- Name
- 2-Butanone
- InChI
- InChI=1S/C4H8O/c1-3-4(2)5/h3H2,1-2H3
- InChI Key
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N
- Formula
- C4H8O
- SMILES
- CCC(C)=O
- Mol. Weight (g/mol)
- 72.11
- CAS
- 78-93-3
- Name
- 1-Butanol
- InChI
- InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
- InChI Key
- LRHPLDYGYMQRHN-UHFFFAOYSA-N
- Formula
- C4H10O
- SMILES
- CCCCO
- Mol. Weight (g/mol)
- 74.12
- CAS
- 71-36-3
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Datasets
- η - Viscosity, Pa*s (4)
- Excess molar enthalpy (molar enthalpy (2)
- n0 - Refractive index (Na D-line) (4)
- ρl - Mass density, kg/m3 (6)
- csound,fluid - Speed of Sound, m/s (2)
Viscosity, Pa*s [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of 1-Butanol (2) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0000 | 0.0003 |
| 0.0704 | 0.0004 |
| 0.1468 | 0.0004 |
| 0.2163 | 0.0004 |
| 0.2818 | 0.0005 |
| 0.3429 | 0.0005 |
| 0.4244 | 0.0006 |
| 0.4988 | 0.0006 |
| 0.5755 | 0.0007 |
| 0.6474 | 0.0008 |
| 0.7105 | 0.0009 |
| 0.7799 | 0.0011 |
| 0.8596 | 0.0013 |
| 0.9263 | 0.0016 |
| 1.0000 | 0.0022 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0034 |
| 288.15 | 0.0997 | 0.0023 |
| 288.15 | 0.1999 | 0.0016 |
| 288.15 | 0.3003 | 0.0013 |
| 288.15 | 0.4008 | 0.0010 |
| 288.15 | 0.5003 | 0.0008 |
| 288.15 | 0.6001 | 0.0007 |
| 288.15 | 0.6992 | 0.0006 |
| 288.15 | 0.7991 | 0.0005 |
| 288.15 | 0.8990 | 0.0005 |
| 288.15 | 1.0000 | 0.0004 |
| 293.15 | 0.0000 | 0.0029 |
| 293.15 | 0.0997 | 0.0020 |
| 293.15 | 0.1999 | 0.0015 |
| 293.15 | 0.3003 | 0.0011 |
| 293.15 | 0.4008 | 0.0009 |
| 293.15 | 0.5003 | 0.0008 |
| 293.15 | 0.6001 | 0.0007 |
| 293.15 | 0.6992 | 0.0006 |
| 293.15 | 0.7991 | 0.0005 |
| 293.15 | 0.8990 | 0.0005 |
| 293.15 | 1.0000 | 0.0004 |
| 298.15 | 0.0000 | 0.0026 |
| 298.15 | 0.0997 | 0.0018 |
| 298.15 | 0.1999 | 0.0013 |
| 298.15 | 0.3003 | 0.0011 |
| 298.15 | 0.4008 | 0.0009 |
| 298.15 | 0.5003 | 0.0007 |
| 298.15 | 0.6001 | 0.0006 |
| 298.15 | 0.6992 | 0.0005 |
| 298.15 | 0.7991 | 0.0005 |
| 298.15 | 0.8990 | 0.0004 |
| 298.15 | 1.0000 | 0.0004 |
| 303.15 | 0.0000 | 0.0023 |
| 303.15 | 0.0997 | 0.0016 |
| 303.15 | 0.1999 | 0.0012 |
| 303.15 | 0.3003 | 0.0010 |
| 303.15 | 0.4008 | 0.0008 |
| 303.15 | 0.5003 | 0.0007 |
| 303.15 | 0.6001 | 0.0006 |
| 303.15 | 0.6992 | 0.0005 |
| 303.15 | 0.7991 | 0.0005 |
| 303.15 | 0.8990 | 0.0004 |
| 303.15 | 1.0000 | 0.0004 |
| 308.15 | 0.0000 | 0.0020 |
| 308.15 | 0.0997 | 0.0015 |
| 308.15 | 0.1999 | 0.0011 |
| 308.15 | 0.3003 | 0.0009 |
| 308.15 | 0.4008 | 0.0007 |
| 308.15 | 0.5003 | 0.0006 |
| 308.15 | 0.6001 | 0.0005 |
| 308.15 | 0.6992 | 0.0005 |
| 308.15 | 0.7991 | 0.0004 |
| 308.15 | 0.8990 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 313.15 | 0.0000 | 0.0018 |
| 313.15 | 0.0997 | 0.0013 |
| 313.15 | 0.1999 | 0.0010 |
| 313.15 | 0.3003 | 0.0008 |
| 313.15 | 0.4008 | 0.0007 |
| 313.15 | 0.5003 | 0.0006 |
| 313.15 | 0.6001 | 0.0005 |
| 313.15 | 0.6992 | 0.0005 |
| 313.15 | 0.7991 | 0.0004 |
| 313.15 | 0.8990 | 0.0004 |
| 313.15 | 1.0000 | 0.0003 |
| 318.15 | 0.0000 | 0.0016 |
| 318.15 | 0.0997 | 0.0012 |
| 318.15 | 0.1999 | 0.0009 |
| 318.15 | 0.3003 | 0.0008 |
| 318.15 | 0.4008 | 0.0006 |
| 318.15 | 0.5003 | 0.0006 |
| 318.15 | 0.6001 | 0.0005 |
| 318.15 | 0.6992 | 0.0004 |
| 318.15 | 0.7991 | 0.0004 |
| 318.15 | 0.8990 | 0.0004 |
| 318.15 | 1.0000 | 0.0003 |
| 323.15 | 0.0000 | 0.0014 |
| 323.15 | 0.0997 | 0.0011 |
| 323.15 | 0.1999 | 0.0009 |
| 323.15 | 0.3003 | 0.0007 |
| 323.15 | 0.4008 | 0.0006 |
| 323.15 | 0.5003 | 0.0005 |
| 323.15 | 0.6001 | 0.0005 |
| 323.15 | 0.6992 | 0.0004 |
| 323.15 | 0.7991 | 0.0004 |
| 323.15 | 0.8990 | 0.0003 |
| 323.15 | 1.0000 | 0.0003 |
