- InChI
- InChI=1S/C6H12O2/c1-5(2)4-8-6(3)7/h5H,4H2,1-3H3
- InChI Key
- GJRQTCIYDGXPES-UHFFFAOYSA-N
- Formula
- C6H12O2
- SMILES
- CC(=O)OCC(C)C
- Molecular Weight1
- 116.16
- CAS
- 110-19-0
- Other Names
-
- 2-METHYL-1-PROPYL ACETATE
- 2-METHYLPROPYL ESTER ACETIC ACID
- 2-Methyl-1-propanol, acetate
- 2-Methylpropyl acetate
- 2-Methylpropyl ethanoate
- Acetate d'isobutyle
- Acetic acid, 2-methylpropyl ester
- Acetic acid, isobutyl ester
- ISOBUTYL ETHANOATE
- Isobutyl acetate fcc
- Isobutylester kyseliny octove
- NSC 8035
- UN 1213
- ethanoic acid, isobutyl ester
- i-Butyl acetate
- «beta»-Methylpropyl ethanoate
- «beta»-Methylpropyl ethanoate
- ω : Acentric Factor.
- 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,cc : Flash Point (Closed Cup Method) (K).
- 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).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- 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.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4550 | KDB | |
| Tig | 695.93 | K | KDB |
| ΔcH°liquid | -3534.00 | kJ/mol | NIST |
| μ | 1.90 | debye | KDB |
| LFL | 2.40 | % in Air | KDB |
| UFL | 10.50 | % in Air | KDB |
| Tflash,cc | 302.59 | K | KDB |
| Tflash,oc | 289.82 | K | KDB |
| ΔfG° | -236.72 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -495.50 | kJ/mol | KDB |
| ΔfusH° | 10.56 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 35.90 ± 0.04 | kJ/mol | NIST |
| IE | 9.97 | eV | NIST |
| log10WS | [-1.21; -1.21] |
|
|
| log10WS | -1.21 | Aq. Sol... | |
| log10WS | -1.21 | Estimat... | |
| logPoct/wat | 1.205 | Crippen Calculated Property | |
| McVol | 102.840 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3010.00; 3180.00] | kPa |
|
| Pc | 3160.00 | kPa | KDB |
| Pc | 3010.00 ± 20.00 | kPa | NIST |
| Pc | 3180.00 ± 60.79 | kPa | NIST |
| ρc | 281.10 ± 8.13 | kg/m3 | NIST |
| Inp | [730.00; 788.00] |
|
|
| Inp | 757.70 | NIST | |
| Inp | 758.98 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 757.20 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | Outlier 783.00 | NIST | |
| Inp | Outlier 788.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 767.20 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 779.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 745.30 | NIST | |
| Inp | 748.40 | NIST | |
| Inp | 749.70 | NIST | |
| Inp | 752.10 | NIST | |
| Inp | 749.80 | NIST | |
| Inp | 748.70 | NIST | |
| Inp | 754.45 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | Outlier 786.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 776.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 766.00 | NIST | |
| Inp | Outlier 734.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 779.50 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 745.00 | NIST | |
| Inp | 743.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 764.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | Outlier 730.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 762.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 754.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 758.00 | NIST | |
| Inp | 749.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | 748.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 771.00 | NIST | |
