- InChI
- InChI=1S/C7H14O2/c1-6(2)4-5-9-7(3)8/h6H,4-5H2,1-3H3
- InChI Key
- MLFHJEHSLIIPHL-UHFFFAOYSA-N
- Formula
- C7H14O2
- SMILES
- CC(=O)OCCC(C)C
- Molecular Weight1
- 130.18
- CAS
- 123-92-2
- Other Names
-
- 1-Butanol, 3-methyl-, 1-acetate
- 2-Methylbutyl ethanoate
- 3-METHYLBUTYL ACETATE
- 3-METHYLBUTYL ESTER ACETIC ACID
- 3-Methyl butyl ester acetic acid
- 3-Methyl-1-butanol acetate
- 3-Methyl-1-butanyl acetate
- 3-Methyl-1-butyl acetate
- 3-Methylbutyl ester of acetic acid
- 3-Methylbutyl ethanoate
- 3-methyl-1-butyl acetate (isoamyl acetate)
- 3-methyl-but-1-yl acetate
- Acetic acid, 3-methylbutyl ester
- Acetic acid, isoamyl ester
- Acetic acid, isopentyl ester
- Amyl acetate ester
- Amyl acetate, common
- Banana oil
- CH3C(O)O(CH2)2CH(CH3)2
- ISOAMYL ACETATE
- Isoamyl ethanoate
- Isoamylester kyseliny octove
- Isopentyl acetate
- Isopentyl alcohol, acetate
- Isopentyl alcohol, acetate pear oil
- Isopentyl ester acetic acid
- Isopentyl ethanoate
- Jargonelle pear essence
- NSC 9260
- Pear oil
- i-Amyl acetate
- «beta»-Methyl butyl acetate
- «beta»-Methyl butyl acetate
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- 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.
- 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).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| μ | 1.80 | debye | KDB |
| ΔfG° | -228.30 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -437.89 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 13.15 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 46.40 ± 0.20 | kJ/mol | NIST |
| log10WS | [-1.92; -1.92] |
|
|
| log10WS | -1.92 | Aq. Sol... | |
| log10WS | -1.92 | Estimat... | |
| logPoct/wat | 1.596 | Crippen Calculated Property | |
| McVol | 116.930 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 2760.00 ± 20.00 | kPa | NIST |
| Inp | [836.00; 893.00] |
|
|
| Inp | 861.32 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 857.80 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 859.70 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | Outlier 836.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 855.50 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 874.60 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 875.70 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 882.60 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | Outlier 893.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | Outlier 843.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | Outlier 843.00 | NIST | |
| Inp | Outlier 843.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 853.00 | NIST | |
| I | [1096.00; 1168.00] |
|
|
| I | 1131.00 | NIST | |
| I | Outlier 1096.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1102.00 | NIST | |
| I | 1105.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1121.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1111.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1131.00 | NIST | |
| I | 1101.00 | NIST | |
| I | 1115.00 | NIST | |
| I | 1121.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1143.00 | NIST | |
| I | 1123.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1134.00 | NIST | |
| I | 1114.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1121.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1115.00 | NIST | |
| I | 1107.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1119.00 | NIST | |
| I | 1123.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1123.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1115.00 | NIST | |
| I | 1115.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1137.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1113.00 | NIST | |
| I | 1113.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1115.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1114.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1114.00 | NIST | |