Viscosity, Pa*s [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of 1-Butanol (2) - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 0.0000 | 0.0003 |
| 0.0704 | 0.0004 |
| 0.1468 | 0.0004 |
| 0.2163 | 0.0004 |
| 0.2818 | 0.0005 |
| 0.3429 | 0.0005 |
| 0.4244 | 0.0006 |
| 0.4988 | 0.0006 |
| 0.5755 | 0.0007 |
| 0.6474 | 0.0008 |
| 0.7105 | 0.0009 |
| 0.7799 | 0.0011 |
| 0.8596 | 0.0013 |
| 0.9263 | 0.0016 |
| 1.0000 | 0.0022 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0034 |
| 288.15 | 0.0997 | 0.0023 |
| 288.15 | 0.1999 | 0.0016 |
| 288.15 | 0.3003 | 0.0013 |
| 288.15 | 0.4008 | 0.0010 |
| 288.15 | 0.5003 | 0.0008 |
| 288.15 | 0.6001 | 0.0007 |
| 288.15 | 0.6992 | 0.0006 |
| 288.15 | 0.7991 | 0.0005 |
| 288.15 | 0.8990 | 0.0005 |
| 288.15 | 1.0000 | 0.0004 |
| 293.15 | 0.0000 | 0.0029 |
| 293.15 | 0.0997 | 0.0020 |
| 293.15 | 0.1999 | 0.0015 |
| 293.15 | 0.3003 | 0.0011 |
| 293.15 | 0.4008 | 0.0009 |
| 293.15 | 0.5003 | 0.0008 |
| 293.15 | 0.6001 | 0.0007 |
| 293.15 | 0.6992 | 0.0006 |
| 293.15 | 0.7991 | 0.0005 |
| 293.15 | 0.8990 | 0.0005 |
| 293.15 | 1.0000 | 0.0004 |
| 298.15 | 0.0000 | 0.0026 |
| 298.15 | 0.0997 | 0.0018 |
| 298.15 | 0.1999 | 0.0013 |
| 298.15 | 0.3003 | 0.0011 |
| 298.15 | 0.4008 | 0.0009 |
| 298.15 | 0.5003 | 0.0007 |
| 298.15 | 0.6001 | 0.0006 |
| 298.15 | 0.6992 | 0.0005 |
| 298.15 | 0.7991 | 0.0005 |
| 298.15 | 0.8990 | 0.0004 |
| 298.15 | 1.0000 | 0.0004 |
| 303.15 | 0.0000 | 0.0023 |
| 303.15 | 0.0997 | 0.0016 |
| 303.15 | 0.1999 | 0.0012 |
| 303.15 | 0.3003 | 0.0010 |
| 303.15 | 0.4008 | 0.0008 |
| 303.15 | 0.5003 | 0.0007 |
| 303.15 | 0.6001 | 0.0006 |
| 303.15 | 0.6992 | 0.0005 |
| 303.15 | 0.7991 | 0.0005 |
| 303.15 | 0.8990 | 0.0004 |
| 303.15 | 1.0000 | 0.0004 |
| 308.15 | 0.0000 | 0.0020 |
| 308.15 | 0.0997 | 0.0015 |
| 308.15 | 0.1999 | 0.0011 |
| 308.15 | 0.3003 | 0.0009 |
| 308.15 | 0.4008 | 0.0007 |
| 308.15 | 0.5003 | 0.0006 |
| 308.15 | 0.6001 | 0.0005 |
| 308.15 | 0.6992 | 0.0005 |
| 308.15 | 0.7991 | 0.0004 |
| 308.15 | 0.8990 | 0.0004 |
| 308.15 | 1.0000 | 0.0004 |
| 313.15 | 0.0000 | 0.0018 |
| 313.15 | 0.0997 | 0.0013 |
| 313.15 | 0.1999 | 0.0010 |
| 313.15 | 0.3003 | 0.0008 |
| 313.15 | 0.4008 | 0.0007 |
| 313.15 | 0.5003 | 0.0006 |
| 313.15 | 0.6001 | 0.0005 |
| 313.15 | 0.6992 | 0.0005 |
| 313.15 | 0.7991 | 0.0004 |
| 313.15 | 0.8990 | 0.0004 |
| 313.15 | 1.0000 | 0.0003 |
| 318.15 | 0.0000 | 0.0016 |
| 318.15 | 0.0997 | 0.0012 |
| 318.15 | 0.1999 | 0.0009 |
| 318.15 | 0.3003 | 0.0008 |
| 318.15 | 0.4008 | 0.0006 |
| 318.15 | 0.5003 | 0.0006 |
| 318.15 | 0.6001 | 0.0005 |
| 318.15 | 0.6992 | 0.0004 |
| 318.15 | 0.7991 | 0.0004 |
| 318.15 | 0.8990 | 0.0004 |
| 318.15 | 1.0000 | 0.0003 |
| 323.15 | 0.0000 | 0.0014 |
| 323.15 | 0.0997 | 0.0011 |
| 323.15 | 0.1999 | 0.0009 |
| 323.15 | 0.3003 | 0.0007 |
| 323.15 | 0.4008 | 0.0006 |
| 323.15 | 0.5003 | 0.0005 |
| 323.15 | 0.6001 | 0.0005 |
| 323.15 | 0.6992 | 0.0004 |
| 323.15 | 0.7991 | 0.0004 |
| 323.15 | 0.8990 | 0.0003 |
| 323.15 | 1.0000 | 0.0003 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 303 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Butanol (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0000 | 0.0000 |
| 0.1340 | 0.6430 |
| 0.1930 | 0.9190 |
| 0.2890 | 1.177 |
| 0.3500 | 1.356 |
| 0.4250 | 1.472 |
| 0.5140 | 1.467 |
| 0.6190 | 1.411 |
| 0.7000 | 1.228 |
| 0.7690 | 1.123 |
| 0.8200 | 0.8490 |
| 0.9110 | 0.5910 |
| 1.0000 | 0.0000 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 303 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Butanol (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0000 | 0.0000 |
| 0.1340 | 0.6430 |
| 0.1930 | 0.9190 |
| 0.2890 | 1.177 |
| 0.3500 | 1.356 |
| 0.4250 | 1.472 |
| 0.5140 | 1.467 |
| 0.6190 | 1.411 |
| 0.7000 | 1.228 |
| 0.7690 | 1.123 |