| Inp | Outlier 730.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 753.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 750.00 | NIST | |
| Inp | 746.00 | NIST | |
| I | [976.00; 1047.00] |
|
|
| I | 1025.00 | NIST | |
| I | 1011.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1013.00 | NIST | |
| I | 1033.00 | NIST | |
| I | 1018.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1029.00 | NIST | |
| I | 1005.00 | NIST | |
| I | 1017.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1031.00 | NIST | |
| I | 1029.00 | NIST | |
| I | 1022.00 | NIST | |
| I | 1002.00 | NIST | |
| I | 1007.00 | NIST | |
| I | 1027.00 | NIST | |
| I | 989.00 | NIST | |
| I | 986.00 | NIST | |
| I | 1014.00 | NIST | |
| I | 993.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1013.00 | NIST | |
| I | 1019.00 | NIST | |
| I | 1011.00 | NIST | |
| I | 1009.00 | NIST | |
| I | 1009.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1002.00 | NIST | |
| I | 1018.00 | NIST | |
| I | 1016.00 | NIST | |
| I | 1034.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1009.00 | NIST | |
| I | 1009.00 | NIST | |
| I | 1035.00 | NIST | |
| I | 985.00 | NIST | |
| I | 1015.00 | NIST | |
| I | 1004.00 | NIST | |
| I | 1032.00 | NIST | |
| I | 1008.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1009.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 998.00 | NIST | |
| I | 988.00 | NIST | |
| I | 988.00 | NIST | |
| I | 992.00 | NIST | |
| I | 1005.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1005.00 | NIST | |
| I | 1014.00 | NIST | |
| I | 1007.00 | NIST | |
| I | 1005.00 | NIST | |
| I | 1005.00 | NIST | |
| I | 1009.00 | NIST | |
| I | 1009.00 | NIST | |
| I | 1017.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1011.00 | NIST | |
| I | 1014.00 | NIST | |
| I | 1014.00 | NIST | |
| I | Outlier 1047.00 | NIST | |
| I | 1019.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1012.00 | NIST | |
| I | Outlier 976.00 | NIST | |
| I | 1024.00 | NIST | |
| I | 985.00 | NIST | |
| I | 1017.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 987.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1023.00 | NIST | |
| I | 1023.00 | NIST | |
| I | Outlier 984.00 | NIST | |
| I | 1025.00 | NIST | |
| Tboil | [389.44; 389.90] | K |
|
| Tboil | 389.70 | K | KDB |
| Tboil | 389.44 | K | Isobari... |
| Tboil | 389.55 | K | Vapour-... |
| Tboil | 389.90 | K | Isobari... |
| Tboil | 389.75 | K | Measure... |
| Tboil | 389.55 | K | Isobari... |
| Tc | [560.80; 569.00] | K |
|
| Tc | 561.00 | K | KDB |
| Tc | 560.80 ± 0.60 | K | NIST |
| Tc | 561.50 ± 2.00 | K | NIST |
| Tc | 569.00 ± 5.00 | K | NIST |
| Tfus | [174.25; 240.15] | K |
|
| Tfus | 174.30 | K | KDB |
| Tfus | 174.25 | K | Aq. Sol... |
| Tfus | 176.05 | K | NIST |
| Tfus | 176.10 ± 0.60 | K | NIST |
| Tfus | 240.15 ± 0.50 | K | NIST |
| Vc | 0.414 | m3/kmol | KDB |
| Zc | 0.2804710 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [199.90; 255.87] | J/mol×K | [412.53; 594.22] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 200 210 220 230 240 250 260 450 500 550 | ||||
| Cp,gas | 199.90 | J/mol×K | 412.53 | Joback Calculated Property |
| Cp,gas | 210.06 | J/mol×K | 442.81 | Joback Calculated Property |
| Cp,gas | 219.89 | J/mol×K | 473.09 | Joback Calculated Property |
