- Name
- Acetic anhydride
- InChI
- InChI=1S/C4H6O3/c1-3(5)7-4(2)6/h1-2H3
- InChI Key
- WFDIJRYMOXRFFG-UHFFFAOYSA-N
- Formula
- C4H6O3
- SMILES
- CC(=O)OC(C)=O
- Mol. Weight (g/mol)
- 102.09
- CAS
- 108-24-7
- Name
- Acetic acid
- InChI
- InChI=1S/C2H4O2/c1-2(3)4/h1H3,(H,3,4)
- InChI Key
- QTBSBXVTEAMEQO-UHFFFAOYSA-N
- Formula
- C2H4O2
- SMILES
- CC(=O)O
- Mol. Weight (g/mol)
- 60.05
- CAS
- 64-19-7
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Datasets
- Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
- η - Viscosity, Pa*s (2)
- Excess molar enthalpy (molar enthalpy (2)
- ρl - Mass density, kg/m3 (2)
Molar heat capacity at constant pressure, J/K/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetic anhydride (1) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 308.15 | 0.0000 | 134.93 |
| 308.15 | 0.0613 | 139.18 |
| 308.15 | 0.1282 | 144.25 |
| 308.15 | 0.2013 | 149.40 |
| 308.15 | 0.2817 | 154.90 |
| 308.15 | 0.3704 | 160.85 |
| 308.15 | 0.4687 | 167.30 |
| 308.15 | 0.5785 | 174.47 |
| 308.15 | 0.7017 | 182.33 |
| 308.15 | 0.8411 | 190.56 |
| 308.15 | 1.0000 | 199.93 |
| 313.15 | 0.0000 | 135.50 |
| 313.15 | 0.0613 | 139.82 |
| 313.15 | 0.1282 | 144.91 |
| 313.15 | 0.2013 | 150.09 |
| 313.15 | 0.2817 | 155.59 |
| 313.15 | 0.3704 | 161.58 |
| 313.15 | 0.4687 | 168.08 |
| 313.15 | 0.5785 | 175.28 |
| 313.15 | 0.7017 | 183.12 |
| 313.15 | 0.8411 | 191.49 |
| 313.15 | 1.0000 | 200.73 |
| 318.15 | 0.0000 | 136.00 |
| 318.15 | 0.0613 | 140.51 |
| 318.15 | 0.1282 | 145.46 |
| 318.15 | 0.2013 | 150.76 |
| 318.15 | 0.2817 | 156.27 |
| 318.15 | 0.3704 | 162.26 |
| 318.15 | 0.4687 | 168.76 |
| 318.15 | 0.5785 | 176.03 |
| 318.15 | 0.7017 | 183.96 |
| 318.15 | 0.8411 | 192.33 |
| 318.15 | 1.0000 | 201.58 |
| 323.15 | 0.0000 | 136.35 |
| 323.15 | 0.0613 | 141.12 |
| 323.15 | 0.1282 | 145.90 |
| 323.15 | 0.2013 | 151.31 |
| 323.15 | 0.2817 | 156.85 |
| 323.15 | 0.3704 | 162.89 |
| 323.15 | 0.4687 | 169.45 |
| 323.15 | 0.5785 | 176.76 |
| 323.15 | 0.7017 | 184.78 |
| 323.15 | 0.8411 | 193.23 |
| 323.15 | 1.0000 | 202.53 |
| 328.15 | 0.0000 | 136.87 |
| 328.15 | 0.0613 | 141.75 |
| 328.15 | 0.1282 | 146.52 |
| 328.15 | 0.2013 | 152.03 |
| 328.15 | 0.2817 | 157.59 |
| 328.15 | 0.3704 | 163.68 |
| 328.15 | 0.4687 | 170.33 |
