- InChI
- InChI=1S/C5H10O2/c1-2-3-4-5(6)7/h2-4H2,1H3,(H,6,7)
- InChI Key
- NQPDZGIKBAWPEJ-UHFFFAOYSA-N
- Formula
- C5H10O2
- SMILES
- CCCCC(=O)O
- Molecular Weight1
- 102.13
- CAS
- 109-52-4
- Other Names
-
- 1-Butanecarboxylic acid
- 1-Pentanoic acid
- Butanecarboxylic acid
- Kyselina valerova
- N-PENTANOIC ACID
- N-VALERIC ACID
- NA 1760
- NSC 406833
- Propylacetic acid
- VALERIANIC ACID
- Valeric acid
- Valeric acid, n-
- Valeric acid, normal
- n-C4H9COOH
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- 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).
- 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.
- 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).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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 |
|---|---|---|---|
| ΔcH°liquid | [-2850.10; -2833.40] | kJ/mol |
|
| ΔcH°liquid | -2837.80 ± 0.70 | kJ/mol | NIST |
| ΔcH°liquid | -2836.50 ± 0.67 | kJ/mol | NIST |
| ΔcH°liquid | -2850.10 ± 5.90 | kJ/mol | NIST |
| ΔcH°liquid | -2833.40 ± 1.30 | kJ/mol | NIST |
| ΔcH°solid | -2838.80 | kJ/mol | NIST |
| ΔfG° | -357.40 | kJ/mol | KDB |
| ΔfH°gas | [-500.90; -477.30] | kJ/mol |
|
| ΔfH°gas | -490.70 | kJ/mol | KDB |
| ΔfH°gas | -496.50 ± 4.10 | kJ/mol | NIST |
| ΔfH°gas | -497.80 ± 4.10 | kJ/mol | NIST |
| ΔfH°gas | -491.00 | kJ/mol | NIST |
| ΔfH°gas | -497.80 ± 4.10 | kJ/mol | NIST |
| ΔfH°gas | -484.20 ± 7.10 | kJ/mol | NIST |
| ΔfH°gas | -477.30 | kJ/mol | NIST |
| ΔfH°gas | -484.20 ± 7.10 | kJ/mol | NIST |
| ΔfH°gas | -500.90 ± 4.20 | kJ/mol | NIST |
| ΔfH°liquid | [-563.30; -546.60] | kJ/mol |
|
| ΔfH°liquid | -558.90 ± 0.70 | kJ/mol | NIST |
| ΔfH°liquid | -560.24 ± 0.67 | kJ/mol | NIST |
| ΔfH°liquid | -560.20 ± 0.70 | kJ/mol | NIST |
| ΔfH°liquid | -546.60 ± 5.90 | kJ/mol | NIST |
| ΔfH°liquid | -563.30 ± 1.30 | kJ/mol | NIST |
| ΔfusH° | 14.39 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 50.15 | kJ/mol | Joback Calculated Property |
| IE | 10.53 | eV | NIST |
| log10WS | -1.01 | Crippen Calculated Property | |
| logPoct/wat | 1.261 | Crippen Calculated Property | |
| McVol | 88.750 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [3564.40; 3630.00] | kPa |
|
| Pc | 3580.00 | kPa | KDB |
| Pc | 3630.00 ± 30.00 | kPa | NIST |
| Pc | 3628.00 ± 40.00 | kPa | NIST |
| Pc | 3600.00 ± 100.00 | kPa | NIST |
| Pc | 3564.40 ± 90.00 | kPa | NIST |
| ρc | 300.27 ± 6.13 | kg/m3 | NIST |
| Inp | [137.00; 938.00] |
|
|
| Inp | 883.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 933.30 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | Outlier 137.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 933.30 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | Outlier 137.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 880.00 | NIST | |
| I | [1685.00; 1780.00] |
|
|
| I | Outlier 1685.00 | NIST | |
| I | 1733.00 | NIST | |
| I | 1744.00 | NIST | |
| I | 1734.00 | NIST | |
| I | 1723.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1725.00 | NIST | |
| I | Outlier 1686.00 | NIST | |
| I | 1762.00 | NIST | |
| I | 1713.00 | NIST | |
| I | 1720.00 | NIST | |
| I | 1720.00 | NIST | |