| Cp,gas | 229.39 | J/mol×K | 503.38 | Joback Calculated Property |
| Cp,gas | 238.55 | J/mol×K | 533.66 | Joback Calculated Property |
| Cp,gas | 247.38 | J/mol×K | 563.94 | Joback Calculated Property |
| Cp,gas | 255.87 | J/mol×K | 594.22 | Joback Calculated Property |
| Cp,liquid | 240.20 | J/mol×K | 290.00 | NIST |
| η | [0.0002624; 0.0046134] | Pa×s | [214.54; 412.53] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 250 300 350 400 | ||||
| η | 0.0046134 | Pa×s | 214.54 | Joback Calculated Property |
| η | 0.0020807 | Pa×s | 247.54 | Joback Calculated Property |
| η | 0.0011317 | Pa×s | 280.54 | Joback Calculated Property |
| η | 0.0006998 | Pa×s | 313.53 | Joback Calculated Property |
| η | 0.0004742 | Pa×s | 346.53 | Joback Calculated Property |
| η | 0.0003438 | Pa×s | 379.53 | Joback Calculated Property |
| η | 0.0002624 | Pa×s | 412.53 | Joback Calculated Property |
| ΔvapH | [39.20; 39.90] | kJ/mol | [321.50; 359.00] |
|
| ΔvapH | 39.80 | kJ/mol | 321.50 | NIST |
| ΔvapH | 39.90 | kJ/mol | 349.50 | NIST |
| ΔvapH | 39.20 | kJ/mol | 359.00 | NIST |
| Pvap | 101.30 | kPa | 389.55 | Vapour-... |
| n0 | [1.38760; 1.39050] | [293.15; 298.20] |
|
|
|
T(K) Refractive Index 1.39 1.39 1.39 1.39 1.39 1.39 1.39 294 296 298 | ||||
| n0 | 1.39050 | 293.15 | Isobari... | |
| n0 | 1.39020 | 293.15 | Measure... | |
| n0 | 1.38760 | 298.15 | Isobari... | |
| n0 | 1.38760 | 298.15 | Vapor l... | |
| n0 | 1.38760 | 298.15 | Liquid ... | |
| n0 | 1.38760 | 298.15 | Study o... | |
| n0 | 1.38760 | 298.15 | Phase e... | |
| n0 | 1.38760 | 298.15 | Phase e... | |
| n0 | 1.38780 | 298.20 | Tie-lin... | |
| ρl | [849.39; 875.00] | kg/m3 | [293.00; 313.20] |
|
| ρl | 875.00 | kg/m3 | 293.00 | KDB |
| ρl | 871.30 | kg/m3 | 293.20 | Liquid-... |
| ρl | 849.39 | kg/m3 | 313.20 | Liquid-... |
| γ | [0.02; 0.02] | N/m | [298.15; 313.15] |
|
| γ | 0.02 | N/m | 298.15 | Excess ... |
| γ | 0.02 | N/m | 308.15 | Excess ... |
| γ | 0.02 | N/m | 313.15 | Excess ... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [361.00; 403.64] | K | [39.99; 150.00] |
|
|
P(kPa) Boiling point at given pressure (K) 360 370 380 390 400 50 100 150 | ||||
| Tboil | 361.00 | K | 39.99 | Vapor L... |
| Tboil | 367.41 | K | 49.98 | Vapor L... |
| Tboil | 372.89 | K | 59.99 | Vapor L... |
| Tboil | 377.39 | K | 70.00 | Vapor L... |
| Tboil | 381.58 | K | 80.00 | Vapor L... |
| Tboil | 385.54 | K | 90.00 | Vapor L... |
| Tboil | 389.37 | K | 100.00 | Vapor L... |
| Tboil | 392.35 | K | 110.00 | Vapor L... |
| Tboil | 395.26 | K | 120.00 | Vapor L... |
| Tboil | 398.16 | K | 130.00 | Vapor L... |
| Tboil | 400.84 | K | 140.00 | Vapor L... |
| Tboil | 403.64 | K | 150.00 | Vapor L... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [287.55; 414.85] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.50519e+01 | |||
| Coefficient B | -3.64415e+03 | |||
| Coefficient C | -4.07290e+01 | |||
| Temperature range, min. | 287.55 | |||
| Temperature range, max. | 414.85 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 287.55 | Calculated Property |
| Pvap | 2.97 | kPa | 301.69 | Calculated Property |
| Pvap | 6.08 | kPa | 315.84 | Calculated Property |
| Pvap | 11.63 | kPa | 329.98 | Calculated Property |
| Pvap | 20.92 | kPa | 344.13 | Calculated Property |
| Pvap | 35.72 | kPa | 358.27 | Calculated Property |
