pvap | 5.87 | kPa | 343.15 | Vapor P... |
| Pvap | 7.63 | kPa | 348.15 | Vapor P... |
| Pvap | 9.83 | kPa | 353.15 | Vapor P... |
| Pvap | 12.52 | kPa | 358.15 | Vapor P... |
| Pvap | 15.81 | kPa | 363.15 | Vapor P... |
| Pvap | 19.86 | kPa | 368.15 | Vapor P... |
| Pvap | 24.68 | kPa | 373.15 | Vapor P... |
| Pvap | 30.47 | kPa | 378.15 | Vapor P... |
| Pvap | 31.30 | kPa | 379.35 | Isobari... |
| Pvap | 35.30 | kPa | 382.40 | Isobari... |
| Pvap | 37.36 | kPa | 383.15 | Vapor P... |
| Pvap | 40.00 | kPa | 384.45 | Low-Pre... |
| Pvap | 40.01 | kPa | 384.85 | Low-Pre... |
| Pvap | 40.00 | kPa | 385.65 | Isobari... |
| Pvap | 45.45 | kPa | 388.15 | Vapor P... |
| Pvap | 49.20 | kPa | 390.75 | Isobari... |
| Pvap | 54.41 | kPa | 392.76 | Low-Pre... |
| Pvap | 54.88 | kPa | 393.15 | Vapor P... |
| Pvap | 56.90 | kPa | 394.70 | Isobari... |
| Pvap | 66.15 | kPa | 398.11 | Low-Pre... |
| Pvap | 65.84 | kPa | 398.15 | Vapor P... |
| Pvap | 69.30 | kPa | 400.05 | Isobari... |
| Pvap | 72.93 | kPa | 400.95 | Low-Pre... |
| Pvap | 78.45 | kPa | 403.15 | Vapor P... |
| Pvap | 82.75 | kPa | 404.59 | Low-Pre... |
| Pvap | 81.30 | kPa | 404.60 | Isobari... |
| Pvap | 90.21 | kPa | 407.17 | Low-Pre... |
| Pvap | 94.50 | kPa | 409.00 | Isobari... |
| Pvap | 101.20 | kPa | 410.73 | Low-Pre... |
| Pvap | 101.90 | kPa | 411.35 | Isobari... |
| Pvap | 113.30 | kPa | 414.65 | Isobari... |
| n0 | [1.39776; 1.41192] | [288.15; 323.15] |
|
|
|
T(K) Refractive Index 1.4 1.4 1.4 1.4 1.41 1.41 1.41 1.41 290 300 310 320 | ||||
| n0 | 1.41192 | 288.15 | Experim... | |
| n0 | 1.41040 | 293.00 | Quatern... | |
| n0 | 1.40900 | 293.10 | Viscosi... | |
| n0 | 1.40980 | 293.13 | Isobari... | |
| n0 | 1.40980 | 293.13 | Isobari... | |
| n0 | 1.40980 | 293.15 | Isobari... | |
| n0 | 1.40995 | 293.15 | Excess ... | |
| n0 | 1.40980 | 293.15 | Experim... | |
| n0 | 1.40976 | 293.15 | Densiti... | |
| n0 | 1.40920 | 293.15 | Measure... | |
| n0 | 1.40980 | 293.15 | Isobari... | |
| n0 | 1.40980 | 293.15 | Isobari... | |
| n0 | 1.40994 | 293.15 | Experim... | |
| n0 | 1.40995 | 293.15 | Densiti... | |
| n0 | 1.41000 | 293.15 | Isother... | |
| n0 | 1.40980 | 293.15 | ERAS mo... | |
| n0 | 1.40970 | 293.20 | Vapor L... | |
| n0 | 1.41000 | 293.20 | Liquid-... | |
| n0 | 1.40970 | 293.20 | Vapor L... | |
| n0 | 1.40730 | 298.15 | Thermod... | |
| n0 | 1.40784 | 298.15 | Thermop... | |
| n0 | 1.40680 | 298.15 | Densiti... | |
| n0 | 1.40850 | 298.15 | Compara... | |
| n0 | 1.40770 | 298.15 | Isobari... | |
| n0 | 1.40780 | 298.15 | Mixing ... | |
| n0 | 1.40780 | 298.15 | Excess ... | |
| n0 | 1.40970 | 298.15 | Investi... | |
| n0 | 1.40941 | 298.15 | Atmosph... | |
| n0 | 1.40774 | 298.15 | Effect ... | |
| n0 | 1.40797 | 298.15 | Experim... | |
| n0 | 1.40710 | 298.15 | Liquid-... | |
| n0 | 1.40730 | 298.15 | Thermod... | |
| n0 | 1.40850 | 298.15 | Bubble ... | |
| n0 | 1.40780 | 298.15 | Excess ... | |
| n0 | 1.40796 | 298.15 | Experim... | |
| n0 | 1.40703 | 298.15 | Liquid ... | |
| n0 | 1.40770 | 298.15 | Isobari... | |
| n0 | 1.40770 | 298.15 | Density... | |
| n0 | 1.40860 | 298.15 | Excess ... | |
| n0 | 1.40880 | 298.15 | Excess ... | |
| n0 | 1.40780 | 298.15 | Effect ... | |
| n0 | 1.40770 | 298.15 | Liquid-... | |
| n0 | 1.40890 | 298.15 | Excess ... | |
| n0 | 1.40800 | 298.15 | Density... | |
| n0 | 1.40800 | 298.15 | Vapor l... | |
| n0 | 1.40764 | 298.20 | Vapor-L... | |
| n0 | 1.40730 | 298.20 | Tie lin... | |
| n0 | 1.40592 | 303.15 | Densiti... | |
| n0 | 1.40690 | 303.15 | Compara... | |
| n0 | 1.40592 | 303.15 | Densiti... | |
| n0 | 1.40500 | 303.15 | Thermod... | |
| n0 | 1.40595 | 303.15 | Experim... | |
| n0 | 1.40500 | 303.15 | Thermod... | |
| n0 | 1.40388 | 308.15 | Experim... | |
| n0 | 1.40590 | 308.15 | Compara... | |
| n0 | 1.40310 | 308.15 | Densiti... | |
| n0 | 1.40320 | 308.15 | Thermod... | |
| n0 | 1.40320 | 308.15 | Thermod... | |
| n0 | 1.40390 | 313.15 | Compara... | |
| n0 | 1.40189 | 313.15 | Experim... | |
| n0 | 1.40178 | 313.15 | Thermop... | |
| n0 | 1.39987 | 318.15 | Experim... | |
| n0 | 1.40030 | 318.15 | Mixing ... | |
| n0 | 1.39960 | 318.15 | Densiti... | |
| n0 | 1.39776 | 323.15 | Experim... | |
| ρl | [759.77; 822.42] | kg/m3 | [283.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 760 770 780 790 800 810 820 300 320 340 360 | ||||
| ρl | 821.79 | kg/m3 | 283.15 | Excess ... |
| ρl | 822.42 | kg/m3 | 283.15 | Volumet... |
| ρl | 821.95 | kg/m3 | 283.15 | Densiti... |
| ρl | 821.81 | kg/m3 | 283.15 | Excess ... |
| ρl | 821.90 | kg/m3 | 283.15 | Densiti... |
| ρl | 818.56 | kg/m3 | 288.15 | Densiti... |
| ρl | 819.15 | kg/m3 | 288.15 | Excess ... |
| ρl | 818.30 | kg/m3 | 288.15 | Tempera... |
| ρl | 818.34 | kg/m3 | 288.15 | Thermod... |
| ρl | 818.59 | kg/m3 | 288.15 | Densiti... |
| ρl | 818.30 | kg/m3 | 288.15 | Densiti... |
| ρl | 818.79 | kg/m3 | 288.15 | Volumet... |
| ρl | 818.28 | kg/m3 | 288.15 | Influen... |
| ρl | 818.80 | kg/m3 | 288.15 | Excess ... |
| ρl | 815.00 | kg/m3 | 293.00 | KDB |
| ρl | 814.60 | kg/m3 | 293.00 | Fluid-P... |
| ρl | 814.68 | kg/m3 | 293.15 | Densiti... |
| ρl | 814.89 | kg/m3 | 293.15 | Densiti... |
| ρl | 814.59 | kg/m3 | 293.15 | Volumet... |
| ρl | 814.81 | kg/m3 | 293.15 | Thermod... |
| ρl | 814.60 | kg/m3 | 293.15 | Densiti... |
| ρl | 814.50 | kg/m3 | 293.15 | Correla... |
| ρl | 814.63 | kg/m3 | 293.15 | Influen... |
| ρl | 815.13 | kg/m3 | 293.15 | Volumet... |
| ρl | 814.53 | kg/m3 | 293.15 | Osmotic... |
| ρl | 814.80 | kg/m3 | 293.15 | Excess ... |
| ρl | 814.92 | kg/m3 | 293.15 | Densiti... |
| ρl | 810.90 | kg/m3 | 298.00 | Fluid-P... |
| ρl | 811.00 | kg/m3 | 298.00 | Compara... |
| ρl | 810.93 | kg/m3 | 298.15 | Volumet... |
| ρl | 811.10 | kg/m3 | 298.15 | Tempera... |
| ρl | 811.47 | kg/m3 | 298.15 | Excess ... |
| ρl | 810.88 | kg/m3 | 298.15 | Physica... |
| ρl | 810.88 | kg/m3 | 298.15 | Excess ... |
| ρl | 810.84 | kg/m3 | 298.15 | Study o... |
| ρl | 811.00 | kg/m3 | 298.15 | Volumet... |
| ρl | 811.80 | kg/m3 | 298.15 | Excess ... |
| ρl | 810.90 | kg/m3 | 298.15 | Dynamic... |
| ρl | 810.93 | kg/m3 | 298.15 | Densiti... |
| ρl | 810.82 | kg/m3 | 298.15 | FT-IR s... |
| ρl | 811.00 | kg/m3 | 298.15 | Thermod... |
| ρl | 811.03 | kg/m3 | 298.15 | Densiti... |
| ρl | 810.97 | kg/m3 | 298.15 | Influen... |
| ρl | 810.12 | kg/m3 | 298.15 | Isobari... |
| ρl | 810.89 | kg/m3 | 298.15 | Excess ... |
| ρl | 810.83 | kg/m3 | 298.15 | Densiti... |
| ρl | 811.10 | kg/m3 | 298.15 | The stu... |