| I | 1746.00 | NIST | |
| I | 1755.00 | NIST | |
| I | 1718.00 | NIST | |
| I | 1708.00 | NIST | |
| I | 1720.00 | NIST | |
| I | 1719.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1750.00 | NIST | |
| I | Outlier 1780.00 | NIST | |
| I | 1757.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1750.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1736.00 | NIST | |
| I | 1706.00 | NIST | |
| I | 1729.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1766.00 | NIST | |
| I | 1729.00 | NIST | |
| I | 1745.00 | NIST | |
| I | 1734.00 | NIST | |
| I | 1724.00 | NIST | |
| I | 1732.00 | NIST | |
| I | 1732.00 | NIST | |
| I | 1734.00 | NIST | |
| I | 1719.00 | NIST | |
| I | 1732.00 | NIST | |
| I | 1753.00 | NIST | |
| I | 1708.00 | NIST | |
| I | 1707.00 | NIST | |
| I | 1743.00 | NIST | |
| I | 1723.00 | NIST | |
| I | 1752.00 | NIST | |
| I | 1716.00 | NIST | |
| I | 1733.00 | NIST | |
| I | 1720.00 | NIST | |
| I | 1755.00 | NIST | |
| I | 1770.00 | NIST | |
| I | 1751.00 | NIST | |
| I | 1718.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1727.00 | NIST | |
| I | 1727.00 | NIST | |
| I | 1753.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1751.00 | NIST | |
| I | 1766.00 | NIST | |
| I | 1743.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1741.00 | NIST | |
| I | 1741.00 | NIST | |
| I | 1726.00 | NIST | |
| I | 1726.00 | NIST | |
| I | 1712.00 | NIST | |
| I | 1700.00 | NIST | |
| I | 1698.00 | NIST | |
| I | 1738.00 | NIST | |
| I | 1740.00 | NIST | |
| I | 1723.00 | NIST | |
| I | 1725.00 | NIST | |
| I | 1743.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1733.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1740.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1736.00 | NIST | |
| I | Outlier 1689.00 | NIST | |
| I | 1698.00 | NIST | |
| I | Outlier 1689.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1720.00 | NIST | |
| I | 1737.00 | NIST | |
| I | 1750.00 | NIST | |
| I | 1768.00 | NIST | |
| I | 1734.00 | NIST | |
| I | 1734.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1733.00 | NIST | |
| I | 1738.00 | NIST | |
| I | 1745.00 | NIST | |
| I | 1740.00 | NIST | |
| I | 1721.00 | NIST | |
| I | 1721.00 | NIST | |
| I | 1720.00 | NIST | |
| I | 1720.00 | NIST | |
| I | Outlier 1772.00 | NIST | |
| I | 1746.00 | NIST | |
| I | 1731.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1720.00 | NIST | |
| I | 1753.00 | NIST | |
| I | 1721.00 | NIST | |
| I | 1732.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1706.00 | NIST | |
| I | 1716.00 | NIST | |
| I | 1751.00 | NIST | |
| I | 1753.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1712.00 | NIST | |
| I | 1723.00 | NIST | |
| I | 1733.00 | NIST | |
| I | Outlier 1689.00 | NIST | |
| I | 1737.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1721.00 | NIST | |
| I | 1746.00 | NIST | |
| I | Outlier 1685.00 | NIST | |
| I | 1725.00 | NIST | |
| I | 1720.00 | NIST | |
| I | Outlier 1780.00 | NIST | |
| I | 1736.00 | NIST | |
| I | 1724.00 | NIST | |
| I | 1732.00 | NIST | |
| S°gas | 439.82 ± 0.63 | J/mol×K | NIST |
| S°liquid | 259.83 | J/mol×K | NIST |