| 328.15 | 0.5785 | 177.68 |
| 328.15 | 0.7017 | 185.79 |
| 328.15 | 0.8411 | 194.35 |
| 328.15 | 1.0000 | 203.67 |
| 333.15 | 0.0000 | 137.21 |
| 333.15 | 0.0613 | 142.23 |
| 333.15 | 0.1282 | 147.13 |
| 333.15 | 0.2013 | 152.51 |
| 333.15 | 0.2817 | 158.10 |
| 333.15 | 0.3704 | 164.24 |
| 333.15 | 0.4687 | 170.89 |
| 333.15 | 0.5785 | 178.31 |
| 333.15 | 0.7017 | 186.44 |
| 333.15 | 0.8411 | 195.00 |
| 333.15 | 1.0000 | 204.34 |
Molar heat capacity at constant pressure, J/K/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetic anhydride (1) - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 308.15 | 0.0000 | 134.93 |
| 308.15 | 0.0613 | 139.18 |
| 308.15 | 0.1282 | 144.25 |
| 308.15 | 0.2013 | 149.40 |
| 308.15 | 0.2817 | 154.90 |
| 308.15 | 0.3704 | 160.85 |
| 308.15 | 0.4687 | 167.30 |
| 308.15 | 0.5785 | 174.47 |
| 308.15 | 0.7017 | 182.33 |
| 308.15 | 0.8411 | 190.56 |
| 308.15 | 1.0000 | 199.93 |
| 313.15 | 0.0000 | 135.50 |
| 313.15 | 0.0613 | 139.82 |
| 313.15 | 0.1282 | 144.91 |
| 313.15 | 0.2013 | 150.09 |
| 313.15 | 0.2817 | 155.59 |
| 313.15 | 0.3704 | 161.58 |
| 313.15 | 0.4687 | 168.08 |
| 313.15 | 0.5785 | 175.28 |
| 313.15 | 0.7017 | 183.12 |
| 313.15 | 0.8411 | 191.49 |
| 313.15 | 1.0000 | 200.73 |
| 318.15 | 0.0000 | 136.00 |
| 318.15 | 0.0613 | 140.51 |
| 318.15 | 0.1282 | 145.46 |
| 318.15 | 0.2013 | 150.76 |
| 318.15 | 0.2817 | 156.27 |
| 318.15 | 0.3704 | 162.26 |
| 318.15 | 0.4687 | 168.76 |
| 318.15 | 0.5785 | 176.03 |
| 318.15 | 0.7017 | 183.96 |
| 318.15 | 0.8411 | 192.33 |
| 318.15 | 1.0000 | 201.58 |
| 323.15 | 0.0000 | 136.35 |
| 323.15 | 0.0613 | 141.12 |
| 323.15 | 0.1282 | 145.90 |
| 323.15 | 0.2013 | 151.31 |
| 323.15 | 0.2817 | 156.85 |
| 323.15 | 0.3704 | 162.89 |
| 323.15 | 0.4687 | 169.45 |
| 323.15 | 0.5785 | 176.76 |
| 323.15 | 0.7017 | 184.78 |
| 323.15 | 0.8411 | 193.23 |
| 323.15 | 1.0000 | 202.53 |
| 328.15 | 0.0000 | 136.87 |
| 328.15 | 0.0613 | 141.75 |
| 328.15 | 0.1282 | 146.52 |
| 328.15 | 0.2013 | 152.03 |
| 328.15 | 0.2817 | 157.59 |
| 328.15 | 0.3704 | 163.68 |
| 328.15 | 0.4687 | 170.33 |
| 328.15 | 0.5785 | 177.68 |
| 328.15 | 0.7017 | 185.79 |
| 328.15 | 0.8411 | 194.35 |
| 328.15 | 1.0000 | 203.67 |
| 333.15 | 0.0000 | 137.21 |