| ρl | 811.10 | kg/m3 | 298.15 | Surface... |
| ρl | 811.04 | kg/m3 | 298.15 | Densiti... |
| ρl | 811.40 | kg/m3 | 298.15 | Thermod... |
| ρl | 811.26 | kg/m3 | 298.15 | Densiti... |
| ρl | 811.14 | kg/m3 | 298.15 | Thermod... |
| ρl | 810.82 | kg/m3 | 298.15 | Excess ... |
| ρl | 810.80 | kg/m3 | 298.15 | Correla... |
| ρl | 811.45 | kg/m3 | 298.15 | Volumet... |
| ρl | 811.04 | kg/m3 | 298.15 | Vapor-l... |
| ρl | 810.88 | kg/m3 | 298.15 | Excess ... |
| ρl | 810.90 | kg/m3 | 298.15 | Excess ... |
| ρl | 810.90 | kg/m3 | 298.15 | Excess ... |
| ρl | 811.23 | kg/m3 | 298.15 | Densiti... |
| ρl | 811.29 | kg/m3 | 298.20 | Liquid-... |
| ρl | 807.00 | kg/m3 | 303.00 | Compara... |
| ρl | 807.30 | kg/m3 | 303.00 | Fluid-P... |
| ρl | 807.24 | kg/m3 | 303.15 | Volumet... |
| ρl | 807.37 | kg/m3 | 303.15 | Densiti... |
| ρl | 807.11 | kg/m3 | 303.15 | Volumet... |
| ρl | 807.25 | kg/m3 | 303.15 | Densiti... |
| ρl | 807.46 | kg/m3 | 303.15 | Thermod... |
| ρl | 807.07 | kg/m3 | 303.15 | Excess ... |
| ρl | 807.10 | kg/m3 | 303.15 | Correla... |
| ρl | 807.74 | kg/m3 | 303.15 | Volumet... |
| ρl | 807.55 | kg/m3 | 303.15 | Densiti... |
| ρl | 807.57 | kg/m3 | 303.15 | Densiti... |
| ρl | 810.00 | kg/m3 | 303.15 | Study o... |
| ρl | 807.10 | kg/m3 | 303.15 | FT-IR s... |
| ρl | 807.28 | kg/m3 | 303.15 | Influen... |
| ρl | 803.00 | kg/m3 | 308.00 | Compara... |
| ρl | 803.67 | kg/m3 | 308.15 | Densiti... |
| ρl | 804.01 | kg/m3 | 308.15 | Volumet... |
| ρl | 803.52 | kg/m3 | 308.15 | Osmotic... |
| ρl | 803.38 | kg/m3 | 308.15 | FT-IR s... |
| ρl | 803.68 | kg/m3 | 308.15 | Densiti... |
| ρl | 803.70 | kg/m3 | 308.15 | Excess ... |
| ρl | 804.10 | kg/m3 | 308.15 | Tempera... |
| ρl | 803.70 | kg/m3 | 308.15 | The stu... |
| ρl | 803.74 | kg/m3 | 308.15 | Thermod... |
| ρl | 803.53 | kg/m3 | 308.15 | Volumet... |
| ρl | 803.86 | kg/m3 | 308.15 | Densiti... |
| ρl | 803.83 | kg/m3 | 308.15 | Densiti... |
| ρl | 803.50 | kg/m3 | 308.15 | Physica... |
| ρl | 803.30 | kg/m3 | 308.15 | Thermod... |
| ρl | 803.30 | kg/m3 | 308.15 | Correla... |
| ρl | 803.56 | kg/m3 | 308.15 | Influen... |
| ρl | 800.00 | kg/m3 | 313.00 | Compara... |
| ρl | 799.82 | kg/m3 | 313.15 | Influen... |
| ρl | 800.57 | kg/m3 | 313.15 | Excess ... |
| ρl | 800.08 | kg/m3 | 313.15 | Densiti... |
| ρl | 800.11 | kg/m3 | 313.15 | Densiti... |
| ρl | 799.79 | kg/m3 | 313.15 | Volumet... |
| ρl | 800.26 | kg/m3 | 313.15 | Excess ... |
| ρl | 799.71 | kg/m3 | 313.15 | Excess ... |
| ρl | 799.60 | kg/m3 | 313.15 | Correla... |
| ρl | 799.94 | kg/m3 | 313.15 | Densiti... |
| ρl | 799.90 | kg/m3 | 313.15 | Densiti... |
| ρl | 799.40 | kg/m3 | 313.15 | Excess ... |
| ρl | 799.80 | kg/m3 | 313.15 | Excess ... |
| ρl | 800.24 | kg/m3 | 313.15 | Volumet... |
| ρl | 799.99 | kg/m3 | 313.15 | Thermod... |
| ρl | 796.32 | kg/m3 | 318.15 | Densiti... |
| ρl | 796.43 | kg/m3 | 318.15 | Volumet... |
| ρl | 796.17 | kg/m3 | 318.15 | Densiti... |
| ρl | 796.10 | kg/m3 | 318.15 | The stu... |
| ρl | 796.03 | kg/m3 | 318.15 | Volumet... |
| ρl | 795.98 | kg/m3 | 318.15 | Physica... |
| ρl | 796.29 | kg/m3 | 318.15 | Densiti... |
| ρl | 795.80 | kg/m3 | 318.15 | Correla... |
| ρl | 792.48 | kg/m3 | 323.15 | Densiti... |
| ρl | 792.15 | kg/m3 | 323.15 | Osmotic... |
| ρl | 792.46 | kg/m3 | 323.15 | Densiti... |
| ρl | 792.14 | kg/m3 | 323.15 | Osmotic... |
| ρl | 792.23 | kg/m3 | 323.15 | Volumet... |
| ρl | 792.57 | kg/m3 | 323.15 | Volumet... |
| ρl | 792.36 | kg/m3 | 323.15 | Densiti... |
| ρl | 792.00 | kg/m3 | 323.15 | Correla... |
| ρl | 789.01 | kg/m3 | 328.15 | Excess ... |
| ρl | 788.50 | kg/m3 | 328.15 | Densiti... |
| ρl | 788.74 | kg/m3 | 328.15 | Excess ... |
| ρl | 788.61 | kg/m3 | 328.15 | Densiti... |
| ρl | 788.67 | kg/m3 | 328.15 | Volumet... |
| ρl | 788.82 | kg/m3 | 328.15 | Excess ... |
| ρl | 788.40 | kg/m3 | 328.15 | The stu... |
| ρl | 788.56 | kg/m3 | 328.15 | Densiti... |
| ρl | 784.72 | kg/m3 | 333.15 | Volumet... |
| ρl | 784.59 | kg/m3 | 333.15 | Densiti... |
| ρl | 784.66 | kg/m3 | 333.15 | Densiti... |
| ρl | 780.70 | kg/m3 | 338.15 | Densiti... |
| ρl | 781.05 | kg/m3 | 338.15 | Excess ... |
| ρl | 780.62 | kg/m3 | 338.15 | Densiti... |
| ρl | 776.58 | kg/m3 | 343.15 | Densiti... |
| ρl | 772.49 | kg/m3 | 348.15 | Densiti... |
| ρl | 772.87 | kg/m3 | 348.15 | Excess ... |
| ρl | 768.33 | kg/m3 | 353.15 | Densiti... |
| ρl | 764.08 | kg/m3 | 358.15 | Densiti... |
| ρl | 759.77 | kg/m3 | 363.15 | Densiti... |
| D*i | [0.00; 0.00] | m2/s | [253.13; 364.73] |
|
|
T(K) Self diffusion coefficient (m2/s) 0 5.00e-10 1.00e-9 1.50e-9 2.00e-9 300 350 | ||||
| D*i | 0.00 | m2/s | 253.13 | Viscous... |
| D*i | 0.00 | m2/s | 253.19 | Viscous... |
| D*i | 0.00 | m2/s | 258.42 | Viscous... |
| D*i | 0.00 | m2/s | 258.47 | Viscous... |
| D*i | 0.00 | m2/s | 263.25 | Viscous... |
| D*i | 0.00 | m2/s | 263.28 | Viscous... |
| D*i | 0.00 | m2/s | 268.65 | Viscous... |
| D*i | 0.00 | m2/s | 268.66 | Viscous... |
| D*i | 0.00 | m2/s | 278.40 | Viscous... |
| D*i | 0.00 | m2/s | 278.43 | Viscous... |
| D*i | 0.00 | m2/s | 288.31 | Viscous... |
| D*i | 0.00 | m2/s | 288.33 | Viscous... |
| D*i | 0.00 | m2/s | 298.16 | Viscous... |
| D*i | 0.00 | m2/s | 298.17 | Viscous... |
| D*i | 0.00 | m2/s | 298.19 | Viscous... |
| D*i | 0.00 | m2/s | 298.21 | Viscous... |
| D*i | 0.00 | m2/s | 298.21 | Viscous... |
| D*i | 0.00 | m2/s | 298.27 | Viscous... |
| D*i | 0.00 | m2/s | 298.27 | Viscous... |
| D*i | 0.00 | m2/s | 308.09 | Viscous... |
| D*i | 0.00 | m2/s | 308.11 | Viscous... |
| D*i | 0.00 | m2/s | 318.08 | Viscous... |
| D*i | 0.00 | m2/s | 318.09 | Viscous... |
| D*i | 0.00 | m2/s | 323.10 | Viscous... |
| D*i | 0.00 | m2/s | 323.10 | Viscous... |
| D*i | 0.00 | m2/s | 323.15 | Viscous... |
| D*i | 0.00 | m2/s | 323.15 | Viscous... |
| D*i | 0.00 | m2/s | 327.86 | Viscous... |
| D*i | 0.00 | m2/s | 327.86 | Viscous... |
| D*i | 0.00 | m2/s | 337.71 | Viscous... |
| D*i | 0.00 | m2/s | 337.74 | Viscous... |
| D*i | 0.00 | m2/s | 347.21 | Viscous... |
| D*i | 0.00 | m2/s | 347.25 | Viscous... |
| D*i | 0.00 | m2/s | 352.35 | Viscous... |
| D*i | 0.00 | m2/s | 352.36 | Viscous... |
| D*i | 0.00 | m2/s | 352.55 | Viscous... |
| D*i | 0.00 | m2/s | 364.52 | Viscous... |
| D*i | 0.00 | m2/s | 364.59 | Viscous... |
| D*i | 0.00 | m2/s | 364.73 | Viscous... |
| ΔfusS | [50.61; 53.70] | J/mol×K | [194.20; 195.56] |
|
| ΔfusS | 50.61 | J/mol×K | 194.20 | NIST |
| ΔfusS | 53.70 | J/mol×K | 195.56 | NIST |
