- Name
- Butanoic acid, methyl ester
- InChI
- InChI=1S/C5H10O2/c1-3-4-5(6)7-2/h3-4H2,1-2H3
- InChI Key
- UUIQMZJEGPQKFD-UHFFFAOYSA-N
- Formula
- C5H10O2
- SMILES
- CCCC(=O)OC
- Mol. Weight (g/mol)
- 102.13
- CAS
- 623-42-7
- Name
- Water
- InChI
- InChI=1S/H2O/h1H2
- InChI Key
- XLYOFNOQVPJJNP-UHFFFAOYSA-N
- Formula
- H2O
- SMILES
- O
- Mol. Weight (g/mol)
- 18.02
- CAS
- 7732-18-5
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Datasets
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Butanoic acid, methyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 288.15 | 0.0006 | -0.0068 |
| 288.15 | 0.0009 | -0.0103 |
| 288.15 | 0.0009 | -0.0102 |
| 288.15 | 0.0013 | -0.0134 |
| 288.15 | 0.0013 | -0.0134 |
| 288.15 | 0.0016 | -0.0169 |
| 288.15 | 0.0016 | -0.0166 |
| 288.15 | 0.0019 | -0.0198 |
| 288.15 | 0.0019 | -0.0202 |
| 288.15 | 0.0006 | -0.0069 |
| 298.15 | 0.0006 | -0.0051 |
| 298.15 | 0.0009 | -0.0077 |
| 298.15 | 0.0013 | -0.0101 |
| 298.15 | 0.0016 | -0.0124 |
| 298.15 | 0.0016 | -0.0126 |
| 298.15 | 0.0019 | -0.0151 |
| 298.15 | 0.0019 | -0.0147 |
| 298.15 | 0.0022 | -0.0168 |
| 298.15 | 0.0022 | -0.0169 |
| 298.15 | 0.0006 | -0.0052 |
| 298.15 | 0.0009 | -0.0076 |
| 298.15 | 0.0013 | -0.0101 |
| 308.15 | 0.0006 | -0.0035 |
| 308.15 | 0.0006 | -0.0035 |
| 308.15 | 0.0009 | -0.0052 |
| 308.15 | 0.0009 | -0.0052 |
| 308.15 | 0.0013 | -0.0069 |
| 308.15 | 0.0013 | -0.0067 |
| 308.15 | 0.0016 | -0.0083 |
| 308.15 | 0.0016 | -0.0083 |
| 308.15 | 0.0019 | -0.0101 |
| 308.15 | 0.0019 | -0.0099 |
| 308.15 | 0.0022 | -0.0113 |
| 308.15 | 0.0022 | -0.0114 |
| 318.15 | 0.0009 | -0.0028 |
| 318.15 | 0.0009 | -0.0028 |
| 318.15 | 0.0013 | -0.0036 |
| 318.15 | 0.0013 | -0.0037 |
| 318.15 | 0.0016 | -0.0044 |
| 318.15 | 0.0016 | -0.0044 |
| 318.15 | 0.0019 | -0.0053 |
| 318.15 | 0.0019 | -0.0052 |
| 318.15 | 0.0022 | -0.0059 |
| 318.15 | 0.0022 | -0.0060 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Butanoic acid, methyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 288.15 | 0.0006 | -0.0068 |
| 288.15 | 0.0009 | -0.0103 |
| 288.15 | 0.0009 | -0.0102 |
| 288.15 | 0.0013 | -0.0134 |
| 288.15 | 0.0013 | -0.0134 |
| 288.15 | 0.0016 | -0.0169 |
| 288.15 | 0.0016 | -0.0166 |
| 288.15 | 0.0019 | -0.0198 |
| 288.15 | 0.0019 | -0.0202 |
| 288.15 | 0.0006 | -0.0069 |
| 298.15 | 0.0006 | -0.0051 |
| 298.15 | 0.0009 | -0.0077 |
| 298.15 | 0.0013 | -0.0101 |
| 298.15 | 0.0016 | -0.0124 |
| 298.15 | 0.0016 | -0.0126 |
| 298.15 | 0.0019 | -0.0151 |
| 298.15 | 0.0019 | -0.0147 |
| 298.15 | 0.0022 | -0.0168 |
| 298.15 | 0.0022 | -0.0169 |
| 298.15 | 0.0006 | -0.0052 |