| 333.15 | 0.0613 | 142.23 |
| 333.15 | 0.1282 | 147.13 |
| 333.15 | 0.2013 | 152.51 |
| 333.15 | 0.2817 | 158.10 |
| 333.15 | 0.3704 | 164.24 |
| 333.15 | 0.4687 | 170.89 |
| 333.15 | 0.5785 | 178.31 |
| 333.15 | 0.7017 | 186.44 |
| 333.15 | 0.8411 | 195.00 |
| 333.15 | 1.0000 | 204.34 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetic acid (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0009 |
| 293.15 | 0.1000 | 0.0009 |
| 293.15 | 0.2000 | 0.0009 |
| 293.15 | 0.2999 | 0.0009 |
| 293.15 | 0.3996 | 0.0010 |
| 293.15 | 0.4999 | 0.0010 |
| 293.15 | 0.5965 | 0.0010 |
| 293.15 | 0.6992 | 0.0010 |
| 293.15 | 0.8004 | 0.0011 |
| 293.15 | 0.8976 | 0.0011 |
| 293.15 | 1.0000 | 0.0012 |
| 298.15 | 0.0000 | 0.0008 |
| 298.15 | 0.1000 | 0.0008 |
| 298.15 | 0.2000 | 0.0009 |
| 298.15 | 0.2999 | 0.0009 |
| 298.15 | 0.3996 | 0.0009 |
| 298.15 | 0.4999 | 0.0009 |
| 298.15 | 0.5965 | 0.0009 |
| 298.15 | 0.6992 | 0.0010 |
| 298.15 | 0.8004 | 0.0010 |
| 298.15 | 0.8976 | 0.0011 |
| 298.15 | 1.0000 | 0.0011 |
| 303.15 | 0.0000 | 0.0008 |
| 303.15 | 0.1000 | 0.0008 |
| 303.15 | 0.2000 | 0.0008 |
| 303.15 | 0.2999 | 0.0008 |
| 303.15 | 0.3996 | 0.0008 |
| 303.15 | 0.4999 | 0.0008 |
| 303.15 | 0.5965 | 0.0009 |
| 303.15 | 0.6992 | 0.0009 |
| 303.15 | 0.8004 | 0.0009 |
| 303.15 | 0.8976 | 0.0010 |
| 303.15 | 1.0000 | 0.0010 |
| 308.15 | 0.0000 | 0.0007 |
| 308.15 | 0.1000 | 0.0007 |
| 308.15 | 0.2000 | 0.0008 |
| 308.15 | 0.2999 | 0.0008 |
| 308.15 | 0.3996 | 0.0008 |
| 308.15 | 0.4999 | 0.0008 |
| 308.15 | 0.5965 | 0.0008 |
| 308.15 | 0.6992 | 0.0008 |
| 308.15 | 0.8004 | 0.0009 |
| 308.15 | 0.8976 | 0.0009 |
| 308.15 | 1.0000 | 0.0010 |
| 313.15 | 0.0000 | 0.0007 |
| 313.15 | 0.1000 | 0.0007 |
| 313.15 | 0.2000 | 0.0007 |
| 313.15 | 0.2999 | 0.0007 |
| 313.15 | 0.3996 | 0.0007 |
| 313.15 | 0.4999 | 0.0007 |
| 313.15 | 0.5965 | 0.0008 |
| 313.15 | 0.6992 | 0.0008 |
| 313.15 | 0.8004 | 0.0008 |
| 313.15 | 0.8976 | 0.0009 |
| 313.15 | 1.0000 | 0.0009 |
| 318.15 | 0.0000 | 0.0006 |
| 318.15 | 0.1000 | 0.0007 |
| 318.15 | 0.2000 | 0.0007 |
| 318.15 | 0.2999 | 0.0007 |
| 318.15 | 0.3996 | 0.0007 |
| 318.15 | 0.4999 | 0.0007 |
| 318.15 | 0.5965 | 0.0007 |
| 318.15 | 0.6992 | 0.0007 |
| 318.15 | 0.8004 | 0.0008 |
| 318.15 | 0.8976 | 0.0008 |