| csound,fluid | [1192.80; 1325.90] | m/s | [283.15; 323.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1180 1200 1220 1240 1260 1280 1300 1320 290 300 310 320 | ||||
| csound,fluid | 1325.90 | m/s | 283.15 | Excess ... |
| csound,fluid | 1312.50 | m/s | 288.15 | Densiti... |
| csound,fluid | 1292.50 | m/s | 293.15 | Acousti... |
| csound,fluid | 1293.45 | m/s | 293.15 | Densiti... |
| csound,fluid | 1276.01 | m/s | 298.15 | Densiti... |
| csound,fluid | 1274.00 | m/s | 298.15 | Densiti... |
| csound,fluid | 1274.10 | m/s | 298.15 | Excess ... |
| csound,fluid | 1281.20 | m/s | 298.15 | Ultraso... |
| csound,fluid | 1274.32 | m/s | 298.15 | Densiti... |
| csound,fluid | 1258.25 | m/s | 303.15 | Densiti... |
| csound,fluid | 1243.67 | m/s | 308.15 | Densiti... |
| csound,fluid | 1240.00 | m/s | 308.15 | Densiti... |
| csound,fluid | 1242.40 | m/s | 308.15 | Acousti... |
| csound,fluid | 1225.50 | m/s | 313.15 | Excess ... |
| csound,fluid | 1192.80 | m/s | 323.15 | Acousti... |
| γ | [0.02; 0.03] | N/m | [293.15; 323.15] |
|
|
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.03 0.03 0.03 300 310 320 | ||||
| γ | 0.03 | N/m | 293.15 | Density... |
| γ | 0.03 | N/m | 293.15 | The add... |
| γ | 0.03 | N/m | 293.15 | Surface... |
| γ | 0.03 | N/m | 293.20 | KDB |
| γ | 0.03 | N/m | 298.15 | Surface... |
| γ | 0.03 | N/m | 298.15 | Surface... |
| γ | 0.02 | N/m | 298.15 | The add... |
| γ | 0.02 | N/m | 303.15 | Surface... |
| γ | 0.02 | N/m | 303.15 | The add... |
| γ | 0.02 | N/m | 303.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | The add... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 313.15 | The add... |
| γ | 0.02 | N/m | 313.15 | Surface... |
| γ | 0.02 | N/m | 313.15 | Surface... |
| γ | 0.02 | N/m | 318.15 | Surface... |
| γ | 0.02 | N/m | 318.15 | The add... |
| γ | 0.02 | N/m | 318.15 | Surface... |
| γ | 0.02 | N/m | 323.15 | Surface... |
| γ | 0.02 | N/m | 323.15 | Surface... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 323.20 | K | 1.70 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 814.7 |
| 293.15 | 10000.00 | 821.1 |
| 293.15 | 20000.00 | 827.3 |
| 293.15 | 30000.00 | 833.2 |
| 293.15 | 40000.00 | 838.6 |
| 293.15 | 50000.00 | 843.6 |
| 293.15 | 60000.00 | 848.5 |
| 293.15 | 70000.00 | 853.1 |
| 293.15 | 80000.00 | 857.4 |
| 293.15 | 90000.00 | 861.7 |
| 293.15 | 100000.00 | 865.8 |
| 293.15 | 110000.00 | 869.6 |
| 293.15 | 120000.00 | 873.2 |
| 293.15 | 130000.00 | 876.9 |
| 293.15 | 140000.00 | 880.3 |
| 303.15 | 100.00 | 807.3 |
| 303.15 | 10000.00 | 814.4 |
| 303.15 | 20000.00 | 820.7 |
| 303.15 | 30000.00 | 826.7 |
| 303.15 | 40000.00 | 832.2 |
| 303.15 | 50000.00 | 837.5 |
| 303.15 | 60000.00 | 842.4 |
| 303.15 | 70000.00 | 847.0 |
| 303.15 | 80000.00 | 851.6 |
| 303.15 | 90000.00 | 855.8 |
| 303.15 | 100000.00 | 860.1 |
| 303.15 | 110000.00 | 864.1 |
| 303.15 | 120000.00 | 868.0 |
| 303.15 | 130000.00 | 871.7 |
| 303.15 | 140000.00 | 875.2 |
| 313.15 | 100.00 | 799.8 |
| 313.15 | 10000.00 | 807.4 |
| 313.15 | 20000.00 | 814.1 |
| 313.15 | 30000.00 | 820.2 |
| 313.15 | 40000.00 | 826.0 |
| 313.15 | 50000.00 | 831.5 |
| 313.15 | 60000.00 | 836.6 |
| 313.15 | 70000.00 | 841.4 |
| 313.15 | 80000.00 | 846.1 |
| 313.15 | 90000.00 | 850.5 |
| 313.15 | 100000.00 | 854.8 |
| 313.15 | 110000.00 | 858.9 |
| 313.15 | 120000.00 | 862.8 |
| 313.15 | 130000.00 | 866.6 |
| 313.15 | 140000.00 | 870.2 |
| 323.15 | 100.00 | 792.5 |
| 323.15 | 10000.00 | 800.3 |
| 323.15 | 20000.00 | 807.3 |
| 323.15 | 30000.00 | 813.7 |
| 323.15 | 40000.00 | 819.8 |
| 323.15 | 50000.00 | 825.4 |
| 323.15 | 60000.00 | 830.7 |
| 323.15 | 70000.00 | 835.7 |
| 323.15 | 80000.00 | 840.4 |
| 323.15 | 90000.00 | 845.0 |
| 323.15 | 100000.00 | 849.3 |
| 323.15 | 110000.00 | 853.6 |
| 323.15 | 120000.00 | 857.6 |
| 323.15 | 130000.00 | 861.5 |
| 323.15 | 140000.00 | 865.3 |
| 333.15 | 100.00 | 784.4 |
| 333.15 | 10000.00 | 792.7 |
| 333.15 | 20000.00 | 800.1 |
| 333.15 | 30000.00 | 806.8 |
| 333.15 | 40000.00 | 813.1 |
| 333.15 | 50000.00 | 818.9 |
| 333.15 | 60000.00 | 824.4 |
| 333.15 | 70000.00 | 829.7 |
| 333.15 | 80000.00 | 834.6 |
| 333.15 | 90000.00 | 839.2 |
| 333.15 | 100000.00 | 843.7 |
| 333.15 | 110000.00 | 848.0 |
| 333.15 | 120000.00 | 852.1 |
| 333.15 | 130000.00 | 856.0 |
| 333.15 | 140000.00 | 860.0 |
| 343.15 | 100.00 | 776.5 |
| 343.15 | 10000.00 | 785.2 |
| 343.15 | 20000.00 | 792.9 |
| 343.15 | 30000.00 | 799.9 |
| 343.15 | 40000.00 | 806.6 |
| 343.15 | 50000.00 | 812.6 |
| 343.15 | 60000.00 | 818.3 |
| 343.15 | 70000.00 | 823.7 |
| 343.15 | 80000.00 | 828.7 |
| 343.15 | 90000.00 | 833.5 |
| 343.15 | 100000.00 | 838.2 |
| 343.15 | 110000.00 | 842.5 |
| 343.15 | 120000.00 | 846.8 |
| 343.15 | 130000.00 | 850.9 |
| 343.15 | 140000.00 | 854.8 |
| 353.15 | 100.00 | 768.1 |
| 353.15 | 10000.00 | 777.3 |
| 353.15 | 20000.00 | 785.6 |
| 353.15 | 30000.00 | 792.9 |
| 353.15 | 40000.00 | 799.8 |
| 353.15 | 50000.00 | 806.1 |
| 353.15 | 60000.00 | 812.0 |
| 353.15 | 70000.00 | 817.6 |
| 353.15 | 80000.00 | 822.8 |
| 353.15 | 90000.00 | 827.8 |
| 353.15 | 100000.00 | 832.6 |
| 353.15 | 110000.00 | 837.2 |
| 353.15 | 120000.00 | 841.6 |
| 353.15 | 130000.00 | 845.8 |
| 353.15 | 140000.00 | 849.7 |
| 363.15 | 100.00 | 759.4 |
| 363.15 | 10000.00 | 769.2 |
| 363.15 | 20000.00 | 777.7 |
| 363.15 | 30000.00 | 785.6 |
| 363.15 | 40000.00 | 792.6 |
| 363.15 | 50000.00 | 799.2 |
| 363.15 | 60000.00 | 805.5 |
| 363.15 | 70000.00 | 811.3 |
| 363.15 | 80000.00 | 816.7 |
| 363.15 | 90000.00 | 821.8 |
| 363.15 | 100000.00 | 826.8 |
| 363.15 | 110000.00 | 831.3 |
| 363.15 | 120000.00 | 835.8 |
| 363.15 | 130000.00 | 840.1 |
| 363.15 | 140000.00 | 844.2 |
| 373.15 | 100.00 | 750.7 |
| 373.15 | 10000.00 | 761.2 |
| 373.15 | 20000.00 | 770.3 |
| 373.15 | 30000.00 | 778.2 |
| 373.15 | 40000.00 | 785.7 |
| 373.15 | 50000.00 | 792.5 |
| 373.15 | 60000.00 | 798.9 |
| 373.15 | 70000.00 | 804.9 |
| 373.15 | 80000.00 | 810.5 |
| 373.15 | 90000.00 | 815.8 |
| 373.15 | 100000.00 | 820.9 |
| 373.15 | 110000.00 | 825.7 |
| 373.15 | 120000.00 | 830.3 |
| 373.15 | 130000.00 | 834.7 |
| 373.15 | 140000.00 | 839.0 |
| 383.15 | 100.00 | 741.5 |
| 383.15 | 10000.00 | 752.3 |
| 383.15 | 20000.00 | 761.9 |
| 383.15 | 30000.00 | 770.7 |
| 383.15 | 40000.00 | 778.5 |
| 383.15 | 50000.00 | 785.7 |
| 383.15 | 60000.00 | 792.3 |
| 383.15 | 70000.00 | 798.5 |
| 383.15 | 80000.00 | 804.3 |
| 383.15 | 90000.00 | 809.7 |
| 383.15 | 100000.00 | 815.0 |