| I | 1119.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1140.00 | NIST | |
| I | 1147.00 | NIST | |
| I | 1111.00 | NIST | |
| I | 1102.00 | NIST | |
| I | 1137.00 | NIST | |
| I | 1102.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1105.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1103.00 | NIST | |
| I | 1147.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1133.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1134.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1112.00 | NIST | |
| I | 1108.00 | NIST | |
| I | 1143.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1101.00 | NIST | |
| I | 1101.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1140.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1114.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1124.00 | NIST | |
| I | Outlier 1165.00 | NIST | |
| I | Outlier 1166.00 | NIST | |
| I | Outlier 1167.00 | NIST | |
| I | 1113.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1123.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1122.00 | NIST | |
| I | Outlier 1098.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1136.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1136.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1111.00 | NIST | |
| I | 1131.00 | NIST | |
| I | 1115.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1143.00 | NIST | |
| I | 1121.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1136.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1114.00 | NIST | |
| I | 1114.00 | NIST | |
| I | Outlier 1168.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1115.00 | NIST | |
| I | 1110.00 | NIST | |
| Tboil | [415.15; 415.70] | K |
|
| Tboil | 415.70 | K | KDB |
| Tboil | 415.24 | K | Effect ... |
| Tboil | 415.15 | K | Isobari... |
| Tc | [586.10; 599.33] | K |
|
| Tc | 599.00 | K | KDB |
| Tc | 586.10 ± 0.60 | K | NIST |
| Tc | 599.33 ± 6.00 | K | NIST |
| Tfus | [189.53; 194.60] | K |
|
| Tfus | 194.60 | K | KDB |
| Tfus | 189.53 | K | Aq. Sol... |
| Vc | 0.446 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [238.73; 301.45] | J/mol×K | [435.41; 615.76] |
|
| Cp,gas | 238.73 | J/mol×K | 435.41 | Joback Calculated Property |
| Cp,gas | 250.17 | J/mol×K | 465.47 | Joback Calculated Property |
| Cp,gas | 261.22 | J/mol×K | 495.53 | Joback Calculated Property |
| Cp,gas | 271.87 | J/mol×K | 525.58 | Joback Calculated Property |
| Cp,gas | 282.12 | J/mol×K | 555.64 | Joback Calculated Property |
| Cp,gas | 291.98 | J/mol×K | 585.70 | Joback Calculated Property |
| Cp,gas | 301.45 | J/mol×K | 615.76 | Joback Calculated Property |
| η | [0.0004810; 0.0009400] | Pa×s | [288.15; 343.15] |
|
| η | 0.0009400 | Pa×s | 288.15 | Densiti... |
| η | 0.0008880 | Pa×s | 293.15 | Density... |
| η | 0.0008270 | Pa×s | 298.15 | Density... |
| η | 0.0008040 | Pa×s | 298.15 | Densiti... |
| η | 0.0007810 | Pa×s | 298.15 | Densiti... |
| η | 0.0007410 | Pa×s | 303.15 | Thermop... |
| η | 0.0007730 | Pa×s | 303.15 | Density... |
| η | 0.0007240 | Pa×s | 308.15 | Density... |
| η | 0.0007470 | Pa×s | 308.15 | Densiti... |
| η | 0.0007040 | Pa×s | 308.15 | Densiti... |
| η | 0.0006780 | Pa×s | 313.15 | Density... |
| η | 0.0006490 | Pa×s | 313.15 | Thermop... |
| η | 0.0006270 | Pa×s | 318.15 | Densiti... |
| η | 0.0006380 | Pa×s | 318.15 | Density... |
| η | 0.0006010 | Pa×s | 323.15 | Density... |
| η | 0.0005670 | Pa×s | 328.15 | Density... |
| η | 0.0005360 | Pa×s | 333.15 | Density... |
| η | 0.0005070 | Pa×s | 338.15 | Density... |
| η | 0.0004810 | Pa×s | 343.15 | Density... |
| ΔvapH | [44.30; 46.80] | kJ/mol | [291.50; 366.00] |
|
| ΔvapH | 46.80 ± 0.20 | kJ/mol | 291.50 | NIST |
| ΔvapH | 46.40 | kJ/mol | 332.50 | NIST |
| ΔvapH | 45.10 | kJ/mol | 340.50 | NIST |
| ΔvapH | 44.30 | kJ/mol | 366.00 | NIST |
| Pvap | [50.00; 100.00] | kPa | [391.07; 413.46] |
|
| Pvap | 50.00 | kPa | 391.07 | Isobari... |
| Pvap | 100.00 | kPa | 413.46 | Isobari... |