| 318.15 | 1.0000 | 0.0008 |
| 323.15 | 0.0000 | 0.0006 |
| 323.15 | 0.1000 | 0.0006 |
| 323.15 | 0.2000 | 0.0006 |
| 323.15 | 0.2999 | 0.0006 |
| 323.15 | 0.3996 | 0.0006 |
| 323.15 | 0.4999 | 0.0007 |
| 323.15 | 0.5965 | 0.0007 |
| 323.15 | 0.6992 | 0.0007 |
| 323.15 | 0.8004 | 0.0007 |
| 323.15 | 0.8976 | 0.0008 |
| 323.15 | 1.0000 | 0.0008 |
| 328.15 | 0.0000 | 0.0006 |
| 328.15 | 0.1000 | 0.0006 |
| 328.15 | 0.2000 | 0.0006 |
| 328.15 | 0.2999 | 0.0006 |
| 328.15 | 0.3996 | 0.0006 |
| 328.15 | 0.4999 | 0.0006 |
| 328.15 | 0.5965 | 0.0006 |
| 328.15 | 0.6992 | 0.0007 |
| 328.15 | 0.8004 | 0.0007 |
| 328.15 | 0.8976 | 0.0007 |
| 328.15 | 1.0000 | 0.0007 |
| 333.15 | 0.0000 | 0.0005 |
| 333.15 | 0.1000 | 0.0006 |
| 333.15 | 0.2000 | 0.0006 |
| 333.15 | 0.2999 | 0.0006 |
| 333.15 | 0.3996 | 0.0006 |
| 333.15 | 0.4999 | 0.0006 |
| 333.15 | 0.5965 | 0.0006 |
| 333.15 | 0.6992 | 0.0006 |
| 333.15 | 0.8004 | 0.0006 |
| 333.15 | 0.8976 | 0.0007 |
| 333.15 | 1.0000 | 0.0007 |
| 338.15 | 0.0000 | 0.0005 |
| 338.15 | 0.1000 | 0.0005 |
| 338.15 | 0.2000 | 0.0005 |
| 338.15 | 0.2999 | 0.0005 |
| 338.15 | 0.3996 | 0.0006 |
| 338.15 | 0.4999 | 0.0006 |
| 338.15 | 0.5965 | 0.0006 |
| 338.15 | 0.6992 | 0.0006 |
| 338.15 | 0.8004 | 0.0006 |
| 338.15 | 0.8976 | 0.0006 |
| 338.15 | 1.0000 | 0.0007 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetic acid (2) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0009 |
| 293.15 | 0.1000 | 0.0009 |
| 293.15 | 0.2000 | 0.0009 |
| 293.15 | 0.2999 | 0.0009 |
| 293.15 | 0.3996 | 0.0010 |
| 293.15 | 0.4999 | 0.0010 |
| 293.15 | 0.5965 | 0.0010 |
| 293.15 | 0.6992 | 0.0010 |
| 293.15 | 0.8004 | 0.0011 |
| 293.15 | 0.8976 | 0.0011 |
| 293.15 | 1.0000 | 0.0012 |
| 298.15 | 0.0000 | 0.0008 |
| 298.15 | 0.1000 | 0.0008 |
| 298.15 | 0.2000 | 0.0009 |
| 298.15 | 0.2999 | 0.0009 |
| 298.15 | 0.3996 | 0.0009 |
| 298.15 | 0.4999 | 0.0009 |
| 298.15 | 0.5965 | 0.0009 |
| 298.15 | 0.6992 | 0.0010 |
| 298.15 | 0.8004 | 0.0010 |
| 298.15 | 0.8976 | 0.0011 |
| 298.15 | 1.0000 | 0.0011 |
| 303.15 | 0.0000 | 0.0008 |
| 303.15 | 0.1000 | 0.0008 |
| 303.15 | 0.2000 | 0.0008 |
| 303.15 | 0.2999 | 0.0008 |
| 303.15 | 0.3996 | 0.0008 |
| 303.15 | 0.4999 | 0.0008 |
| 303.15 | 0.5965 | 0.0009 |