| 0.8200 | 0.8490 |
| 0.9110 | 0.5910 |
| 1.0000 | 0.0000 |
Refractive index (Na D-line) [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Butanol (2) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0000 | 1.3738 |
| 0.0765 | 1.3756 |
| 0.1392 | 1.377 |
| 0.2097 | 1.3787 |
| 0.2775 | 1.3802 |
| 0.3488 | 1.3819 |
| 0.4420 | 1.384 |
| 0.4933 | 1.3851 |
| 0.5008 | 1.3853 |
| 0.5577 | 1.3866 |
| 0.6404 | 1.3883 |
| 0.6474 | 1.3885 |
| 0.7257 | 1.3901 |
| 0.7944 | 1.3915 |
| 0.8562 | 1.3926 |
| 0.9307 | 1.3939 |
| 1.0000 | 1.3948 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.4014 |
| 288.15 | 0.0997 | 1.3994 |
| 288.15 | 0.1999 | 1.3975 |
| 288.15 | 0.3003 | 1.3956 |
| 288.15 | 0.4008 | 1.3936 |
| 288.15 | 0.5003 | 1.3917 |
| 288.15 | 0.6001 | 1.3897 |
| 288.15 | 0.6992 | 1.3877 |
| 288.15 | 0.7991 | 1.3857 |
| 288.15 | 0.8990 | 1.3836 |
| 288.15 | 1.0000 | 1.3815 |
| 293.15 | 0.0000 | 1.3993 |
| 293.15 | 0.0997 | 1.3973 |
| 293.15 | 0.1999 | 1.3953 |
| 293.15 | 0.3003 | 1.3933 |
| 293.15 | 0.4008 | 1.3913 |
| 293.15 | 0.5003 | 1.3893 |
| 293.15 | 0.6001 | 1.3873 |
| 293.15 | 0.6992 | 1.3853 |
| 293.15 | 0.7991 | 1.3832 |
| 293.15 | 0.8990 | 1.3811 |
| 293.15 | 1.0000 | 1.3789 |
| 298.15 | 0.0000 | 1.3973 |
| 298.15 | 0.0997 | 1.3952 |
| 298.15 | 0.1999 | 1.3932 |
| 298.15 | 0.3003 | 1.3911 |
| 298.15 | 0.4008 | 1.389 |
| 298.15 | 0.5003 | 1.387 |
| 298.15 | 0.6001 | 1.3849 |
| 298.15 | 0.6992 | 1.3828 |
| 298.15 | 0.7991 | 1.3806 |
| 298.15 | 0.8990 | 1.3785 |
| 298.15 | 1.0000 | 1.3763 |
| 303.15 | 0.0000 | 1.3952 |
| 303.15 | 0.0997 | 1.3931 |
| 303.15 | 0.1999 | 1.3909 |
| 303.15 | 0.3003 | 1.3888 |
| 303.15 | 0.4008 | 1.3867 |
| 303.15 | 0.5003 | 1.3846 |
| 303.15 | 0.6001 | 1.3824 |
| 303.15 | 0.6992 | 1.3802 |
| 303.15 | 0.7991 | 1.3781 |
| 303.15 | 0.8990 | 1.3759 |
| 303.15 | 1.0000 | 1.3737 |
| 308.15 | 0.0000 | 1.3932 |
| 308.15 | 0.0997 | 1.391 |
| 308.15 | 0.1999 | 1.3887 |
| 308.15 | 0.3003 | 1.3865 |
| 308.15 | 0.4008 | 1.3843 |
| 308.15 | 0.5003 | 1.3821 |
| 308.15 | 0.6001 | 1.38 |
| 308.15 | 0.6992 | 1.3778 |
| 308.15 | 0.7991 | 1.3755 |
| 308.15 | 0.8990 | 1.3733 |
| 308.15 | 1.0000 | 1.371 |
| 313.15 | 0.0000 | 1.3911 |
| 313.15 | 0.0997 | 1.3888 |
| 313.15 | 0.1999 | 1.3865 |
| 313.15 | 0.3003 | 1.3842 |
| 313.15 | 0.4008 | 1.382 |
| 313.15 | 0.5003 | 1.3797 |
| 313.15 | 0.6001 | 1.3775 |
| 313.15 | 0.6992 | 1.3752 |
| 313.15 | 0.7991 | 1.3729 |
| 313.15 | 0.8990 | 1.3706 |
| 313.15 | 1.0000 | 1.3683 |
| 318.15 | 0.0000 | 1.389 |
| 318.15 | 0.0997 | 1.3866 |
| 318.15 | 0.1999 | 1.3843 |
| 318.15 | 0.3003 | 1.3819 |
| 318.15 | 0.4008 | 1.3796 |
| 318.15 | 0.5003 | 1.3773 |
| 318.15 | 0.6001 | 1.375 |
| 318.15 | 0.6992 | 1.3726 |
| 318.15 | 0.7991 | 1.3703 |
| 318.15 | 0.8990 | 1.368 |
| 318.15 | 1.0000 | 1.3657 |
| 323.15 | 0.0000 | 1.3869 |
| 323.15 | 0.0997 | 1.3845 |
| 323.15 | 0.1999 | 1.382 |
| 323.15 | 0.3003 | 1.3796 |
| 323.15 | 0.4008 | 1.3772 |
| 323.15 | 0.5003 | 1.3748 |
| 323.15 | 0.6001 | 1.3724 |
| 323.15 | 0.6992 | 1.3701 |
| 323.15 | 0.7991 | 1.3677 |
| 323.15 | 0.8990 | 1.3653 |
| 323.15 | 1.0000 | 1.3629 |
Refractive index (Na D-line) [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of 1-Butanol (2) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0000 | 1.3738 |
| 0.0765 | 1.3756 |
| 0.1392 | 1.377 |
| 0.2097 | 1.3787 |
| 0.2775 | 1.3802 |
| 0.3488 | 1.3819 |
| 0.4420 | 1.384 |
| 0.4933 | 1.3851 |
| 0.5008 | 1.3853 |
| 0.5577 | 1.3866 |
| 0.6404 | 1.3883 |
| 0.6474 | 1.3885 |
| 0.7257 | 1.3901 |
| 0.7944 | 1.3915 |
| 0.8562 | 1.3926 |
| 0.9307 | 1.3939 |
| 1.0000 | 1.3948 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.4014 |
| 288.15 | 0.0997 | 1.3994 |
| 288.15 | 0.1999 | 1.3975 |
| 288.15 | 0.3003 | 1.3956 |