| 383.15 | 110000.00 | 819.9 |
| 383.15 | 120000.00 | 824.7 |
| 383.15 | 130000.00 | 829.2 |
| 383.15 | 140000.00 | 833.5 |
| 393.15 | 100.00 | 731.7 |
| 393.15 | 10000.00 | 743.4 |
| 393.15 | 20000.00 | 753.7 |
| 393.15 | 30000.00 | 762.8 |
| 393.15 | 40000.00 | 771.0 |
| 393.15 | 50000.00 | 778.6 |
| 393.15 | 60000.00 | 785.6 |
| 393.15 | 70000.00 | 792.0 |
| 393.15 | 80000.00 | 798.1 |
| 393.15 | 90000.00 | 803.7 |
| 393.15 | 100000.00 | 809.1 |
| 393.15 | 110000.00 | 814.2 |
| 393.15 | 120000.00 | 819.1 |
| 393.15 | 130000.00 | 823.7 |
| 393.15 | 140000.00 | 828.1 |
| 403.15 | 100.00 | 721.7 |
| 403.15 | 10000.00 | 734.4 |
| 403.15 | 20000.00 | 745.3 |
| 403.15 | 30000.00 | 754.9 |
| 403.15 | 40000.00 | 763.4 |
| 403.15 | 50000.00 | 771.3 |
| 403.15 | 60000.00 | 778.4 |
| 403.15 | 70000.00 | 785.1 |
| 403.15 | 80000.00 | 791.3 |
| 403.15 | 90000.00 | 797.2 |
| 403.15 | 100000.00 | 802.8 |
| 403.15 | 110000.00 | 808.0 |
| 403.15 | 120000.00 | 813.0 |
| 403.15 | 130000.00 | 817.8 |
| 403.15 | 140000.00 | 822.3 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 810.8 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Fluid (supercritical or subcritical phases) | Pressure, kPa - Fluid (supercritical or subcritical phases) | Mass density, kg/m3 - Fluid (supercritical or subcritical phases) |
| 312.96 | 512.00 | 799.65 |
| 312.96 | 1022.00 | 800.04 |
| 312.96 | 1998.00 | 800.77 |
| 312.96 | 3005.00 | 801.53 |
| 312.96 | 4003.00 | 802.28 |
| 312.96 | 5002.00 | 803.02 |
| 312.96 | 6018.00 | 803.76 |
| 312.96 | 6994.00 | 804.49 |
| 312.96 | 8008.00 | 805.21 |
| 312.96 | 9005.00 | 805.93 |
| 312.96 | 10008.00 | 806.66 |
| 312.96 | 11008.00 | 807.37 |
| 312.96 | 12000.00 | 808.07 |
| 312.96 | 13024.00 | 808.78 |
| 312.96 | 13987.00 | 809.45 |
| 312.96 | 15014.00 | 810.14 |
| 312.96 | 15991.00 | 810.8 |
| 312.96 | 17019.00 | 811.48 |
| 312.96 | 17991.00 | 812.12 |
| 312.96 | 19007.00 | 812.79 |
| 312.96 | 19992.00 | 813.44 |
| 312.96 | 21031.00 | 814.1 |
| 312.96 | 22041.00 | 814.76 |
| 312.96 | 23014.00 | 815.41 |
| 312.96 | 24003.00 | 816.04 |
| 312.96 | 25037.00 | 816.73 |
| 322.89 | 520.00 | 792.06 |
| 322.89 | 1010.00 | 792.47 |
| 322.89 | 2005.00 | 793.27 |
| 322.89 | 3007.00 | 794.07 |
| 322.89 | 4005.00 | 794.86 |
| 322.89 | 5018.00 | 795.63 |
| 322.89 | 6001.00 | 796.42 |
| 322.89 | 7016.00 | 797.2 |
| 322.89 | 8020.00 | 797.97 |
| 322.89 | 8997.00 | 798.71 |
| 322.89 | 10001.00 | 799.47 |
| 322.89 | 11005.00 | 800.21 |
| 322.89 | 11996.00 | 800.95 |
| 322.89 | 13002.00 | 801.68 |
| 322.89 | 14013.00 | 802.4 |
| 322.89 | 15005.00 | 803.11 |
| 322.89 | 16014.00 | 803.82 |
| 322.89 | 17001.00 | 804.51 |
| 322.89 | 18016.00 | 805.21 |
| 322.89 | 19012.00 | 805.89 |
| 322.89 | 19992.00 | 806.56 |
| 322.89 | 21036.00 | 807.26 |
| 322.89 | 22003.00 | 807.92 |
| 322.89 | 23024.00 | 808.61 |
| 322.89 | 23994.00 | 809.26 |
| 322.89 | 25023.00 | 810.0 |
| 332.79 | 493.00 | 784.29 |
| 332.79 | 1014.00 | 784.76 |
| 332.79 | 2006.00 | 785.61 |
| 332.79 | 3025.00 | 786.48 |
| 332.79 | 4011.00 | 787.28 |
| 332.79 | 5020.00 | 788.11 |
| 332.79 | 6003.00 | 788.91 |
| 332.79 | 6997.00 | 789.73 |
| 332.79 | 8009.00 | 790.54 |
| 332.79 | 8995.00 | 791.31 |
| 332.79 | 9996.00 | 792.12 |
| 332.79 | 11018.00 | 792.9 |
| 332.79 | 11995.00 | 793.66 |
| 332.79 | 13023.00 | 794.45 |
| 332.79 | 13999.00 | 795.19 |
| 332.79 | 15010.00 | 795.95 |
| 332.79 | 16028.00 | 796.68 |
| 332.79 | 17003.00 | 797.41 |
| 332.79 | 18040.00 | 798.14 |
| 332.79 | 19004.00 | 798.84 |
| 332.79 | 20035.00 | 799.59 |
| 332.79 | 21024.00 | 800.29 |
| 332.79 | 21993.00 | 800.97 |
| 332.79 | 23039.00 | 801.71 |
| 332.79 | 24015.00 | 802.4 |
| 332.79 | 25022.00 | 803.12 |
| 342.76 | 505.00 | 776.31 |
| 342.76 | 997.00 | 776.77 |
| 342.76 | 1995.00 | 777.69 |
| 342.76 | 3011.00 | 778.59 |
| 342.76 | 4012.00 | 779.47 |
| 342.76 | 5011.00 | 780.34 |
| 342.76 | 6011.00 | 781.22 |
| 342.76 | 7003.00 | 782.03 |
| 342.76 | 8015.00 | 782.91 |
| 342.76 | 9000.00 | 783.73 |
| 342.76 | 10019.00 | 784.58 |
| 342.76 | 11020.00 | 785.4 |
| 342.76 | 12002.00 | 786.2 |
| 342.76 | 13016.00 | 787.02 |
| 342.76 | 14024.00 | 787.81 |
| 342.76 | 15002.00 | 788.59 |
| 342.76 | 16007.00 | 789.36 |
| 342.76 | 17037.00 | 790.15 |
| 342.76 | 17988.00 | 790.87 |
| 342.76 | 19037.00 | 791.66 |
| 342.76 | 20003.00 | 792.38 |
| 342.76 | 21015.00 | 793.14 |
| 342.76 | 22019.00 | 793.88 |
| 342.76 | 23039.00 | 794.62 |
| 342.76 | 24027.00 | 795.36 |
| 342.76 | 25028.00 | 796.1 |
| 352.71 | 508.00 | 768.15 |
| 352.71 | 1011.00 | 768.66 |
| 352.71 | 1995.00 | 769.61 |
| 352.71 | 3014.00 | 770.57 |
| 352.71 | 3998.00 | 771.49 |
| 352.71 | 5022.00 | 772.45 |
| 352.71 | 6012.00 | 773.35 |
| 352.71 | 7006.00 | 774.26 |
| 352.71 | 8024.00 | 775.17 |
| 352.71 | 9005.00 | 776.05 |
| 352.71 | 10016.00 | 776.94 |
| 352.71 | 11026.00 | 777.81 |
| 352.71 | 12001.00 | 778.65 |
| 352.71 | 13002.00 | 779.5 |
| 352.71 | 14026.00 | 780.35 |
| 352.71 | 15000.00 | 781.18 |
| 352.71 | 16005.00 | 781.98 |
| 352.71 | 17023.00 | 782.81 |
| 352.71 | 18003.00 | 783.59 |
| 352.71 | 19049.00 | 784.43 |
| 352.71 | 20035.00 | 785.2 |
| 352.71 | 21002.00 | 785.96 |
| 352.71 | 21995.00 | 786.73 |
| 352.71 | 23020.00 | 787.52 |
| 352.71 | 24045.00 | 788.32 |
| 352.71 | 25009.00 | 789.05 |
| 362.59 | 517.00 | 759.7 |
| 362.59 | 1023.00 | 760.25 |
| 362.59 | 2005.00 | 761.26 |
| 362.59 | 3010.00 | 762.29 |
| 362.59 | 3998.00 | 763.28 |
| 362.59 | 5006.00 | 764.25 |
| 362.59 | 6013.00 | 765.23 |
| 362.59 | 7014.00 | 766.21 |
| 362.59 | 8007.00 | 767.16 |
| 362.59 | 9020.00 | 768.1 |
| 362.59 | 10006.00 | 769.02 |
| 362.59 | 10991.00 | 769.93 |
| 362.59 | 12025.00 | 770.87 |
| 362.59 | 13008.00 | 771.76 |
| 362.59 | 13998.00 | 772.62 |
| 362.59 | 15017.00 | 773.51 |
| 362.59 | 16000.00 | 774.37 |
| 362.59 | 17013.00 | 775.24 |
| 362.59 | 18032.00 | 776.11 |
| 362.59 | 19003.00 | 776.9 |
| 362.59 | 20030.00 | 777.77 |
| 362.59 | 20987.00 | 778.55 |
| 362.59 | 22033.00 | 779.4 |
| 362.59 | 23000.00 | 780.2 |
| 362.59 | 24031.00 | 781.02 |
| 362.59 | 25026.00 | 781.82 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 100.00 | 825.2 |
| 278.15 | 1000.00 | 825.8 |
| 278.15 | 5000.00 | 828.5 |
| 278.15 | 10000.00 | 831.6 |
| 278.15 | 15000.00 | 834.7 |
| 278.15 | 20000.00 | 837.6 |
| 278.15 | 25000.00 | 840.4 |
| 278.15 | 30000.00 | 843.2 |
| 278.15 | 35000.00 | 845.9 |
| 278.15 | 40000.00 | 848.6 |
| 278.15 | 45000.00 | 851.1 |
| 278.15 | 50000.00 | 853.6 |
| 278.15 | 55000.00 | 856.1 |