| 303.15 | 0.6992 | 0.0009 |
| 303.15 | 0.8004 | 0.0009 |
| 303.15 | 0.8976 | 0.0010 |
| 303.15 | 1.0000 | 0.0010 |
| 308.15 | 0.0000 | 0.0007 |
| 308.15 | 0.1000 | 0.0007 |
| 308.15 | 0.2000 | 0.0008 |
| 308.15 | 0.2999 | 0.0008 |
| 308.15 | 0.3996 | 0.0008 |
| 308.15 | 0.4999 | 0.0008 |
| 308.15 | 0.5965 | 0.0008 |
| 308.15 | 0.6992 | 0.0008 |
| 308.15 | 0.8004 | 0.0009 |
| 308.15 | 0.8976 | 0.0009 |
| 308.15 | 1.0000 | 0.0010 |
| 313.15 | 0.0000 | 0.0007 |
| 313.15 | 0.1000 | 0.0007 |
| 313.15 | 0.2000 | 0.0007 |
| 313.15 | 0.2999 | 0.0007 |
| 313.15 | 0.3996 | 0.0007 |
| 313.15 | 0.4999 | 0.0007 |
| 313.15 | 0.5965 | 0.0008 |
| 313.15 | 0.6992 | 0.0008 |
| 313.15 | 0.8004 | 0.0008 |
| 313.15 | 0.8976 | 0.0009 |
| 313.15 | 1.0000 | 0.0009 |
| 318.15 | 0.0000 | 0.0006 |
| 318.15 | 0.1000 | 0.0007 |
| 318.15 | 0.2000 | 0.0007 |
| 318.15 | 0.2999 | 0.0007 |
| 318.15 | 0.3996 | 0.0007 |
| 318.15 | 0.4999 | 0.0007 |
| 318.15 | 0.5965 | 0.0007 |
| 318.15 | 0.6992 | 0.0007 |
| 318.15 | 0.8004 | 0.0008 |
| 318.15 | 0.8976 | 0.0008 |
| 318.15 | 1.0000 | 0.0008 |
| 323.15 | 0.0000 | 0.0006 |
| 323.15 | 0.1000 | 0.0006 |
| 323.15 | 0.2000 | 0.0006 |
| 323.15 | 0.2999 | 0.0006 |
| 323.15 | 0.3996 | 0.0006 |
| 323.15 | 0.4999 | 0.0007 |
| 323.15 | 0.5965 | 0.0007 |
| 323.15 | 0.6992 | 0.0007 |
| 323.15 | 0.8004 | 0.0007 |
| 323.15 | 0.8976 | 0.0008 |
| 323.15 | 1.0000 | 0.0008 |
| 328.15 | 0.0000 | 0.0006 |
| 328.15 | 0.1000 | 0.0006 |
| 328.15 | 0.2000 | 0.0006 |
| 328.15 | 0.2999 | 0.0006 |
| 328.15 | 0.3996 | 0.0006 |
| 328.15 | 0.4999 | 0.0006 |
| 328.15 | 0.5965 | 0.0006 |
| 328.15 | 0.6992 | 0.0007 |
| 328.15 | 0.8004 | 0.0007 |
| 328.15 | 0.8976 | 0.0007 |
| 328.15 | 1.0000 | 0.0007 |
| 333.15 | 0.0000 | 0.0005 |
| 333.15 | 0.1000 | 0.0006 |
| 333.15 | 0.2000 | 0.0006 |
| 333.15 | 0.2999 | 0.0006 |
| 333.15 | 0.3996 | 0.0006 |
| 333.15 | 0.4999 | 0.0006 |
| 333.15 | 0.5965 | 0.0006 |
| 333.15 | 0.6992 | 0.0006 |
| 333.15 | 0.8004 | 0.0006 |
| 333.15 | 0.8976 | 0.0007 |
| 333.15 | 1.0000 | 0.0007 |
| 338.15 | 0.0000 | 0.0005 |
| 338.15 | 0.1000 | 0.0005 |
| 338.15 | 0.2000 | 0.0005 |
| 338.15 | 0.2999 | 0.0005 |
| 338.15 | 0.3996 | 0.0006 |
| 338.15 | 0.4999 | 0.0006 |
| 338.15 | 0.5965 | 0.0006 |
| 338.15 | 0.6992 | 0.0006 |