| 288.15 | 0.4008 | 1.3936 |
| 288.15 | 0.5003 | 1.3917 |
| 288.15 | 0.6001 | 1.3897 |
| 288.15 | 0.6992 | 1.3877 |
| 288.15 | 0.7991 | 1.3857 |
| 288.15 | 0.8990 | 1.3836 |
| 288.15 | 1.0000 | 1.3815 |
| 293.15 | 0.0000 | 1.3993 |
| 293.15 | 0.0997 | 1.3973 |
| 293.15 | 0.1999 | 1.3953 |
| 293.15 | 0.3003 | 1.3933 |
| 293.15 | 0.4008 | 1.3913 |
| 293.15 | 0.5003 | 1.3893 |
| 293.15 | 0.6001 | 1.3873 |
| 293.15 | 0.6992 | 1.3853 |
| 293.15 | 0.7991 | 1.3832 |
| 293.15 | 0.8990 | 1.3811 |
| 293.15 | 1.0000 | 1.3789 |
| 298.15 | 0.0000 | 1.3973 |
| 298.15 | 0.0997 | 1.3952 |
| 298.15 | 0.1999 | 1.3932 |
| 298.15 | 0.3003 | 1.3911 |
| 298.15 | 0.4008 | 1.389 |
| 298.15 | 0.5003 | 1.387 |
| 298.15 | 0.6001 | 1.3849 |
| 298.15 | 0.6992 | 1.3828 |
| 298.15 | 0.7991 | 1.3806 |
| 298.15 | 0.8990 | 1.3785 |
| 298.15 | 1.0000 | 1.3763 |
| 303.15 | 0.0000 | 1.3952 |
| 303.15 | 0.0997 | 1.3931 |
| 303.15 | 0.1999 | 1.3909 |
| 303.15 | 0.3003 | 1.3888 |
| 303.15 | 0.4008 | 1.3867 |
| 303.15 | 0.5003 | 1.3846 |
| 303.15 | 0.6001 | 1.3824 |
| 303.15 | 0.6992 | 1.3802 |
| 303.15 | 0.7991 | 1.3781 |
| 303.15 | 0.8990 | 1.3759 |
| 303.15 | 1.0000 | 1.3737 |
| 308.15 | 0.0000 | 1.3932 |
| 308.15 | 0.0997 | 1.391 |
| 308.15 | 0.1999 | 1.3887 |
| 308.15 | 0.3003 | 1.3865 |
| 308.15 | 0.4008 | 1.3843 |
| 308.15 | 0.5003 | 1.3821 |
| 308.15 | 0.6001 | 1.38 |
| 308.15 | 0.6992 | 1.3778 |
| 308.15 | 0.7991 | 1.3755 |
| 308.15 | 0.8990 | 1.3733 |
| 308.15 | 1.0000 | 1.371 |
| 313.15 | 0.0000 | 1.3911 |
| 313.15 | 0.0997 | 1.3888 |
| 313.15 | 0.1999 | 1.3865 |
| 313.15 | 0.3003 | 1.3842 |
| 313.15 | 0.4008 | 1.382 |
| 313.15 | 0.5003 | 1.3797 |
| 313.15 | 0.6001 | 1.3775 |
| 313.15 | 0.6992 | 1.3752 |
| 313.15 | 0.7991 | 1.3729 |
| 313.15 | 0.8990 | 1.3706 |
| 313.15 | 1.0000 | 1.3683 |
| 318.15 | 0.0000 | 1.389 |
| 318.15 | 0.0997 | 1.3866 |
| 318.15 | 0.1999 | 1.3843 |
| 318.15 | 0.3003 | 1.3819 |
| 318.15 | 0.4008 | 1.3796 |
| 318.15 | 0.5003 | 1.3773 |
| 318.15 | 0.6001 | 1.375 |
| 318.15 | 0.6992 | 1.3726 |
| 318.15 | 0.7991 | 1.3703 |
| 318.15 | 0.8990 | 1.368 |
| 318.15 | 1.0000 | 1.3657 |
| 323.15 | 0.0000 | 1.3869 |
| 323.15 | 0.0997 | 1.3845 |
| 323.15 | 0.1999 | 1.382 |
| 323.15 | 0.3003 | 1.3796 |
| 323.15 | 0.4008 | 1.3772 |
| 323.15 | 0.5003 | 1.3748 |
| 323.15 | 0.6001 | 1.3724 |
| 323.15 | 0.6992 | 1.3701 |
| 323.15 | 0.7991 | 1.3677 |
| 323.15 | 0.8990 | 1.3653 |
| 323.15 | 1.0000 | 1.3629 |
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of 1-Butanol (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 794.5 |
| 0.0765 | 795.0 |
| 0.1392 | 795.4 |
| 0.2097 | 795.9 |
| 0.2775 | 796.4 |
| 0.3488 | 796.9 |
| 0.4420 | 797.6 |
| 0.4933 | 798.0 |
| 0.5008 | 798.1 |
| 0.5577 | 798.5 |
| 0.6404 | 799.2 |
| 0.6474 | 799.3 |
| 0.7257 | 799.9 |
| 0.7944 | 800.5 |
| 0.8562 | 801.0 |
| 0.9307 | 801.6 |
| 1.0000 | 802.2 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of 2-Butanone (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.0000 | 293.15 | 809.613 |
| 0.0000 | 298.15 | 805.808 |
| 0.0000 | 303.15 | 801.969 |
| 0.0000 | 308.15 | 798.101 |
| 0.0000 | 313.15 | 794.193 |
| 0.0000 | 318.15 | 790.244 |
| 0.0000 | 323.15 | 786.25 |
| 0.1033 | 293.15 | 809.161 |
| 0.1033 | 298.15 | 805.17 |
| 0.1033 | 303.15 | 801.15 |
| 0.1033 | 308.15 | 797.099 |
| 0.1033 | 313.15 | 793.012 |
| 0.1033 | 318.15 | 788.886 |
| 0.1033 | 323.15 | 784.717 |
| 0.2069 | 293.15 | 808.682 |
| 0.2069 | 298.15 | 804.522 |
| 0.2069 | 303.15 | 800.336 |
| 0.2069 | 308.15 | 796.113 |
| 0.2069 | 313.15 | 791.857 |
| 0.2069 | 318.15 | 787.562 |
| 0.2069 | 323.15 | 783.207 |
| 0.3055 | 293.15 | 808.213 |
| 0.3055 | 298.15 | 803.902 |
| 0.3055 | 303.15 | 799.56 |
| 0.3055 | 308.15 | 795.189 |
| 0.3055 | 313.15 | 790.782 |