| n0 | [1.39750; 1.39893] | [293.20; 298.15] |
|
|
| n0 | 1.39760 | 293.20 | Experim... | |
| n0 | 1.39750 | 298.15 | Applica... | |
| n0 | 1.39770 | 298.15 | Isobari... | |
| n0 | 1.39842 | 298.15 | Vapor-L... | |
| n0 | 1.39893 | 298.15 | Isobari... | |
| ρl | [833.30; 876.00] | kg/m3 | [288.00; 333.15] |
|
| ρl | 876.00 | kg/m3 | 288.00 | KDB |
| ρl | 872.90 | kg/m3 | 293.15 | Experim... |
| ρl | 872.49 | kg/m3 | 293.20 | Liquid-... |
| ρl | 867.36 | kg/m3 | 298.15 | Volumet... |
| ρl | 868.00 | kg/m3 | 298.15 | Experim... |
| ρl | 867.91 | kg/m3 | 298.15 | Refract... |
| ρl | 866.70 | kg/m3 | 298.20 | Experim... |
| ρl | 853.30 | kg/m3 | 313.15 | Experim... |
| ρl | 852.64 | kg/m3 | 313.20 | Liquid-... |
| ρl | 833.30 | kg/m3 | 333.15 | Experim... |
| γ | [0.02; 0.03] | N/m | [288.15; 358.15] |
|
| γ | 0.03 | N/m | 288.15 | Densiti... |
| γ | 0.02 | N/m | 298.15 | Densiti... |
| γ | 0.02 | N/m | 308.15 | Densiti... |
| γ | 0.02 | N/m | 318.15 | Densiti... |
| γ | 0.02 | N/m | 328.15 | Densiti... |
| γ | 0.02 | N/m | 338.15 | Densiti... |
| γ | 0.02 | N/m | 348.15 | Densiti... |
| γ | 0.02 | N/m | 358.15 | Densiti... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [365.29; 431.61] | K | [20.00; 160.01] |
|
| Tboil | 365.29 | K | 20.00 | Vapor L... |
| Tboil | 376.06 | K | 29.98 | Vapor L... |
| Tboil | 384.31 | K | 40.01 | Vapor L... |
| Tboil | 391.07 | K | 49.99 | Vapor L... |
| Tboil | 396.76 | K | 60.00 | Vapor L... |
| Tboil | 401.72 | K | 70.00 | Vapor L... |
| Tboil | 406.18 | K | 80.01 | Vapor L... |
| Tboil | 410.24 | K | 90.00 | Vapor L... |
| Tboil | 413.90 | K | 100.01 | Vapor L... |
| Tboil | 417.15 | K | 110.00 | Vapor L... |
| Tboil | 420.43 | K | 119.99 | Vapor L... |
| Tboil | 423.46 | K | 130.00 | Vapor L... |
| Tboil | 426.33 | K | 139.99 | Vapor L... |
| Tboil | 429.05 | K | 149.99 | Vapor L... |
| Tboil | 431.61 | K | 160.01 | Vapor L... |
| Tboilr | 415.20 | K | 101.00 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 867.3 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [311.22; 438.68] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53486e+01 | |||
| Coefficient B | -3.83541e+03 | |||
| Coefficient C | -5.65620e+01 | |||
| Temperature range, min. | 311.22 | |||
| Temperature range, max. | 438.68 | |||
| Pvap | 1.33 | kPa | 311.22 | Calculated Property |
| Pvap | 2.95 | kPa | 325.38 | Calculated Property |
| Pvap | 6.02 | kPa | 339.54 | Calculated Property |
| Pvap | 11.49 | kPa | 353.71 | Calculated Property |
| Pvap | 20.66 | kPa | 367.87 | Calculated Property |
| Pvap | 35.32 | kPa | 382.03 | Calculated Property |
| Pvap | 57.73 | kPa | 396.19 | Calculated Property |
| Pvap | 90.72 | kPa | 410.36 | Calculated Property |
| Pvap | 137.69 | kPa | 424.52 | Calculated Property |
| Pvap | 202.63 | kPa | 438.68 | Calculated Property |
| Pvap | [2.06e-05; 2676.19] | kPa | [194.65; 599.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.60348e+01 | |||
| Coefficient B | -7.92872e+03 | |||
| Coefficient C | -8.76739e+00 | |||
| Coefficient D | 3.24333e-06 | |||
| Temperature range, min. | 194.65 | |||
| Temperature range, max. | 599.00 | |||
| Pvap | 2.06e-05 | kPa | 194.65 | Calculated Property |
| Pvap | 7.38e-03 | kPa | 239.58 | Calculated Property |
| Pvap | 0.33 | kPa | 284.51 | Calculated Property |
| Pvap | 4.44 | kPa | 329.43 | Calculated Property |
| Pvap | 28.83 | kPa | 374.36 | Calculated Property |
| Pvap | 115.89 | kPa | 419.29 | Calculated Property |
| Pvap | 336.66 | kPa | 464.22 | Calculated Property |
| Pvap | 779.09 | kPa | 509.14 | Calculated Property |
| Pvap | 1532.08 | kPa | 554.07 | Calculated Property |
| Pvap | 2676.19 | kPa | 599.00 | Calculated Property |
Similar Compounds
![Propan-1,3-dioic acid, di[3-methylbutyl] ester.](data:image/png;base64,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)
Find more compounds similar to 1-Butanol, 3-methyl-, acetate.
