- 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.
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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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 240 250 260 270 280 290 300 450 500 550 600 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 5.00e-4 6.00e-4 7.00e-4 8.00e-4 9.00e-4 300 320 340 | ||||
| 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] |
|
|
|
T(K) Refractive Index 1.4 1.4 1.4 1.4 294 296 298 | ||||
| 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] |
|
|
T(K) Liquid Density (kg/m3) 830 840 850 860 870 880 300 320 | ||||
| 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] |
|
|
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.02 0.02 0.03 0.03 300 320 340 | ||||
| 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] |
|
|
P(kPa) Boiling point at given pressure (K) 360 370 380 390 400 410 420 430 50 100 150 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 200 400 600 | ||||
| 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
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