| 278.15 | 60000.00 | 858.4 |
| 288.15 | 100.00 | 818.0 |
| 288.15 | 1000.00 | 818.7 |
| 288.15 | 5000.00 | 821.5 |
| 288.15 | 10000.00 | 824.8 |
| 288.15 | 15000.00 | 828.0 |
| 288.15 | 20000.00 | 831.1 |
| 288.15 | 25000.00 | 834.0 |
| 288.15 | 30000.00 | 836.9 |
| 288.15 | 35000.00 | 839.7 |
| 288.15 | 40000.00 | 842.4 |
| 288.15 | 45000.00 | 845.0 |
| 288.15 | 50000.00 | 847.6 |
| 288.15 | 55000.00 | 850.1 |
| 288.15 | 60000.00 | 852.5 |
| 298.15 | 100.00 | 810.7 |
| 298.15 | 1000.00 | 811.3 |
| 298.15 | 5000.00 | 814.2 |
| 298.15 | 10000.00 | 817.7 |
| 298.15 | 15000.00 | 821.0 |
| 298.15 | 20000.00 | 824.3 |
| 298.15 | 25000.00 | 827.3 |
| 298.15 | 30000.00 | 830.3 |
| 298.15 | 35000.00 | 833.2 |
| 298.15 | 40000.00 | 836.0 |
| 298.15 | 45000.00 | 838.7 |
| 298.15 | 50000.00 | 841.4 |
| 298.15 | 55000.00 | 844.0 |
| 298.15 | 60000.00 | 846.4 |
| 308.15 | 100.00 | 803.3 |
| 308.15 | 1000.00 | 804.0 |
| 308.15 | 5000.00 | 807.0 |
| 308.15 | 10000.00 | 810.7 |
| 308.15 | 15000.00 | 814.0 |
| 308.15 | 20000.00 | 817.5 |
| 308.15 | 25000.00 | 820.7 |
| 308.15 | 30000.00 | 823.8 |
| 308.15 | 35000.00 | 826.8 |
| 308.15 | 40000.00 | 829.7 |
| 308.15 | 45000.00 | 832.5 |
| 308.15 | 50000.00 | 835.3 |
| 308.15 | 55000.00 | 838.0 |
| 308.15 | 60000.00 | 840.4 |
| 318.15 | 100.00 | 795.8 |
| 318.15 | 1000.00 | 796.6 |
| 318.15 | 5000.00 | 799.8 |
| 318.15 | 10000.00 | 803.6 |
| 318.15 | 15000.00 | 807.2 |
| 318.15 | 20000.00 | 810.7 |
| 318.15 | 25000.00 | 814.0 |
| 318.15 | 30000.00 | 817.3 |
| 318.15 | 35000.00 | 820.4 |
| 318.15 | 40000.00 | 823.4 |
| 318.15 | 45000.00 | 826.3 |
| 318.15 | 50000.00 | 829.1 |
| 318.15 | 55000.00 | 831.9 |
| 318.15 | 60000.00 | 834.6 |
| 328.15 | 100.00 | 788.2 |
| 328.15 | 1000.00 | 789.0 |
| 328.15 | 5000.00 | 792.3 |
| 328.15 | 10000.00 | 796.3 |
| 328.15 | 15000.00 | 800.1 |
| 328.15 | 20000.00 | 803.8 |
| 328.15 | 25000.00 | 807.2 |
| 328.15 | 30000.00 | 810.6 |
| 328.15 | 35000.00 | 813.8 |
| 328.15 | 40000.00 | 817.0 |
| 328.15 | 45000.00 | 820.0 |
| 328.15 | 50000.00 | 822.9 |
| 328.15 | 55000.00 | 825.8 |
| 328.15 | 60000.00 | 828.4 |
| 338.15 | 100.00 | 780.3 |
| 338.15 | 1000.00 | 781.2 |
| 338.15 | 5000.00 | 784.8 |
| 338.15 | 10000.00 | 788.9 |
| 338.15 | 15000.00 | 792.9 |
| 338.15 | 20000.00 | 796.7 |
| 338.15 | 25000.00 | 800.3 |
| 338.15 | 30000.00 | 803.8 |
| 338.15 | 35000.00 | 807.2 |
| 338.15 | 40000.00 | 810.5 |
| 338.15 | 45000.00 | 813.6 |
| 338.15 | 50000.00 | 816.6 |
| 338.15 | 55000.00 | 819.6 |
| 338.15 | 60000.00 | 822.5 |
| 348.15 | 100.00 | 772.3 |
| 348.15 | 1000.00 | 773.1 |
| 348.15 | 5000.00 | 776.9 |
| 348.15 | 10000.00 | 781.2 |
| 348.15 | 15000.00 | 785.5 |
| 348.15 | 20000.00 | 789.5 |
| 348.15 | 25000.00 | 793.3 |
| 348.15 | 30000.00 | 796.9 |
| 348.15 | 35000.00 | 800.4 |
| 348.15 | 40000.00 | 803.8 |
| 348.15 | 45000.00 | 807.1 |
| 348.15 | 50000.00 | 810.3 |
| 348.15 | 55000.00 | 813.3 |
| 348.15 | 60000.00 | 816.2 |
| 358.15 | 100.00 | 763.8 |
| 358.15 | 1000.00 | 764.8 |
| 358.15 | 5000.00 | 768.8 |
| 358.15 | 10000.00 | 773.5 |
| 358.15 | 15000.00 | 777.9 |
| 358.15 | 20000.00 | 782.1 |
| 358.15 | 25000.00 | 786.1 |
| 358.15 | 30000.00 | 789.9 |
| 358.15 | 35000.00 | 793.6 |
| 358.15 | 40000.00 | 797.1 |
| 358.15 | 45000.00 | 800.5 |
| 358.15 | 50000.00 | 803.8 |
| 358.15 | 55000.00 | 807.0 |
| 358.15 | 60000.00 | 810.0 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 2003.00 | 811.93 |
| 298.15 | 3999.00 | 813.3 |
| 298.15 | 6003.00 | 814.64 |
| 298.15 | 8005.00 | 815.96 |
| 298.15 | 10001.00 | 817.26 |
| 298.15 | 13000.00 | 819.15 |
| 298.15 | 16004.00 | 821.0 |
| 298.15 | 19006.00 | 822.8 |
| 298.15 | 22000.00 | 824.56 |
| 298.15 | 24998.00 | 826.27 |
| 323.15 | 1999.00 | 794.19 |
| 323.15 | 4001.00 | 795.77 |
| 323.15 | 6001.00 | 797.32 |
| 323.15 | 8000.00 | 798.83 |
| 323.15 | 9998.00 | 800.31 |
| 323.15 | 12999.00 | 802.47 |
| 323.15 | 16001.00 | 804.56 |
| 323.15 | 19002.00 | 806.59 |
| 323.15 | 22001.00 | 808.56 |
| 323.15 | 25002.00 | 810.48 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 2000.00 | 813.0 |
| 298.15 | 4000.00 | 814.4 |
| 298.15 | 6000.00 | 815.8 |
| 298.15 | 8010.00 | 817.1 |
| 298.15 | 10000.00 | 818.5 |
| 298.15 | 13000.00 | 820.4 |
| 298.15 | 16000.00 | 822.3 |
| 298.15 | 19010.00 | 824.1 |
| 298.15 | 22000.00 | 825.9 |
| 298.15 | 25000.00 | 827.6 |
| 298.15 | 27990.00 | 829.4 |
| 298.15 | 29980.00 | 830.4 |
| 303.16 | 1980.00 | 808.8 |
| 303.16 | 3980.00 | 810.2 |
| 303.16 | 6010.00 | 811.7 |
| 303.16 | 8020.00 | 813.0 |
| 303.16 | 10030.00 | 814.4 |
| 303.16 | 12990.00 | 816.4 |
| 303.16 | 15980.00 | 818.4 |
| 303.15 | 19000.00 | 820.3 |
| 303.16 | 22010.00 | 822.1 |
| 303.16 | 25000.00 | 823.9 |
| 303.15 | 27980.00 | 825.6 |
| 303.16 | 29990.00 | 826.7 |
| 313.15 | 1990.00 | 800.6 |
| 313.15 | 4000.00 | 802.2 |
| 313.15 | 5980.00 | 803.7 |
| 313.15 | 7980.00 | 805.1 |
| 313.15 | 10020.00 | 806.6 |
| 313.15 | 13010.00 | 808.7 |
| 313.16 | 15980.00 | 810.8 |
| 313.15 | 19020.00 | 812.8 |
| 313.15 | 21980.00 | 814.7 |
| 313.16 | 24990.00 | 816.6 |
| 313.16 | 28000.00 | 818.4 |
| 313.15 | 30020.00 | 819.6 |
| 323.15 | 2000.00 | 793.5 |
| 323.15 | 4000.00 | 795.0 |
| 323.15 | 6000.00 | 796.7 |
| 323.15 | 8000.00 | 798.2 |
| 323.15 | 10000.00 | 799.6 |
| 323.15 | 13000.00 | 801.9 |
| 323.15 | 16000.00 | 804.0 |
| 323.15 | 19000.00 | 806.1 |
| 323.15 | 22000.00 | 808.2 |
| 323.15 | 25000.00 | 810.2 |
| 323.15 | 27990.00 | 812.1 |
| 323.15 | 29990.00 | 813.4 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 815.25 |
| 293.15 | 5000.00 | 818.83 |
| 293.15 | 10000.00 | 822.19 |
| 293.15 | 15000.00 | 825.37 |
| 293.15 | 20000.00 | 828.41 |
| 293.15 | 25000.00 | 831.36 |
| 293.15 | 30000.00 | 834.24 |
| 293.15 | 35000.00 | 837.11 |
| 303.15 | 100.00 | 808.05 |
| 303.15 | 5000.00 | 811.93 |
| 303.15 | 10000.00 | 815.5 |
| 303.15 | 15000.00 | 818.82 |
| 303.15 | 20000.00 | 821.92 |
| 303.15 | 25000.00 | 824.88 |
| 303.15 | 30000.00 | 827.74 |
| 303.15 | 35000.00 | 830.55 |
| 313.15 | 100.00 | 800.67 |
| 313.15 | 5000.00 | 804.61 |
| 313.15 | 10000.00 | 808.28 |
| 313.15 | 15000.00 | 811.75 |
| 313.15 | 20000.00 | 815.06 |
| 313.15 | 25000.00 | 818.26 |
| 313.15 | 30000.00 | 821.41 |
| 313.15 | 35000.00 | 824.56 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 810.8 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [317.91; 433.96] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45991e+01 | |||
| Coefficient B | -3.07041e+03 | |||