| 0.3055 | 318.15 | 786.339 |
| 0.3055 | 323.15 | 781.851 |
| 0.3998 | 293.15 | 807.77 |
| 0.3998 | 298.15 | 803.322 |
| 0.3998 | 303.15 | 798.841 |
| 0.3998 | 308.15 | 794.328 |
| 0.3998 | 313.15 | 789.78 |
| 0.3998 | 318.15 | 785.192 |
| 0.3998 | 323.15 | 780.568 |
| 0.5002 | 293.15 | 807.329 |
| 0.5002 | 298.15 | 802.74 |
| 0.5002 | 303.15 | 798.114 |
| 0.5002 | 308.15 | 793.459 |
| 0.5002 | 313.15 | 788.765 |
| 0.5002 | 318.15 | 784.037 |
| 0.5002 | 323.15 | 779.268 |
| 0.5937 | 293.15 | 806.88 |
| 0.5937 | 298.15 | 802.161 |
| 0.5937 | 303.15 | 797.412 |
| 0.5937 | 308.15 | 792.628 |
| 0.5937 | 313.15 | 787.807 |
| 0.5937 | 318.15 | 782.953 |
| 0.5937 | 323.15 | 778.061 |
| 0.7008 | 293.15 | 806.418 |
| 0.7008 | 298.15 | 801.555 |
| 0.7008 | 303.15 | 796.66 |
| 0.7008 | 308.15 | 791.73 |
| 0.7008 | 313.15 | 786.766 |
| 0.7008 | 318.15 | 781.765 |
| 0.7008 | 323.15 | 776.725 |
| 0.8030 | 293.15 | 805.915 |
| 0.8030 | 298.15 | 800.92 |
| 0.8030 | 303.15 | 795.887 |
| 0.8030 | 308.15 | 790.827 |
| 0.8030 | 313.15 | 785.725 |
| 0.8030 | 318.15 | 780.596 |
| 0.8030 | 323.15 | 775.415 |
| 0.8974 | 293.15 | 805.458 |
| 0.8974 | 298.15 | 800.34 |
| 0.8974 | 303.15 | 795.198 |
| 0.8974 | 308.15 | 790.021 |
| 0.8974 | 313.15 | 784.812 |
| 0.8974 | 318.15 | 779.565 |
| 0.8974 | 323.15 | 774.284 |
| 1.0000 | 293.15 | 804.903 |
| 1.0000 | 298.15 | 799.678 |
| 1.0000 | 303.15 | 794.414 |
| 1.0000 | 308.15 | 789.124 |
| 1.0000 | 313.15 | 783.798 |
| 1.0000 | 318.15 | 778.438 |
| 1.0000 | 323.15 | 773.04 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 813.373 |
| 288.15 | 0.0997 | 813.126 |
| 288.15 | 0.1999 | 812.877 |
| 288.15 | 0.3003 | 812.583 |
| 288.15 | 0.4008 | 812.253 |
| 288.15 | 0.5003 | 811.906 |
| 288.15 | 0.6001 | 811.555 |
| 288.15 | 0.6992 | 811.203 |
| 288.15 | 0.7991 | 810.843 |
| 288.15 | 0.8990 | 810.477 |
| 288.15 | 1.0000 | 810.133 |
| 293.15 | 0.0000 | 809.573 |
| 293.15 | 0.0997 | 809.157 |
| 293.15 | 0.1999 | 808.747 |
| 293.15 | 0.3003 | 808.3 |
| 293.15 | 0.4008 | 807.824 |
| 293.15 | 0.5003 | 807.337 |
| 293.15 | 0.6001 | 806.848 |
| 293.15 | 0.6992 | 806.362 |
| 293.15 | 0.7991 | 805.875 |
| 293.15 | 0.8990 | 805.39 |
| 293.15 | 1.0000 | 804.926 |
| 298.15 | 0.0000 | 805.762 |
| 298.15 | 0.0997 | 805.165 |
| 298.15 | 0.1999 | 804.592 |
| 298.15 | 0.3003 | 803.992 |
| 298.15 | 0.4008 | 803.369 |
| 298.15 | 0.5003 | 802.741 |
| 298.15 | 0.6001 | 802.114 |
| 298.15 | 0.6992 | 801.494 |
| 298.15 | 0.7991 | 800.878 |
| 298.15 | 0.8990 | 800.271 |
| 298.15 | 1.0000 | 799.695 |
| 303.15 | 0.0000 | 801.923 |
| 303.15 | 0.0997 | 801.147 |
| 303.15 | 0.1999 | 800.407 |
| 303.15 | 0.3003 | 799.653 |
| 303.15 | 0.4008 | 798.884 |
| 303.15 | 0.5003 | 798.115 |
| 303.15 | 0.6001 | 797.349 |
| 303.15 | 0.6992 | 796.597 |
| 303.15 | 0.7991 | 795.852 |
| 303.15 | 0.8990 | 795.126 |
| 303.15 | 1.0000 | 794.435 |
| 308.15 | 0.0000 | 798.053 |
| 308.15 | 0.0997 | 797.097 |
| 308.15 | 0.1999 | 796.195 |
| 308.15 | 0.3003 | 795.288 |
| 308.15 | 0.4008 | 794.369 |
| 308.15 | 0.5003 | 793.457 |
| 308.15 | 0.6001 | 792.551 |
| 308.15 | 0.6992 | 791.666 |
| 308.15 | 0.7991 | 790.793 |
| 308.15 | 0.8990 | 789.946 |
| 308.15 | 1.0000 | 789.142 |
| 313.15 | 0.0000 | 794.147 |
| 313.15 | 0.0997 | 793.009 |
| 313.15 | 0.1999 | 791.945 |
| 313.15 | 0.3003 | 790.885 |
| 313.15 | 0.4008 | 789.819 |
| 313.15 | 0.5003 | 788.763 |
| 313.15 | 0.6001 | 787.719 |
| 313.15 | 0.6992 | 786.701 |
| 313.15 | 0.7991 | 785.7 |
| 313.15 | 0.8990 | 784.731 |
| 313.15 | 1.0000 | 783.814 |
| 318.15 | 0.0000 | 790.231 |
| 318.15 | 0.0997 | 788.88 |
| 318.15 | 0.1999 | 787.652 |
| 318.15 | 0.3003 | 786.442 |
| 318.15 | 0.4008 | 785.228 |
| 318.15 | 0.5003 | 784.03 |
| 318.15 | 0.6001 | 782.849 |
| 318.15 | 0.6992 | 781.696 |