| Tboil | [459.15; 459.30] | K |
|
| Tboil | 459.30 | K | KDB |
| Tboil | 459.15 | K | Ternary... |
| Tc | [637.20; 652.02] | K |
|
| Tc | 643.00 | K | KDB |
| Tc | 637.20 ± 1.00 | K | NIST |
| Tc | 637.20 ± 1.00 | K | NIST |
| Tc | 639.90 ± 0.60 | K | NIST |
| Tc | 643.00 ± 2.00 | K | NIST |
| Tc | 652.01 ± 2.50 | K | NIST |
| Tc | 652.02 ± 6.00 | K | NIST |
| Tfus | [238.40; 239.70] | K |
|
| Tfus | 239.00 | K | KDB |
| Tfus | 239.15 ± 2.00 | K | NIST |
| Tfus | 239.70 ± 0.10 | K | NIST |
| Tfus | 238.40 ± 0.60 | K | NIST |
| Tfus | 238.70 ± 1.50 | K | NIST |
| Tfus | 238.65 ± 0.40 | K | NIST |
| Ttriple | 239.49 ± 0.06 | K | NIST |
| Vc | 0.340 | m3/kmol | KDB |
| Zc | 0.2276740 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [183.75; 226.08] | J/mol×K | [459.85; 632.49] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 230 500 550 600 | ||||
| Cp,gas | 183.75 | J/mol×K | 459.85 | Joback Calculated Property |
| Cp,gas | 191.56 | J/mol×K | 488.62 | Joback Calculated Property |
| Cp,gas | 199.06 | J/mol×K | 517.40 | Joback Calculated Property |
| Cp,gas | 206.25 | J/mol×K | 546.17 | Joback Calculated Property |
| Cp,gas | 213.15 | J/mol×K | 574.94 | Joback Calculated Property |
| Cp,gas | 219.76 | J/mol×K | 603.72 | Joback Calculated Property |
| Cp,gas | 226.08 | J/mol×K | 632.49 | Joback Calculated Property |
| Cp,liquid | [197.00; 210.33] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 197.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 210.33 | J/mol×K | 298.15 | NIST |
| η | [0.0002424; 0.0272118] | Pa×s | [256.86; 459.85] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-3 0.01 0.02 0.02 0.03 300 350 400 450 | ||||
| η | 0.0272118 | Pa×s | 256.86 | Joback Calculated Property |
| η | 0.0078379 | Pa×s | 290.69 | Joback Calculated Property |
| η | 0.0029265 | Pa×s | 324.52 | Joback Calculated Property |
| η | 0.0013161 | Pa×s | 358.36 | Joback Calculated Property |
| η | 0.0006794 | Pa×s | 392.19 | Joback Calculated Property |
| η | 0.0003895 | Pa×s | 426.02 | Joback Calculated Property |
| η | 0.0002424 | Pa×s | 459.85 | Joback Calculated Property |
| ΔfusH | [14.16; 14.16] | kJ/mol | [239.49; 239.50] |
|
| ΔfusH | 14.16 | kJ/mol | 239.49 | NIST |
| ΔfusH | 14.16 | kJ/mol | 239.50 | NIST |
| ΔfusH | 14.16 | kJ/mol | 239.50 | NIST |
| ΔvapH | [57.90; 58.00] | kJ/mol | [419.00; 449.00] |
|
| ΔvapH | 57.90 | kJ/mol | 419.00 | NIST |
| ΔvapH | 58.00 | kJ/mol | 449.00 | NIST |
| Pvap | [14.56; 85.03] | kPa | [403.15; 451.92] |
|
|
T(K) Vapor pressure (kPa) 20 40 60 80 420 440 | ||||
| Pvap | 14.56 | kPa | 403.15 | Subatmo... |
| Pvap | 19.59 | kPa | 410.71 | Subatmo... |
| Pvap | 24.63 | kPa | 417.07 | Subatmo... |
| Pvap | 29.65 | kPa | 422.19 | Subatmo... |
| Pvap | 39.72 | kPa | 430.08 | Subatmo... |
| Pvap | 49.78 | kPa | 436.48 | Subatmo... |
| Pvap | 59.85 | kPa | 441.89 | Subatmo... |
| Pvap | 69.92 | kPa | 446.45 | Subatmo... |
| Pvap | 74.96 | kPa | 448.48 | Subatmo... |
| Pvap | 79.99 | kPa | 450.35 | Subatmo... |
| Pvap | 85.03 | kPa | 451.92 | Subatmo... |
| n0 | [1.40470; 1.40870] | [293.15; 303.15] |
|
|
| n0 | 1.40870 | 293.15 | Vapour ... | |