| 298.15 | 0.0009 | -0.0076 |
| 298.15 | 0.0013 | -0.0101 |
| 308.15 | 0.0006 | -0.0035 |
| 308.15 | 0.0006 | -0.0035 |
| 308.15 | 0.0009 | -0.0052 |
| 308.15 | 0.0009 | -0.0052 |
| 308.15 | 0.0013 | -0.0069 |
| 308.15 | 0.0013 | -0.0067 |
| 308.15 | 0.0016 | -0.0083 |
| 308.15 | 0.0016 | -0.0083 |
| 308.15 | 0.0019 | -0.0101 |
| 308.15 | 0.0019 | -0.0099 |
| 308.15 | 0.0022 | -0.0113 |
| 308.15 | 0.0022 | -0.0114 |
| 318.15 | 0.0009 | -0.0028 |
| 318.15 | 0.0009 | -0.0028 |
| 318.15 | 0.0013 | -0.0036 |
| 318.15 | 0.0013 | -0.0037 |
| 318.15 | 0.0016 | -0.0044 |
| 318.15 | 0.0016 | -0.0044 |
| 318.15 | 0.0019 | -0.0053 |
| 318.15 | 0.0019 | -0.0052 |
| 318.15 | 0.0022 | -0.0059 |
| 318.15 | 0.0022 | -0.0060 |
Interfacial tension, N/m [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Interfacial tension, N/m - Liquid mixture 1 |
|---|---|
| 278.15 | 0.0106 |
| 288.15 | 0.0109 |
| 298.15 | 0.0111 |
| 308.15 | 0.0111 |
| 318.15 | 0.0110 |
| 328.15 | 0.0106 |
| 338.15 | 0.0100 |
| 348.15 | 0.0094 |
Interfacial tension, N/m [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Interfacial tension, N/m - Liquid mixture 1 |
|---|---|
| 278.15 | 0.0106 |
| 288.15 | 0.0109 |
| 298.15 | 0.0111 |
| 308.15 | 0.0111 |
| 318.15 | 0.0110 |
| 328.15 | 0.0106 |
| 338.15 | 0.0100 |
| 348.15 | 0.0094 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass density, kg/m3 - Liquid mixture 1 |
|---|---|
| 278.15 | 999.94 |
| 288.15 | 998.96 |
| 298.15 | 996.63 |
| 308.15 | 993.51 |
| 318.15 | 990.78 |
| 328.15 | 985.18 |
| 338.15 | 980.14 |
| 348.15 | 974.74 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mass density, kg/m3 - Liquid mixture 2 |
|---|---|
| 278.15 | 916.59 |
| 288.15 | 905.0 |
| 298.15 | 894.28 |
| 308.15 | 883.48 |
| 318.15 | 872.65 |
| 328.15 | 861.77 |
| 338.15 | 850.77 |
| 348.15 | 839.88 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Butanoic acid, methyl ester (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0006 | 999.058 |
| 288.15 | 0.0009 | 999.037 |
| 288.15 | 0.0009 | 999.038 |
| 288.15 | 0.0013 | 999.019 |
| 288.15 | 0.0013 | 999.019 |
| 288.15 | 0.0016 | 998.999 |
| 288.15 | 0.0016 | 999.001 |
| 288.15 | 0.0019 | 998.985 |
| 288.15 | 0.0019 | 998.981 |
| 288.15 | 0.0006 | 999.058 |
| 298.15 | 0.0006 | 996.968 |
| 298.15 | 0.0009 | 996.917 |
| 298.15 | 0.0013 | 996.885 |
| 298.15 | 0.0016 | 996.85 |
| 298.15 | 0.0016 | 996.838 |
| 298.15 | 0.0019 | 996.8 |
| 298.15 | 0.0019 | 996.81 |
| 298.15 | 0.0022 | 996.774 |
| 298.15 | 0.0022 | 996.773 |
| 298.15 | 0.0006 | 996.965 |
| 298.15 | 0.0009 | 996.921 |
| 298.15 | 0.0013 | 996.884 |