| 318.15 | 0.7991 | 780.568 |
| 318.15 | 0.8990 | 779.478 |
| 318.15 | 1.0000 | 778.451 |
| 323.15 | 0.0000 | 786.238 |
| 323.15 | 0.0997 | 784.708 |
| 323.15 | 0.1999 | 783.318 |
| 323.15 | 0.3003 | 781.954 |
| 323.15 | 0.4008 | 780.593 |
| 323.15 | 0.5003 | 779.253 |
| 323.15 | 0.6001 | 777.934 |
| 323.15 | 0.6992 | 776.652 |
| 323.15 | 0.7991 | 775.398 |
| 323.15 | 0.8990 | 774.188 |
| 323.15 | 1.0000 | 773.047 |
Mass density, kg/m3 [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 303.15 (Liquid)
| Mole fraction of 1-Butanol (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 794.5 |
| 0.0765 | 795.0 |
| 0.1392 | 795.4 |
| 0.2097 | 795.9 |
| 0.2775 | 796.4 |
| 0.3488 | 796.9 |
| 0.4420 | 797.6 |
| 0.4933 | 798.0 |
| 0.5008 | 798.1 |
| 0.5577 | 798.5 |
| 0.6404 | 799.2 |
| 0.6474 | 799.3 |
| 0.7257 | 799.9 |
| 0.7944 | 800.5 |
| 0.8562 | 801.0 |
| 0.9307 | 801.6 |
| 1.0000 | 802.2 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of 2-Butanone (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.0000 | 293.15 | 809.613 |
| 0.0000 | 298.15 | 805.808 |
| 0.0000 | 303.15 | 801.969 |
| 0.0000 | 308.15 | 798.101 |
| 0.0000 | 313.15 | 794.193 |
| 0.0000 | 318.15 | 790.244 |
| 0.0000 | 323.15 | 786.25 |
| 0.1033 | 293.15 | 809.161 |
| 0.1033 | 298.15 | 805.17 |
| 0.1033 | 303.15 | 801.15 |
| 0.1033 | 308.15 | 797.099 |
| 0.1033 | 313.15 | 793.012 |
| 0.1033 | 318.15 | 788.886 |
| 0.1033 | 323.15 | 784.717 |
| 0.2069 | 293.15 | 808.682 |
| 0.2069 | 298.15 | 804.522 |
| 0.2069 | 303.15 | 800.336 |
| 0.2069 | 308.15 | 796.113 |
| 0.2069 | 313.15 | 791.857 |
| 0.2069 | 318.15 | 787.562 |
| 0.2069 | 323.15 | 783.207 |
| 0.3055 | 293.15 | 808.213 |
| 0.3055 | 298.15 | 803.902 |
| 0.3055 | 303.15 | 799.56 |
| 0.3055 | 308.15 | 795.189 |
| 0.3055 | 313.15 | 790.782 |
| 0.3055 | 318.15 | 786.339 |
| 0.3055 | 323.15 | 781.851 |
| 0.3998 | 293.15 | 807.77 |
| 0.3998 | 298.15 | 803.322 |
| 0.3998 | 303.15 | 798.841 |
| 0.3998 | 308.15 | 794.328 |
| 0.3998 | 313.15 | 789.78 |
| 0.3998 | 318.15 | 785.192 |
| 0.3998 | 323.15 | 780.568 |
| 0.5002 | 293.15 | 807.329 |
| 0.5002 | 298.15 | 802.74 |
| 0.5002 | 303.15 | 798.114 |
| 0.5002 | 308.15 | 793.459 |
| 0.5002 | 313.15 | 788.765 |
| 0.5002 | 318.15 | 784.037 |
| 0.5002 | 323.15 | 779.268 |
| 0.5937 | 293.15 | 806.88 |
| 0.5937 | 298.15 | 802.161 |
| 0.5937 | 303.15 | 797.412 |
| 0.5937 | 308.15 | 792.628 |
| 0.5937 | 313.15 | 787.807 |
| 0.5937 | 318.15 | 782.953 |
| 0.5937 | 323.15 | 778.061 |
| 0.7008 | 293.15 | 806.418 |
| 0.7008 | 298.15 | 801.555 |
| 0.7008 | 303.15 | 796.66 |
| 0.7008 | 308.15 | 791.73 |
| 0.7008 | 313.15 | 786.766 |
| 0.7008 | 318.15 | 781.765 |
| 0.7008 | 323.15 | 776.725 |
| 0.8030 | 293.15 | 805.915 |
| 0.8030 | 298.15 | 800.92 |
| 0.8030 | 303.15 | 795.887 |
| 0.8030 | 308.15 | 790.827 |
| 0.8030 | 313.15 | 785.725 |
| 0.8030 | 318.15 | 780.596 |
| 0.8030 | 323.15 | 775.415 |
| 0.8974 | 293.15 | 805.458 |
| 0.8974 | 298.15 | 800.34 |
| 0.8974 | 303.15 | 795.198 |
| 0.8974 | 308.15 | 790.021 |
| 0.8974 | 313.15 | 784.812 |
| 0.8974 | 318.15 | 779.565 |
| 0.8974 | 323.15 | 774.284 |
| 1.0000 | 293.15 | 804.903 |
| 1.0000 | 298.15 | 799.678 |
| 1.0000 | 303.15 | 794.414 |
| 1.0000 | 308.15 | 789.124 |
| 1.0000 | 313.15 | 783.798 |
| 1.0000 | 318.15 | 778.438 |
| 1.0000 | 323.15 | 773.04 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of 2-Butanone (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 813.373 |
| 288.15 | 0.0997 | 813.126 |
| 288.15 | 0.1999 | 812.877 |
| 288.15 | 0.3003 | 812.583 |
| 288.15 | 0.4008 | 812.253 |
| 288.15 | 0.5003 | 811.906 |
| 288.15 | 0.6001 | 811.555 |
| 288.15 | 0.6992 | 811.203 |
| 288.15 | 0.7991 | 810.843 |
| 288.15 | 0.8990 | 810.477 |