| n0 | 1.40820 | 293.15 | Vapour-... | |
| n0 | 1.40470 | 303.15 | Liquid ... | |
| n0 | 1.40470 | 303.15 | Phase e... | |
| ρl | [812.10; 939.70] | kg/m3 | [293.00; 428.20] |
|
|
T(K) Liquid Density (kg/m3) 800 820 840 860 880 900 920 940 300 350 400 | ||||
| ρl | 939.00 | kg/m3 | 293.00 | KDB |
| ρl | 939.41 | kg/m3 | 293.15 | Influen... |
| ρl | 939.70 | kg/m3 | 293.40 | Density... |
| ρl | 935.04 | kg/m3 | 298.00 | Optimiz... |
| ρl | 934.85 | kg/m3 | 298.15 | Influen... |
| ρl | 934.75 | kg/m3 | 298.15 | Liquid-... |
| ρl | 930.29 | kg/m3 | 303.15 | Influen... |
| ρl | 925.73 | kg/m3 | 308.15 | Influen... |
| ρl | 922.30 | kg/m3 | 312.10 | Density... |
| ρl | 921.16 | kg/m3 | 313.15 | Influen... |
| ρl | 904.10 | kg/m3 | 332.10 | Density... |
| ρl | 885.40 | kg/m3 | 352.20 | Density... |
| ρl | 870.60 | kg/m3 | 368.10 | Density... |
| ρl | 851.00 | kg/m3 | 388.40 | Density... |
| ρl | 831.90 | kg/m3 | 408.30 | Density... |
| ρl | 812.10 | kg/m3 | 428.20 | Density... |
| ΔfusS | 59.13 | J/mol×K | 239.49 | NIST |
| γ | [0.03; 0.03] | N/m | [293.15; 308.15] |
|
| γ | 0.03 | N/m | 293.15 | Apparen... |
| γ | 0.03 | N/m | 298.15 | Apparen... |
| γ | 0.03 | N/m | 303.15 | Apparen... |
| γ | 0.03 | N/m | 308.15 | Apparen... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 935.1 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [349.70; 485.04] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.55964e+01 | |||
| Coefficient B | -4.24155e+03 | |||
| Coefficient C | -7.26340e+01 | |||
| Temperature range, min. | 349.70 | |||
| Temperature range, max. | 485.04 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 349.70 | Calculated Property |
| Pvap | 2.93 | kPa | 364.74 | Calculated Property |
| Pvap | 5.97 | kPa | 379.78 | Calculated Property |
| Pvap | 11.37 | kPa | 394.81 | Calculated Property |
| Pvap | 20.46 | kPa | 409.85 | Calculated Property |
| Pvap | 35.00 | kPa | 424.89 | Calculated Property |
| Pvap | 57.30 | kPa | 439.93 | Calculated Property |
| Pvap | 90.24 | kPa | 454.96 | Calculated Property |
| Pvap | 137.32 | kPa | 470.00 | Calculated Property |
| Pvap | 202.65 | kPa | 485.04 | Calculated Property |
| Pvap | [5.85e-05; 3576.21] | kPa | [239.15; 651.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.38077e+01 | |||
| Coefficient B | -9.69682e+03 | |||
| Coefficient C | -7.85615e+00 | |||
| Coefficient D | 3.91183e-07 | |||
| Temperature range, min. | 239.15 | |||
| Temperature range, max. | 651.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 600 | ||||
| Pvap | 5.85e-05 | kPa | 239.15 | Calculated Property |
| Pvap | 0.01 | kPa | 284.91 | Calculated Property |
| Pvap | 0.35 | kPa | 330.67 | Calculated Property |
| Pvap | 4.53 | kPa | 376.43 | Calculated Property |
| Pvap | 30.44 | kPa | 422.19 | Calculated Property |
| Pvap | 130.21 | kPa | 467.96 | Calculated Property |
| Pvap | 403.27 | kPa | 513.72 | Calculated Property |
| Pvap | 984.69 | kPa | 559.48 | Calculated Property |
| Pvap | 2010.16 | kPa | 605.24 | Calculated Property |
| Pvap | 3576.21 | kPa | 651.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentanoic acid.