| 308.15 | 0.0006 | 993.913 |
| 308.15 | 0.0006 | 993.914 |
| 308.15 | 0.0009 | 993.855 |
| 308.15 | 0.0009 | 993.855 |
| 308.15 | 0.0013 | 993.793 |
| 308.15 | 0.0013 | 993.798 |
| 308.15 | 0.0016 | 993.741 |
| 308.15 | 0.0016 | 993.742 |
| 308.15 | 0.0019 | 993.673 |
| 308.15 | 0.0019 | 993.682 |
| 308.15 | 0.0022 | 993.626 |
| 308.15 | 0.0022 | 993.63 |
| 318.15 | 0.0009 | 989.988 |
| 318.15 | 0.0009 | 989.983 |
| 318.15 | 0.0013 | 989.911 |
| 318.15 | 0.0013 | 989.908 |
| 318.15 | 0.0016 | 989.837 |
| 318.15 | 0.0016 | 989.832 |
| 318.15 | 0.0019 | 989.762 |
| 318.15 | 0.0019 | 989.758 |
| 318.15 | 0.0022 | 989.694 |
| 318.15 | 0.0022 | 989.679 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass density, kg/m3 - Liquid mixture 1 |
|---|---|
| 278.15 | 999.94 |
| 288.15 | 998.96 |
| 298.15 | 996.63 |
| 308.15 | 993.51 |
| 318.15 | 990.78 |
| 328.15 | 985.18 |
| 338.15 | 980.14 |
| 348.15 | 974.74 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mass density, kg/m3 - Liquid mixture 2 |
|---|---|
| 278.15 | 916.59 |
| 288.15 | 905.0 |
| 298.15 | 894.28 |
| 308.15 | 883.48 |
| 318.15 | 872.65 |
| 328.15 | 861.77 |
| 338.15 | 850.77 |
| 348.15 | 839.88 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Butanoic acid, methyl ester (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0006 | 999.058 |
| 288.15 | 0.0009 | 999.037 |
| 288.15 | 0.0009 | 999.038 |
| 288.15 | 0.0013 | 999.019 |
| 288.15 | 0.0013 | 999.019 |
| 288.15 | 0.0016 | 998.999 |
| 288.15 | 0.0016 | 999.001 |
| 288.15 | 0.0019 | 998.985 |
| 288.15 | 0.0019 | 998.981 |
| 288.15 | 0.0006 | 999.058 |
| 298.15 | 0.0006 | 996.968 |
| 298.15 | 0.0009 | 996.917 |
| 298.15 | 0.0013 | 996.885 |
| 298.15 | 0.0016 | 996.85 |
| 298.15 | 0.0016 | 996.838 |
| 298.15 | 0.0019 | 996.8 |
| 298.15 | 0.0019 | 996.81 |
| 298.15 | 0.0022 | 996.774 |
| 298.15 | 0.0022 | 996.773 |
| 298.15 | 0.0006 | 996.965 |
| 298.15 | 0.0009 | 996.921 |
| 298.15 | 0.0013 | 996.884 |
| 308.15 | 0.0006 | 993.913 |
| 308.15 | 0.0006 | 993.914 |
| 308.15 | 0.0009 | 993.855 |
| 308.15 | 0.0009 | 993.855 |
| 308.15 | 0.0013 | 993.793 |
| 308.15 | 0.0013 | 993.798 |
| 308.15 | 0.0016 | 993.741 |
| 308.15 | 0.0016 | 993.742 |
| 308.15 | 0.0019 | 993.673 |
| 308.15 | 0.0019 | 993.682 |
| 308.15 | 0.0022 | 993.626 |
| 308.15 | 0.0022 | 993.63 |
| 318.15 | 0.0009 | 989.988 |
| 318.15 | 0.0009 | 989.983 |
| 318.15 | 0.0013 | 989.911 |
| 318.15 | 0.0013 | 989.908 |
| 318.15 | 0.0016 | 989.837 |
| 318.15 | 0.0016 | 989.832 |
| 318.15 | 0.0019 | 989.762 |
| 318.15 | 0.0019 | 989.758 |
| 318.15 | 0.0022 | 989.694 |
| 318.15 | 0.0022 | 989.679 |