| 288.15 | 1.0000 | 810.133 |
| 293.15 | 0.0000 | 809.573 |
| 293.15 | 0.0997 | 809.157 |
| 293.15 | 0.1999 | 808.747 |
| 293.15 | 0.3003 | 808.3 |
| 293.15 | 0.4008 | 807.824 |
| 293.15 | 0.5003 | 807.337 |
| 293.15 | 0.6001 | 806.848 |
| 293.15 | 0.6992 | 806.362 |
| 293.15 | 0.7991 | 805.875 |
| 293.15 | 0.8990 | 805.39 |
| 293.15 | 1.0000 | 804.926 |
| 298.15 | 0.0000 | 805.762 |
| 298.15 | 0.0997 | 805.165 |
| 298.15 | 0.1999 | 804.592 |
| 298.15 | 0.3003 | 803.992 |
| 298.15 | 0.4008 | 803.369 |
| 298.15 | 0.5003 | 802.741 |
| 298.15 | 0.6001 | 802.114 |
| 298.15 | 0.6992 | 801.494 |
| 298.15 | 0.7991 | 800.878 |
| 298.15 | 0.8990 | 800.271 |
| 298.15 | 1.0000 | 799.695 |
| 303.15 | 0.0000 | 801.923 |
| 303.15 | 0.0997 | 801.147 |
| 303.15 | 0.1999 | 800.407 |
| 303.15 | 0.3003 | 799.653 |
| 303.15 | 0.4008 | 798.884 |
| 303.15 | 0.5003 | 798.115 |
| 303.15 | 0.6001 | 797.349 |
| 303.15 | 0.6992 | 796.597 |
| 303.15 | 0.7991 | 795.852 |
| 303.15 | 0.8990 | 795.126 |
| 303.15 | 1.0000 | 794.435 |
| 308.15 | 0.0000 | 798.053 |
| 308.15 | 0.0997 | 797.097 |
| 308.15 | 0.1999 | 796.195 |
| 308.15 | 0.3003 | 795.288 |
| 308.15 | 0.4008 | 794.369 |
| 308.15 | 0.5003 | 793.457 |
| 308.15 | 0.6001 | 792.551 |
| 308.15 | 0.6992 | 791.666 |
| 308.15 | 0.7991 | 790.793 |
| 308.15 | 0.8990 | 789.946 |
| 308.15 | 1.0000 | 789.142 |
| 313.15 | 0.0000 | 794.147 |
| 313.15 | 0.0997 | 793.009 |
| 313.15 | 0.1999 | 791.945 |
| 313.15 | 0.3003 | 790.885 |
| 313.15 | 0.4008 | 789.819 |
| 313.15 | 0.5003 | 788.763 |
| 313.15 | 0.6001 | 787.719 |
| 313.15 | 0.6992 | 786.701 |
| 313.15 | 0.7991 | 785.7 |
| 313.15 | 0.8990 | 784.731 |
| 313.15 | 1.0000 | 783.814 |
| 318.15 | 0.0000 | 790.231 |
| 318.15 | 0.0997 | 788.88 |
| 318.15 | 0.1999 | 787.652 |
| 318.15 | 0.3003 | 786.442 |
| 318.15 | 0.4008 | 785.228 |
| 318.15 | 0.5003 | 784.03 |
| 318.15 | 0.6001 | 782.849 |
| 318.15 | 0.6992 | 781.696 |
| 318.15 | 0.7991 | 780.568 |
| 318.15 | 0.8990 | 779.478 |
| 318.15 | 1.0000 | 778.451 |
| 323.15 | 0.0000 | 786.238 |
| 323.15 | 0.0997 | 784.708 |
| 323.15 | 0.1999 | 783.318 |
| 323.15 | 0.3003 | 781.954 |
| 323.15 | 0.4008 | 780.593 |
| 323.15 | 0.5003 | 779.253 |
| 323.15 | 0.6001 | 777.934 |
| 323.15 | 0.6992 | 776.652 |
| 323.15 | 0.7991 | 775.398 |
| 323.15 | 0.8990 | 774.188 |
| 323.15 | 1.0000 | 773.047 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of 2-Butanone (1) - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 0.0000 | 293.15 | 1257.01 |
| 0.0000 | 298.15 | 1240.37 |
| 0.0000 | 303.15 | 1223.64 |
| 0.0000 | 308.15 | 1206.95 |
| 0.0000 | 313.15 | 1190.34 |
| 0.0000 | 318.15 | 1173.84 |
| 0.0000 | 323.15 | 1157.36 |
| 0.1033 | 293.15 | 1253.19 |
| 0.1033 | 298.15 | 1235.96 |
| 0.1033 | 303.15 | 1218.6 |
| 0.1033 | 308.15 | 1201.3 |
| 0.1033 | 313.15 | 1184.11 |
| 0.1033 | 318.15 | 1166.99 |
| 0.1033 | 323.15 | 1149.96 |
| 0.2069 | 293.15 | 1248.52 |
| 0.2069 | 298.15 | 1230.78 |
| 0.2069 | 303.15 | 1212.91 |
| 0.2069 | 308.15 | 1195.07 |
| 0.2069 | 313.15 | 1177.32 |
| 0.2069 | 318.15 | 1159.64 |
| 0.2069 | 323.15 | 1141.75 |
| 0.3055 | 293.15 | 1243.9 |
| 0.3055 | 298.15 | 1225.51 |
| 0.3055 | 303.15 | 1207.32 |
| 0.3055 | 308.15 | 1189.09 |
| 0.3055 | 313.15 | 1170.9 |
| 0.3055 | 318.15 | 1152.79 |
| 0.3055 | 323.15 | 1134.72 |
| 0.3998 | 293.15 | 1239.61 |
| 0.3998 | 298.15 | 1221.08 |
| 0.3998 | 303.15 | 1202.31 |
| 0.3998 | 308.15 | 1183.64 |
| 0.3998 | 313.15 | 1165.03 |
| 0.3998 | 318.15 | 1146.45 |
| 0.3998 | 323.15 | 1127.99 |
| 0.5002 | 293.15 | 1235.42 |
| 0.5002 | 298.15 | 1216.38 |
| 0.5002 | 303.15 | 1197.2 |
| 0.5002 | 308.15 | 1178.15 |
| 0.5002 | 313.15 | 1159.11 |
| 0.5002 | 318.15 | 1140.14 |
| 0.5002 | 323.15 | 1121.21 |
| 0.5937 | 293.15 | 1231.47 |
| 0.5937 | 298.15 | 1212.18 |