Mixtures
- Pentanoic acid + Propanoic acid
- Pentanoic acid + Propanoic acid, 2-methyl-
- 1-Undecanol + Pentanoic acid + Water
- Hexanoic acid + Pentanoic acid
- Acetonitrile + Dodecane + Pentanoic acid
- Pentane + Pentanoic acid + Thiophene, tetrahydro-, 1,1-dioxide
- Benzene, chloro- + Pentanoic acid + Water
- Pentanoic acid + Benzene, 1,1'-[oxybis(methylene)]bis- + Water
- Benzenemethanol, «alpha»-methyl- + Pentanoic acid + Water
- Heptane + Pentanoic acid + Thiophene, tetrahydro-, 1,1-dioxide
- Butanoic acid + Pentanoic acid
- Heptanoic acid + Pentanoic acid
- 1-Pentanol + Pentanoic acid
- 1-Hexanol + Pentanoic acid
- 1-Octanol + Pentanoic acid
- 1-Decanol + Pentanoic acid
- Pentanoic acid + Water
- Formic acid + Pentanoic acid
- 2-Pyrrolidinone, 1-methyl- + Pentanoic acid + Water
- Acetic acid + Pentanoic acid
Find more mixtures with Pentanoic acid.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Liquid-liquid equilibria for ternary systems of (water + carboxylic acid + 1-octanol) at 293.15 K: modeling phase equilibria using a solvatochromic approach
- Vapour liquid equilibrium of carboxylic acid systems: Propionic acid + valeric acid and isobutyric acid + valeric acid
- Liquid liquid equilibria for the system (water + carboxylic acid + chloroform): Thermodynamic modeling
- Phase equilibria of (water + carboxylic acid + diethyl maleate) ternary liquid systems at 298.15 K
- Ternary liquid-liquid phase equilibria of (water-carboxylic acid-1-undecanol) systems at 298.15 K
- Vapour-liquid equilibrium of propionic acid + caproic acid, isobutyric acid + caproic acid, valeric acid + caproic acid and caproic acid + enanthoic acid binary mixtures
- Liquid liquid equilibria measurements of ternary systems (acetonitrile + a carboxylic acid + dodecane) at 303.15 K
- Phase equilibria measurements of ternary mixtures (sulfolane + a carboxylic acid + pentane) at 303.15 K
- Optimization of liquid-liquid equilibria of the type 2 ternary systems (water + valeric acid + aromatic solvent): Modeling through SERLAS
- Understanding ion-ion and ion-solvent interactions in aqueous solutions of NMP based protic ionic liquids through partial molar properties and DFT calculations
- Differential scanning calorimetry determination of Solid-Liquid equilibria phase diagrams for binary monocarboxylic acids solutions
- (Liquid + liquid) equilibria measurements for ternary systems (sulfolane + a carboxylic acid + n-heptane) at T = 303.15 K and at 0.1 MPa
- Liquid-liquid equilibrium of ternary systems comprising ethyl valerate(1), water(2), ethanol(3) and valeric acid(4)
- Phase equilibrium measurements and thermodynamic modelling for the systems involving valeric acid, ethanol, ethyl valerate and water plus CO2
- Liquid-liquid equilibria for the aqueous mixture of C5 carboxylic acids and heavier than water solvents at T = 298.2 K
- Liquid-liquid equilibria and density data for pseudoternary systems of refined soybean oil + (hexanal, or heptanal, or butyric acid, or valeric acid, or caproic acid, or caprylic acid) + dimethyl sulfoxide at 298.15 K
- Effect of temperature on the dilution enthalpies of carboxylic acids in aqueous solutions
- Influence of alkyl group and temperature on thermophysical properties of carboxylic acid and their binary mixtures
- Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
- Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
- Subatmospheric Vapor Pressure Curves for Propionic Acid, Butyric Acid, Isobutyric Acid, Valeric Acid, Isovaleric Acid, Hexanoic Acid, and Heptanoic Acid
- Apparent Molar Volume and Surface Tension of Dilute Aqueous Solutions of Carboxylic Acids
- Liquid Liquid Equilibria for the Ternary Systems Water + n-Pentanoic Acid with n-Heptane or Dichloromethane at 298.2 K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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