Mixtures
- 1-Butanol, 3-methyl-, acetate + 2-Propenoic acid, butyl ester
- 2-Propenoic acid, ethyl ester + 1-Butanol, 3-methyl-, acetate
- 1-Butanol, 3-methyl-, acetate + Methyl methacrylate
- Styrene + 1-Butanol, 3-methyl-, acetate
- 1-Butanol, 3-methyl-, acetate + Acetic acid + Water
- 1-Butanol, 3-methyl-, acetate + Water
- 1-Butanol, 3-methyl-, acetate + Methyl Alcohol
- Ethanol + 1-Butanol, 3-methyl-, acetate
- 1-Propanol + 1-Butanol, 3-methyl-, acetate
- Isopropyl Alcohol + 1-Butanol, 3-methyl-, acetate
- 1-Butanol, 3-methyl-, acetate + 1-Butanol
- Methylene chloride + 1-Butanol, 3-methyl-, acetate
- 1,3-Dioxolane + Methylene chloride + 1-Butanol, 3-methyl-, acetate
- 1-Butanol, 3-methyl- + 1-Butanol, 3-methyl-, acetate
- Isobutyl acetate + 1-Butanol, 3-methyl-, acetate
- 1-Butanol, 3-methyl-, acetate + Dimethyl Sulfoxide
- 1-Butanol, 3-methyl- + 1-Butanol, 3-methyl-, acetate + Dimethyl Sulfoxide
- Carbonic acid, dimethyl ester + 1-Butanol, 3-methyl-, acetate
- 1-Butanol, 3-methyl-, acetate + Acetic acid, methyl ester
- 1-Butanol, 3-methyl-, acetate + Ethyl Acetate
Find more mixtures with 1-Butanol, 3-methyl-, acetate.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Volumetric Properties of 3-Methylbutyl Ethanoate with Ethyl Acrylate, Butyl Acrylate, Methyl Methacrylate, and Styrene at 25 C
- Experimental study of phase equilibria in aqueous mixtures of phosphoric acid with isoamyl acetate and methyl isoamyl ketone at T = (298.2, 308.2, and 318.2) K
- Phase behavior of binary mixture for the isoalkyl acetate in supercritical carbon dioxide
- Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
- Application of the ERAS model to volumetric properties of binary mixtures of banana oil with primary and secondary alcohols (C1- C4) at different temperatures
- Studies on liquid liquid interactions of some ternary mixtures by density, viscosity, ultrasonic speed and refractive index measurements
- Effect of Pressure on the Azeotrope of the Mixture Isoamyl Acetate Isoamyl Alcohol at 50.00, 101.32, 250.00, and 350.00 kPa
- Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
- Isobaric Vapor Liquid Equilibrium for Binary and Ternary Systems of Isoamyl Alcohol + Isoamyl Acetate + Dimethyl Sulfoxide at 101.33 kPa
- Vapor-Liquid Equilibrium Data for Binary Mixtures of Dimethyl Carbonate with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, Isopropyl Acetate, n-Butyl Acetate, and Isoamyl Acetate at 93.13 kPa
- Isobaric Vapor-Liquid Equilibrium Measurements for Separation of Azeotrope (Methanol + Methyl Acetate)
- Isobaric Vapor Liquid Equilibria for Binary Mixtures of Isoamyl Acetate + Ethyl Acetate at 50 and 100 kPa
- Experimental High-Temperature, High-Pressure Density Measurement and Perturbed-Chain Statistical Associating Fluid Theory Modeling of Dimethyl Sulfoxide, Isoamyl Acetate, and Benzyl Alcohol
- Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Isopropyl Acetate, sec-Butyl Acetate, or Isoamyl Acetate at 101.3 kPa
- Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
- Liquid-Liquid Equilibria for the Ternary Systems of (Water + Tetrahydrofuran + Polar Solvent) at 298.15 K
- Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
- Densities, Viscosities, Refractive Indices, and Surface Tensions for 12 Flavor Esters from T ) 288.15 K to T ) 358.15 K
- Densities and Viscosities of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at T = (288.15, 298.15, 308.15, and 318.15) K
- Refractive Indices and Surface Tensions of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at (288.15, 298.15, 308.15, and 318.15) K
- Vapor-Liquid Equilibrium for Carbon Dioxide + Isopropyl, Isobutyl, and Isoamyl Acetates
- Experimental and Correlational Study of Phase Equilibria in Aqueous Solutions of Formic and Butyric Acids with Isoamyl Acetate and Methyl Isoamyl Ketone at T = 298.15 K
- Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
- 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
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.