| 0.5937 | 303.15 | 1192.7 |
| 0.5937 | 308.15 | 1173.24 |
| 0.5937 | 313.15 | 1153.82 |
| 0.5937 | 318.15 | 1134.49 |
| 0.5937 | 323.15 | 1115.23 |
| 0.7008 | 293.15 | 1227.47 |
| 0.7008 | 298.15 | 1207.71 |
| 0.7008 | 303.15 | 1187.75 |
| 0.7008 | 308.15 | 1167.81 |
| 0.7008 | 313.15 | 1147.93 |
| 0.7008 | 318.15 | 1128.12 |
| 0.7008 | 323.15 | 1108.31 |
| 0.8030 | 293.15 | 1223.62 |
| 0.8030 | 298.15 | 1203.33 |
| 0.8030 | 303.15 | 1182.84 |
| 0.8030 | 308.15 | 1162.46 |
| 0.8030 | 313.15 | 1142.04 |
| 0.8030 | 318.15 | 1121.75 |
| 0.8030 | 323.15 | 1101.39 |
| 0.8974 | 293.15 | 1219.34 |
| 0.8974 | 298.15 | 1198.4 |
| 0.8974 | 303.15 | 1177.74 |
| 0.8974 | 308.15 | 1156.89 |
| 0.8974 | 313.15 | 1136.08 |
| 0.8974 | 318.15 | 1115.34 |
| 0.8974 | 323.15 | 1094.68 |
| 1.0000 | 293.15 | 1213.3 |
| 1.0000 | 298.15 | 1192.14 |
| 1.0000 | 303.15 | 1170.79 |
| 1.0000 | 308.15 | 1149.57 |
| 1.0000 | 313.15 | 1128.37 |
| 1.0000 | 318.15 | 1107.27 |
| 1.0000 | 323.15 | 1086.19 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of 2-Butanone (1) - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 0.0000 | 293.15 | 1257.01 |
| 0.0000 | 298.15 | 1240.37 |
| 0.0000 | 303.15 | 1223.64 |
| 0.0000 | 308.15 | 1206.95 |
| 0.0000 | 313.15 | 1190.34 |
| 0.0000 | 318.15 | 1173.84 |
| 0.0000 | 323.15 | 1157.36 |
| 0.1033 | 293.15 | 1253.19 |
| 0.1033 | 298.15 | 1235.96 |
| 0.1033 | 303.15 | 1218.6 |
| 0.1033 | 308.15 | 1201.3 |
| 0.1033 | 313.15 | 1184.11 |
| 0.1033 | 318.15 | 1166.99 |
| 0.1033 | 323.15 | 1149.96 |
| 0.2069 | 293.15 | 1248.52 |
| 0.2069 | 298.15 | 1230.78 |
| 0.2069 | 303.15 | 1212.91 |
| 0.2069 | 308.15 | 1195.07 |
| 0.2069 | 313.15 | 1177.32 |
| 0.2069 | 318.15 | 1159.64 |
| 0.2069 | 323.15 | 1141.75 |
| 0.3055 | 293.15 | 1243.9 |
| 0.3055 | 298.15 | 1225.51 |
| 0.3055 | 303.15 | 1207.32 |
| 0.3055 | 308.15 | 1189.09 |
| 0.3055 | 313.15 | 1170.9 |
| 0.3055 | 318.15 | 1152.79 |
| 0.3055 | 323.15 | 1134.72 |
| 0.3998 | 293.15 | 1239.61 |
| 0.3998 | 298.15 | 1221.08 |
| 0.3998 | 303.15 | 1202.31 |
| 0.3998 | 308.15 | 1183.64 |
| 0.3998 | 313.15 | 1165.03 |
| 0.3998 | 318.15 | 1146.45 |
| 0.3998 | 323.15 | 1127.99 |
| 0.5002 | 293.15 | 1235.42 |
| 0.5002 | 298.15 | 1216.38 |
| 0.5002 | 303.15 | 1197.2 |
| 0.5002 | 308.15 | 1178.15 |
| 0.5002 | 313.15 | 1159.11 |
| 0.5002 | 318.15 | 1140.14 |
| 0.5002 | 323.15 | 1121.21 |
| 0.5937 | 293.15 | 1231.47 |
| 0.5937 | 298.15 | 1212.18 |
| 0.5937 | 303.15 | 1192.7 |
| 0.5937 | 308.15 | 1173.24 |
| 0.5937 | 313.15 | 1153.82 |
| 0.5937 | 318.15 | 1134.49 |
| 0.5937 | 323.15 | 1115.23 |
| 0.7008 | 293.15 | 1227.47 |
| 0.7008 | 298.15 | 1207.71 |
| 0.7008 | 303.15 | 1187.75 |
| 0.7008 | 308.15 | 1167.81 |
| 0.7008 | 313.15 | 1147.93 |
| 0.7008 | 318.15 | 1128.12 |
| 0.7008 | 323.15 | 1108.31 |
| 0.8030 | 293.15 | 1223.62 |
| 0.8030 | 298.15 | 1203.33 |
| 0.8030 | 303.15 | 1182.84 |
| 0.8030 | 308.15 | 1162.46 |
| 0.8030 | 313.15 | 1142.04 |
| 0.8030 | 318.15 | 1121.75 |
| 0.8030 | 323.15 | 1101.39 |
| 0.8974 | 293.15 | 1219.34 |
| 0.8974 | 298.15 | 1198.4 |
| 0.8974 | 303.15 | 1177.74 |
| 0.8974 | 308.15 | 1156.89 |
| 0.8974 | 313.15 | 1136.08 |
| 0.8974 | 318.15 | 1115.34 |
| 0.8974 | 323.15 | 1094.68 |
| 1.0000 | 293.15 | 1213.3 |
| 1.0000 | 298.15 | 1192.14 |
| 1.0000 | 303.15 | 1170.79 |
| 1.0000 | 308.15 | 1149.57 |
| 1.0000 | 313.15 | 1128.37 |
| 1.0000 | 318.15 | 1107.27 |
| 1.0000 | 323.15 | 1086.19 |
Sources
- Density, viscosity, refractive index, excess molar enthalpy, viscosity, and refractive index deviations for the (1-butanol + 2-butanone) binary system at T = 303 K. A new adiabatic calorimeter for heat of mixing
- Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
- Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K