| Coefficient C | -1.03369e+02 | |||
| Temperature range, min. | 317.91 | |||
| Temperature range, max. | 433.96 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
| Pvap | 1.33 | kPa | 317.91 | Calculated Property |
| Pvap | 3.00 | kPa | 330.80 | Calculated Property |
| Pvap | 6.19 | kPa | 343.70 | Calculated Property |
| Pvap | 11.87 | kPa | 356.59 | Calculated Property |
| Pvap | 21.36 | kPa | 369.49 | Calculated Property |
| Pvap | 36.40 | kPa | 382.38 | Calculated Property |
| Pvap | 59.19 | kPa | 395.28 | Calculated Property |
| Pvap | 92.36 | kPa | 408.17 | Calculated Property |
| Pvap | 139.01 | kPa | 421.07 | Calculated Property |
| Pvap | 202.66 | kPa | 433.96 | Calculated Property |
| Pvap | [3.32e-07; 3863.36] | kPa | [195.56; 588.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.49346e+02 | |||
| Coefficient B | -1.21964e+04 | |||
| Coefficient C | -1.93819e+01 | |||
| Coefficient D | 9.39571e-06 | |||
| Temperature range, min. | 195.56 | |||
| Temperature range, max. | 588.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 300 400 500 | ||||
| Pvap | 3.32e-07 | kPa | 195.56 | Calculated Property |
| Pvap | 6.96e-04 | kPa | 239.16 | Calculated Property |
| Pvap | 0.09 | kPa | 282.77 | Calculated Property |
| Pvap | 2.21 | kPa | 326.37 | Calculated Property |
| Pvap | 21.18 | kPa | 369.98 | Calculated Property |
| Pvap | 108.89 | kPa | 413.58 | Calculated Property |
| Pvap | 371.28 | kPa | 457.19 | Calculated Property |
| Pvap | 959.68 | kPa | 500.79 | Calculated Property |
| Pvap | 2053.63 | kPa | 544.40 | Calculated Property |
| Pvap | 3863.36 | kPa | 588.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Pentanol.
Mixtures
- 2-Butanone + Benzene, 1,3-dichloro- + 1-Pentanol
- Di-n-propyl ether + 1-Pentanol
- 1-Propanol + 1-Pentanol
- 1-Propanol + Di-n-propyl ether + 1-Pentanol
- Benzene, chloro- + 1-Pentanol
- 1-Pentanol + Acetylacetone
- 1-Pentanol + Diethylene glycol hexyl ether
- 1-Pentanol + 2-Heptanone
- 1-Pentanol + Simvastatin
- Cholesterol + 1-Pentanol
- Cholesterol + 1-Pentanol + Cyclohexane
- Diethyl malonate + 1-Pentanol
- 1-Pentanol + Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)-
- Pentane, 2,2,4-trimethyl- + 1-Pentanol
- Isopropyl Alcohol + 1-Pentanol
- 1-Butanol + 1-Pentanol
- Isopropyl Alcohol + 1-Butanol + 1-Pentanol
- 1-Propanol, 2-methyl- + 1-Pentanol + Water
- Formic acid + 1-Pentanol + Water
- Lactic acid + 1-Pentanol + Water
Find more mixtures with 1-Pentanol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Determination of excess molar enthalpies of the ternary system methyl tert-butyl ether + 1-pentanol + nonane at 298.15K Analysis and comparison with predicted values of the UNIFAC model and some empirical methods
- Measurement of infinite dilution activity coefficients of 1-alkanols (C1 C5) in water as a function of temperature (273 373 K)
- The co-solubility of 2-ethylhexanoic acid and some liquid alcohols in supercritical carbon dioxide
- Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
- Vapor liquid equilibria in the ternary system dipropyl ether + 1-propanol + 1-pentanol and the binary systems dipropyl ether + 1-pentanol, 1-propanol + 1-pentanol at 101.3 kPa
- Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
- Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
- Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
- Determination and correlation of molar excess enthalpies of binary systems 2,4-pentanedione + (1-butanol, + 2-methyl-1-propanol, + 1-pentanol, + 1-heptane, + ethyl acetate, and + water)
- Salting effect on the liquid liquid equilibria for the ternary system water +N-methyl-2-pyrrolidone + 1-pentanol
- Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
- Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
- Liquid density of 1-pentanol at pressures up to 140MPa and from 293.15 to 403.15K
- Solubility and limiting activity coefficient of simvastatin in different organic solvents
- Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
- Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
- Liquid-liquid equilibrium of (water + 1-propanol + 1-pentanol) system at 298.15 and 323.15 K
- Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
- Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
- The influence of cation, anion and temperature on the liquid-liquid equilibrium of some pentanols-water system
- Experimental measurement and thermodynamic modeling of liquid-liquid equilibrium for 1-pentanol + water + NaNO3 at 298.15 and 308.15 K
- Study of the influence of the structure of the alcohol on vapor pressures and osmotic coefficients of binary mixtures alcohol + 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at T = 323.15 K
- Thermodynamic characterization of second generation biofuels: Vapour-liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol and cyclohexane or toluene
- Solubility of triclosan and iodopropynyl butylcarbamate in pure alkanols at several temperatures
- Solubility of lansoprazole in different solvents
- Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
- Vapour liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol with 2,2,4-trimethylpentane or n-heptane
- Investigation on vapor liquid equilibrium for 2-propanol + 1-butanol + 1-pentanol at 101.3 kPa
- Liquid-liquid equilibrium data for ternary aqueous mixtures containing 1-pentanol and 2-methyl-1-propanol at (298.15, 323.15, and 348.15) K
- Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
- Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
- Vapor-liquid equilibria of binary systems composed of polyoxyethylene 4-octylphenyl ether and alcohols: Experimental measurements and correlation
- Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
- Measurement and correlation of solid-liquid equilibrium for abietic acid + alcohol systems at atmospheric pressure
- Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
- Solubility of N-Ethylcarbazole in different organic solvent at 279.15 - 319.15 K
- Liquid-liquid phase equilibria of ionic liquid solutions in the critical region: 1-Methyl-3-octylimidazolium tetrafluoroborate with1-pentanol or 1-hexanol
- Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
- Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
- Vapour-liquid equilibria of the ternary mixture (1-pentanol + 2,2,4-trimethylpentane + heptane) and the binary mixture (2,2,4-trimethylpentane + heptane) at T = 313.15 K for the characterization of second generation biofuels.
- Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
- An improved static-analytic apparatus for vapor-liquid equilibrium (PTxy) measurement using modified in-situ samplers
- Characterizing second generation biofuels: Excess enthalpies and vapour-liquid equilibria of the binary mixtures containing 1-pentanol or 2-pentanol and n-hexane
- Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
- Determination and correlation of solubility of N-methyl-3,4,5- trinitropyrazole (MTNP) in ten pure solvents from 283.15 K to 323.15 K
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Vapor-liquid equilibria and excess enthalpies of the binary systems 1- pentanol or 2-pentanol and 1-hexene or 1,2,4-trimethylbenzene for the development of biofuels
- Solubility, liquid-liquid equilibrium and critical states for quaternary system acetic acid - n-amyl alcohol - n-amyl acetate - water at 303.15 K and atmospheric pressure
- Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
- Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
- Measurement of the thermal conductivity of biofuel mixtures: Methyl caprate components of biodiesel and alcohols
- Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
- Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-pentanol and 3-pentanol
- Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
- Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
- Excess molar enthalpies of ethylformate and (1-propanol, 2-propanol, 1-butanol, 2-butanol, and 1-pentanol) at T = (298.15 and 308.15) K and p = (5 and 10) MPa
- Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
- Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
- Excess molar enthalpies of dimethyl carbonate and (butanol isomers and 1-pentanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
- Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
- Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
- Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
- Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
- Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
- Compressed liquid densities and excess molar volumes for (CO2 + 1-pentanol) binary system at temperatures from 313 to 363 K and pressures up to 25 MPa
- Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
- Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
- Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of dipropylene glycol dimethyl ether with 1-alkanols at 298.15 K
- Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
- Mixing thermodynamic properties of 1-butyl-4-methylpyridinium tetrafluoroborate [b4mpy][BF4] with water and with an alkan-1ol (methanol to pentanol)
- Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
- Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
- Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
- Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure
- Measurement and modeling of high-pressure (vapour + liquid) equilibria of (CO2 + alcohol) binary systems
- Vapour pressures, osmotic and activity coefficients for binary mixtures containing (1-ethylpyridinium ethylsulfate + several alcohols) at T = 323.15 K
- Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
- Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
- Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
- Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
- Cloud point measurements of 1-butyl-2,3-dimethylimidazolium tetrafluoroborate with alcohols
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- Measurement and modeling of osmotic coefficients of binary mixtures (alcohol + 1,3-dimethylpyridinium methylsulfate) at T = 323.15 K
- Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
- (Liquid + liquid) equilibria in {water + acrylic acid + (1-butanol, or 2-butanol, or 1-pentanol)} systems at T = 293.2 K, T = 303.2 K, and T = 313.2 K and atmospheric pressure
- Application of the extended real associated solution (ERAS) theory to excess molar enthalpies of benzaldehyde + 1-alkanols (C1 to C5) at T = 298.15 K
- PrhoT measurements and derived properties of liquid 1-alkanols
- Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
- Determination and correlation of the solubility for diosgenin in alcohols solvents
- Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
- Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
- Solubility of salicylic acid in pure alcohols at different temperatures
- Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
- On the solubility of nicotinic acid and isonicotinic acid in water and organic solvents
- Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Vapour pressures and osmotic coefficients of binary mixtures containing alcohol and pyrrolidinium-based ionic liquids
- FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
- Study of molecular interactions in the mixtures of some primary alcohols with equimolar mixture of 1-propanol and alkylbenzoates at T = 303.15 K
- Osmotic coefficients and apparent molar volumes of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid in alcohols
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- Tie line data for the (water + butyric acid + n-butyl alcohol or amyl alcohol) at T = (298.2, 308.2, and 318.2) K and (water + butyric acid + isoamyl alcohol) at T = 298.2 K
- Osmotic coefficients of alcoholic mixtures containing BMpyrDCA: Experimental determination and correlation
- Contribution to study of the thermodynamics properties of mixtures containing 2-methoxy-2-methylpropane, alkanol, alkane
- Effect of the temperature on the physical properties of the pure ionic liquid 1-ethyl-3-methylimidazolium methylsulfate and characterization of its binary mixtures with alcohols
- Solubility of climbazole in various alcohols at different temperatures
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
- Thermodynamic models for determination of the solubility of (-)-shikimic acid in different pure solvents and in (H2O + ethanol) binary solvent mixtures
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- (Vapor + liquid) equilibria of alcohol + 1-methyl-1-propylpiperidinium triflate ionic liquid: VPO measurements and modeling
- Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
- Experimental measurement and correlation of the solubility of aloe-emodin in seven pure solvents
- The study of molecular interactions in 1-ethyl-3-methylimidazolium trifluoromethanesulfonate + 1-pentanol from density, speed of sound and refractive index measurements
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Thermodynamic and spectroscopic properties of binary mixtures of n-butylammonium butanoate ionic liquid with alcohols at T = (293.15-313.15) K
- Determination and modelling of troxerutin solubility in eleven mono-solvents and (1,4-dioxane + 2-propanol) binary solvents at temperatures from 288.15 K to 323.15 K
- Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
- Solubility and thermodynamic properties of vanillyl alcohol in some pure solvents
- Comparative study of physical properties of binary mixtures of halogen free ionic liquids with alcohols
- Solubility of commercial octacosanol in organic solvents and their correlation by thermodynamic models at different temperatures
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Mutual diffusion coefficients of n-butanol + n-heptane and n-pentanol + n-heptane from 288.15 K to 318.15 K
- Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
- Excess molar enthalpies of R-fenchone + butan-1-ol or + pentan-1-ol. Modeling with COSMO-RS and UNIFAC
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
- Thermodynamic properties of paracetamol impurities 4-nitrophenol and 4'-chloroacetanilide and the impact of such impurities on the crystallisation of paracetamol from solution
- Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
- Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
- Experimental studies on the thermal conductivity of methyl laurate component of biodiesel with three alcohols
- Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
- Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
- Excess molar enthalpies of methylformate + (1-propanol, 2-propanol, 1-butanol, 2-butanol and 1-pentanol) at T = 298.15 K, p = (5.0, 10.0)MPa, and methylformate + 1-propanol at T = 333.15 K, p = 10.0MPa
- ERAS modeling of the excess molar enthalpies of binary liquid mixtures of 1-pentanol and 1-hexanol with acetonitrile at atmospheric pressure and 288, 298, 313 and 323K
- Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
- Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
- Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
- Measurement and Correlation for Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
- THERMODYNAMICS OF MIXTURES CONTAINING AMINES. XIV. CpEm OF BENZYLAMINE WITH HEPTANE AT 293.15 K OR WITH METHANOL, 1-PROPANOL OR 1-PENTANOL AT (293.15-308.15) K
- Measurement and correlation of solubility of carbendazim in lower alcohols
- Capillary Viscometer and Vibrating Tube Densimeter for Simultaneous Measurements up to 70 MPa and 423 K
- Viscous Calibration Liquids for Self-diffusion Measurements
- Thermodynamics of 1,3-dimethylurea in eight alcohols
- Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
- Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
- Measurement and Correlation of Solubility on Reactive Crystallization of Methyl D-(-)-4-Hydroxy-phenylglycinate
- Physical Properties of the Pure Deep Eutectic Solvent, [ChCl]:[Lev] (1:2) DES, and Its Binary Mixtures with Alcohols
- Solubility Correlation and Thermodynamic Analysis of Sorafenib Free Base and Sorafenib Tosylate in Monosolvents and Binary Solvent Mixtures
- Solubility and Thermodynamic Behavior of Veramoss in Different Pure Solvents and {Ethanol + Water} Mixtures from T = 283.15 to 333.15 K
- Measurement and Correlation of Solubility of Loratadine in Different Pure Solvents and Binary Mixtures
- Measurement and Correlation of Solubility of Amorphous Cefmetazole Sodium in Pure Solvents and Binary Solvent Mixtures
- Determination and Correlation of Solubility of Phenylbutazone in Monosolvents and Binary Solvent Mixtures
- Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
- Pressurized-Synthetic Methodology for Solubility Determination at Elevated Temperatures with Application to Paracetamol in Pure Solvents
- Studying the Liquid-Liquid Equilibrium of Systems Water +2-Hydroxyethylammonium Propanoate or 2-Hydroxyethylammonium Butanoate or 2-Hydroxyethylammonium Pentanoate +1-Pentanol at 293.15, 313.15, and 333.15 K: Experimental Determination and Thermodynamic Modeling
- Liquid-Liquid Equilibria Determination and Prediction for Ternary Systems of Water + 1,6-Hexanediamine + (1-Butanol or 1-Pentanol) at 298.2, 308.2, and 318.2 K
- Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
- Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
- Isothermal Vapor-Liquid Equilibrium Measurements of Butan-2-one + 2-Methyl-propan-1-ol/Pentan-1-ol
- Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
- Synergistic Extraction of Hydroquinone from Aqueous Solution with Solvent Mixture of 2-Pentanone and n-Pentanol: Liquid-Liquid Equilibria and Data Correlation
- Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
- Viscosity and Density of n-Alcohols at Temperatures between (298.15 and 323.15) K and Pressures up to 30 MPa
- Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
- Effect of the Alkyl Chain on the Physical Properties of Imidazolium-Based Ionic Liquids with 1-Propanol, 1-Butanol, and 1-Pentanol Binary Mixtures
- Density and Derived Properties of Binary Mixtures Containing {2-(Dimethylamino)ethyl Methacrylate + Alcohols} at Temperatures from T = (293.15 to 313.15) K and Pressures of up to 35 MPa
- Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
- Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
- Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
- Measurement and Correlation of Solubility of Hydrochlorothiazide in Monosolvents and Binary Solvent Mixtures from 283.15 to 323.15 K
- Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
- Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
- Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
- Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
- Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
- Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
- Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
- Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 3. Liquid-Liquid Equilibria of Binary Mixtures of 1-Ethyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide with Propan-1-ol, Butan-1-ol, and Pentan-1-ol
- Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Acetonitrile Mixtures at 298.2 K
- Density, Refractive Index, and Speed of Sound at 298.15 K and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + 1-Pentanol and Ethanol + 2-Methyl-1-propanol
- Measurement and Correlation of Mutual Solubilities for High Viscosity Binary Systems: Aniline + Methylcyclohexane, Phenol + Heptane, Phenol + Octane, and Glycerol + 1-Pentanol
- Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
- Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
- Vapor-Liquid Equilibria of the Binary System 1-Pentanol + Anisole and the Quaternary System Benzene+Cyclohexane+1-Pentanol+Anisole at 101.32 kPa
- Thermodynamic Properties of Mixtures Containing Ionic Liquids.4.LLE of Binary Mixtures of [C2MIM][NTf2] with Propan-1-ol, Butan-1-ol, and Pentan-1-ol and [C4MIM][NTf2] with Cyclohexanol and 1,2-Hexanediol Including Studies of the Influence of Small Amounts of Water
- Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
- Experimental and Predicted Excess Molar Enthalpies of the Ternary System tert-Butyl Methyl Ether + 1-Pentanol + Decane at 298.15 K
- Quaternary Liquid-Liquid Equilibrium of Water + Acetic Acid + Propionic Acid + Solvent (Amyl Alcohol, Cyclohexyl Acetate, or Toluene) Systems
- Solubility and Density of 2,6-Dimethylnaphthalene in C1-C7 1-Alkanols
- Heat Capacities and Derived Thermodynamic Functions of 1-Propanol between 10 K and 350 K and of 1-Pentanol between 85 K and 370 K
- Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
- Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Excess Molar Enthalpies of Methyl Acetate and (1-Propanol, 2-Propanol, 1-Butanol, 2-Butanol, and 1-Pentanol) at T = (298.15 and 308.15) K and P = (5.0 and 10.0) MPa
- Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Nonane
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Solubility of Organic Systems Containing 1,4-Dioxan-2-one
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
- Density and Surface Tension of Binary Mixtures of Acetonitrile + 1-Alkanol at 293.15 K
- Liquid-Liquid Equilibrium Diagrams of Ethanol + Water + (Ethyl Acetate or 1-Pentanol) at Several Temperatures
- Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
- Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
- Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
- Excess Molar Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1- or 2-Pentanol at (283.15, 298.15, and 313.15) K
- Isobaric Vapor-Liquid Equilibria of the Ternary System Dibutyl Ether + 1-Pentanol + Nonane
- Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures Containing 2-Methyl-1-propanol + 2-Methyl-1-butanol, 2-Methyl-1-propanol + 3-Methyl-1-butanol, and 2-Methyl-1-propanol + 1-Pentanol
- Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Fluid-Phase Behavior of {1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide, [C6mim][NTf2], + C2-C8 n-Alcohol} Mixtures: Liquid-Liquid Equilibrium and Excess Volumes
- Solubility of Xylitol in Ethanol, Acetone, N,N-Dimethylformamide, 1-Butanol, 1-Pentanol, Toluene, 2-Propanol, and Water
- Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
- Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K
- Solubilities of Ibuprofen in Different Pure Solvents
- Thermodynamic Parameters of Anionic Surfactant-Additive Systems at the Cloud Point
- Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
- Excess Molar Enthalpies of 2-Methyl-2-butanol (1) + 1-Alkanols (C1-C5) (2) at 298.15 K
- Liquid-Liquid Equilibria of Water + Pentan-1-ol + 2,6,6-Trimethylbicyclo[3.1.1]hep-2-ene or 6,6-Dimethyl-2-methylenebicyclo[3.1.1]heptane at (293.15, 303.15, 313.15, and 323.15) K
- Solubilities of Phloretin in 12 Solvents at Different Temperatures
- Measurement and Study on the Liquid Liquid Equilibrium of Ionic Liquids with Aliphatic Alcohols
- Isobaric Vapor-Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane
- Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
- Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
- Measurement and Correlation of Solubility of Clopidogrel Hydrogen Sulfate (Metastable Form) in Lower Alcohols
- Isobaric Vapor Liquid Equilibrium of 3-Methyl-1-butanol + Ethyl Lactate and 1-Pentanol + Ethyl Lactate at (13.0 and 101.3) kPa
- Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
- Extraction of n-Alcohols from n-Heptane Using Ionic Liquids.
- Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
- Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
- Measurements and Modeling of High-Pressure Phase Behavior of the Carbon Dioxide + Pentan-1-ol Binary System
- Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
- Vapor Liquid Equilibrium Data for Binary Systems of 1H-Pyrrole with Butan-1-ol, Propan-1-ol, or Pentan-1-ol
- Isobaric Vapor Liquid Equilibria of Tertiary Amine and n-Alkane/Alkanol Binary Mixtures: Experimental Measurements and Modeling with GC-PPC-SAFT
- Densities and Viscosities for Binary Liquid Mixtures of Ethanol + 1-Propanol, 1-Butanol, and 1-Pentanol from (293.15 to 328.15) K at 0.1 MPa
- Liquid Liquid Phase Equilibria of the Binary Ionic Liquid Systems [Cn MIM][NTf2] + n-Butanol, + n-Pentanol, + H2O Using UV Spectroscopic and Densimetric Analytical Methods
- Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
- Liquid Liquid Phase Behavior of Solutions of 1,3-Dimethylimidazolium- and 1-Methyl-3-propylimidazolium Bis((trifluoromethyl)sulphonyl)amide (C1,3mimNTf2) in n-Alkyl Alcohols
- Liquid Liquid Equilibrium for the Ternary System 2-Methyl-2-propanol + 1-Pentanol + Water at T = (303.15, 328.15, and 353.15) K
- Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
- Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
- Excess Molar Enthalpies of Binary Mixtures Containing 1-Methyl-3-octyl-imidazolium Tetrafluoroborate and Alcohols at T = 298.15 K
- Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + n-Pentanol), (Propyl Acetate + 1-Methyl-1-butanol), and (Propyl Acetate + 3-Methyl-1-butanol) at 101.3 kPa
- Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of Cefixime Trihydrate in Seven Pure Solvents
- Determination and Correlation of Solubilities of Lauric Acid in Eight Alcohols
- Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
- Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
- Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
- Experimental Liquid-Liquid Equilibria of 1-Alkyl-3-methylimidazolium Hexafluorophosphate with 1-Alcohols
- Solubility of Phenacetinum in Methanol, Ethanol, 1-Propanol, 1-Butanol, 1-Pentanol, Tetrahydrofuran, Ethyl Acetate, and Benzene between 282.65 K and 333.70 K
- Isobaric Vapor-Liquid Equilibrium for the Binary Systems 1-Pentanol + Cyclohexane and 1-Pentanol + n-Hexane at Low Alcohol Compositions
- Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
- Isobaric Vapor Liquid Equilibria of the Ternary System 1-Pentanol + Nonane Anisole
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
- Solubility of Losartan Potassium in Different Pure Solvents from (293.15 to 343.15) K
- Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
- Determination and Correlation of Excess Molar Enthalpies of Eight Binary Systems Containing Acetophenone at Different Temperatures
- Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
- Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
- Solubility of Alcohols and Aromatic Compounds in Imidazolium-Based Ionic Liquids
- Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
- Solubility of D(-)-p-Hydroxyphenylglycine Dane Salt in Eight Alcohols between (293 and 343) K
- Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
- Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
- Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
- Excess Molar Enthalpies of Five Binary Systems Containing Ethyl Acetoacetate at Different Temperatures
- Thermodynamic Properties of Micellization of Sodium Dodecylbenzene Sulfonate in the Aqueous-Rich Region of 1-Pentanol and 1-Hexanol
- Study of the Effects of Temperature and Pressure on the Thermodynamic and Acoustic Properties of Pentan-1-ol, 2-Methyl-2-butanol, and Cyclopentanol in the Pressure Range from (0.1 to 100) MPa and Temperature from (293 to 318) K
- Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Anisole
- Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 2-Ethyl-1-hexanol with 1-Pentanol, 1-Heptanol, or 1-Nonanol at the Temperature 298.15 K
- Densities and Viscosities of exo-Tetrahydrodicyclopentadiene + n-Butanol and exo-Tetrahydrodicyclopentadiene + n-Pentanol at Temperatures of (293.15 to 313.15) K
- Measurement and Correlation of Solubilities of Decanedioic Acid in C4-C6 Alcohol Solvents
- Studies of Monohydric Alcohols in Aqueous Sodium Dodecyl Sulfate Solutions at T = (298.15 and 308.15) K
- Isobaric Vapor-Liquid Equilibria of Heptane + 1-Butanol and Heptane + 1-Pentanol Systems at (53.3 and 91.3) kPa
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubilities of (?,Z)-2-Amino-?-(methoxyimino)-4-thiazole-ethanethioic Acid S-2-Benzothiazolyl Ester in Pure Solvents and a Mixture of Acetonitrile and Dichloromethane
- Isobaric Vapor-Liquid Equilibrium for Binary Mixtures of 3-Methyl-1-butanol + 3-Methyl-1-butyl Ethanoate and 1-Pentanol + Pentyl Ethanoate at 101.3 kPa
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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