| Pvap | 58.28 | kPa | 372.42 | Calculated Property |
| Pvap | 91.34 | kPa | 386.56 | Calculated Property |
| Pvap | 138.19 | kPa | 400.71 | Calculated Property |
| Pvap | 202.63 | kPa | 414.85 | Calculated Property |
| Pvap | [4.57e-06; 3169.48] | kPa | [174.30; 561.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.01223e+01 | |||
| Coefficient B | -7.87047e+03 | |||
| Coefficient C | -1.11424e+01 | |||
| Coefficient D | 7.93342e-06 | |||
| Temperature range, min. | 174.30 | |||
| Temperature range, max. | 561.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 300 400 500 | ||||
| Pvap | 4.57e-06 | kPa | 174.30 | Calculated Property |
| Pvap | 3.39e-03 | kPa | 217.27 | Calculated Property |
| Pvap | 0.21 | kPa | 260.23 | Calculated Property |
| Pvap | 3.39 | kPa | 303.20 | Calculated Property |
| Pvap | 24.24 | kPa | 346.17 | Calculated Property |
| Pvap | 104.11 | kPa | 389.13 | Calculated Property |
| Pvap | 320.39 | kPa | 432.10 | Calculated Property |
| Pvap | 788.29 | kPa | 475.07 | Calculated Property |
| Pvap | 1665.25 | kPa | 518.03 | Calculated Property |
| Pvap | 3169.48 | kPa | 561.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Isobutyl acetate.
Mixtures
- Isobutyl acetate + 1-Propanol, 2-methyl-
- Isobutyl acetate + Formamide, N,N-dimethyl-
- Isobutyl acetate + Formamide, N,N-dimethyl- + 1-Propanol, 2-methyl-
- Isobutyl acetate + 1-Hexanol
- Isobutyl acetate + 1-Propanol, 2-methyl- + 1-Hexanol
- Propanoic acid, butyl ester + Isobutyl acetate
- Propanoic acid, butyl ester + Isobutyl acetate + 1-Propanol, 2-methyl-
- Isobutyl acetate + 1-Propanol, 2-methyl- + Water
- Isobutyl acetate + Glycerin + 1-Propanol, 2-methyl-
- Isobutyl acetate + Acetic acid + Water
- Isobutyl acetate + Simvastatin
- Isobutyl acetate + Ethanol
- 1-Propanol + Isobutyl acetate
- Isobutyl acetate + Isopropyl Alcohol
- Isobutyl acetate + Heptane + Simvastatin
- Isobutyl acetate + Water
- Isobutyl acetate + Phenol + Water
- Isobutyl acetate + Carbonic acid, dimethyl ester
- Isobutyl acetate + Ethyl Acetate
- Isobutyl acetate + 1-Butanol, 3-methyl-, acetate
Find more mixtures with Isobutyl acetate.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa
- Phase equilibria in the systems isobutyl alcohol +N,N-dimethylformamide, isobutyl acetate +N,N-dimethylformamide and isobutyl alcohol + isobutyl acetate +N,N-dimethylformamide at 101.3 kPa
- Phase equilibria in the ternary system isobutyl alcohol + isobutyl acetate + 1-hexanol and the binary systems isobutyl alcohol + 1-hexanol, isobutyl acetate + 1-hexanol at 101.3 kPa
- Vapor liquid equilibria in the ternary system isobutyl alcohol + isobutyl acetate + butyl propionate and the binary systems isobutyl alcohol + butyl propionate, isobutyl acetate + butyl propionate at 101.3 kPa
- Liquid liquid equilibria of the systems isobutyl acetate + isobutyl alcohol +water and isobutyl acetate + isobutyl alcohol + glycerol at different temperatures
- Study of liquid liquid equilibrium of the systems isobutyl acetate + acetic acid +water and isobutyl alcohol + acetic acid +water at different temperatures
- Solubility and limiting activity coefficient of simvastatin in different organic solvents
- Investigation on isobaric vapor-liquid equilibrium for acetic acid + water + (n-propyl acetate or iso-butyl acetate)
- Solubility of lansoprazole in different solvents
- Isobaric VLE at 0.6 MPa for binary systems isobutyl acetate + ethanol, + 1-propanol or + 2-propanol
- Phase behavior of binary mixture for the isoalkyl acetate in supercritical carbon dioxide
- Solution thermodynamics of simvastatin in pure solvents and binary solvent mixtures
- Liquid-liquid equilibrium determination and thermodynamics modeling for extraction of isopropanol from its aqueous solution
- Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
- (Liquid + liquid) equilibria in ternary aqueous mixtures of phosphoric acid with organic solvents at T = 298.2 K
- Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
- Measurement and thermodynamic modelling of ternary liquid-liquid equilibrium for extraction of thioglycolic acid from aqueous solution with different solvents
- Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
- Binodal Curves and Tie Line Data of the Water - Propionic Acid - Isobutyl Acetate at T = (298.2, 308.2, 318.2, and 328.2) K
- Solubility of Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
- Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
- Isobaric Vapor Liquid Equilibrium for Binary Systems of Thioglycolic Acid with Water, Butyl Acetate, Butyl Formate, and Isobutyl Acetate at 101.3 kPa
- Measurement and Correlation of Phase Equilibria for Isobutyl Acetate + {Ethanol or Methanol} + Water at 303.15 and 323.15 K
- Isobaric Vapor Liquid Equilibrium for the Binary and Ternary System with Isobutyl Alcohol, Isobutyl Acetate and Dimethyl Sulfoxide at 101.3 kPa
- Separation of Protocatechuic Acid Using Di-(2-ethylhexyl)phosphoric Acid in Isobutyl Acetate, Toluene, and Petroleum Ether
- Measurement and Correlation of Isobaric Vapor-Liquid Equilibrium for Binary Systems of Allyl Alcohol with Isobutyl Acetate, Butyl Acetate, and Butyl Propionate at 101.3 kPa
- Isobaric Vapor-Liquid Equilibrium Measurements for Separation of Azeotrope (Methanol + Methyl Acetate)
- Liquid-Liquid Equilibrium of Isobutyl Acetate + Isobutyl Alcohol + Imidazolium-Based Ionic Liquids at 298.15 and 308.15 K
- Vapor-Liquid Equilibrium for Carbon Dioxide + Isopropyl, Isobutyl, and Isoamyl Acetates
- Solubilities of Benzene Carboxylic Acids in Isobutyl Acetate from (299.73 to 353.15) K
- Ternary Liquid Liquid Equilibria of Water + Prop-2-enoic Acid + Isobutyl Ethanoate at Different Temperatures
- Fast Determination of Binary Vapor Liquid Equilibrium of CO2-Based Mixtures at Elevated Pressures
- Liquid-Liquid Equilibria for the Ternary Systems Acetic Acid + Water + Butyl Acetate and Acetic Acid + Water + 2-Methyl Propyl Acetate at 304.15 K, 332.15 K, and 366.15 K
- Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with Isopropyl Acetate and Isobutyl Acetate at (298.15, 308.15, and 313.15) K
- Solubility of Lovastatin in Ethyl Acetate, Propyl Acetate, Isopropyl Acetate, Butyl Acetate, sec-Butyl Acetate, Isobutyl Acetate, tert-Butyl Acetate, and 2-Butanone, between (285 and 313) K
- Solubility of Naphthalene in Isobutyl Acetate, n-Butyric Acid, Ethyl Acetate, N-Methyl Pyrrolidone, N,N-Dimethylformamide, and Tetrahydrofuran
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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