| 338.15 | 0.8004 | 0.0006 |
| 338.15 | 0.8976 | 0.0006 |
| 338.15 | 1.0000 | 0.0007 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mole fraction of Acetic anhydride (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0500 | 0.0450 |
| 0.1000 | 0.0890 |
| 0.1500 | 0.1340 |
| 0.2000 | 0.1770 |
| 0.2500 | 0.2170 |
| 0.3000 | 0.2540 |
| 0.3500 | 0.2880 |
| 0.4000 | 0.3170 |
| 0.4500 | 0.3400 |
| 0.5000 | 0.3560 |
| 0.5500 | 0.3660 |
| 0.6000 | 0.3680 |
| 0.6500 | 0.3610 |
| 0.7000 | 0.3440 |
| 0.7500 | 0.3170 |
| 0.8000 | 0.2800 |
| 0.8500 | 0.2300 |
| 0.9000 | 0.1680 |
| 0.9500 | 0.0920 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 100 (Liquid)
| Mole fraction of Acetic anhydride (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0500 | 0.0450 |
| 0.1000 | 0.0890 |
| 0.1500 | 0.1340 |
| 0.2000 | 0.1770 |
| 0.2500 | 0.2170 |
| 0.3000 | 0.2540 |
| 0.3500 | 0.2880 |
| 0.4000 | 0.3170 |
| 0.4500 | 0.3400 |
| 0.5000 | 0.3560 |
| 0.5500 | 0.3660 |
| 0.6000 | 0.3680 |
| 0.6500 | 0.3610 |
| 0.7000 | 0.3440 |
| 0.7500 | 0.3170 |
| 0.8000 | 0.2800 |
| 0.8500 | 0.2300 |
| 0.9000 | 0.1680 |
| 0.9500 | 0.0920 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetic acid (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 1080.89 |
| 293.15 | 0.1000 | 1079.28 |
| 293.15 | 0.2000 | 1077.19 |
| 293.15 | 0.2999 | 1074.93 |
| 293.15 | 0.3996 | 1072.42 |
| 293.15 | 0.4999 | 1069.56 |
| 293.15 | 0.5965 | 1066.68 |
| 293.15 | 0.6992 | 1063.1 |
| 293.15 | 0.8004 | 1059.19 |
| 293.15 | 0.8976 | 1054.94 |
| 293.15 | 1.0000 | 1049.42 |
| 298.15 | 0.0000 | 1074.8 |
| 298.15 | 0.1000 | 1073.24 |
| 298.15 | 0.2000 | 1071.18 |
| 298.15 | 0.2999 | 1068.96 |
| 298.15 | 0.3996 | 1066.47 |
| 298.15 | 0.4999 | 1063.66 |
| 298.15 | 0.5965 | 1060.8 |
| 298.15 | 0.6992 | 1057.27 |
| 298.15 | 0.8004 | 1053.41 |
| 298.15 | 0.8976 | 1049.21 |
| 298.15 | 1.0000 | 1043.76 |
| 303.15 | 0.0000 | 1068.7 |
| 303.15 | 0.1000 | 1067.18 |
| 303.15 | 0.2000 | 1065.17 |
| 303.15 | 0.2999 | 1062.98 |
| 303.15 | 0.3996 | 1060.53 |
| 303.15 | 0.4999 | 1057.75 |
| 303.15 | 0.5965 | 1054.93 |
| 303.15 | 0.6992 | 1051.45 |
| 303.15 | 0.8004 | 1047.64 |
| 303.15 | 0.8976 | 1043.48 |
| 303.15 | 1.0000 | 1038.1 |
| 308.15 | 0.0000 | 1062.61 |
| 308.15 | 0.1000 | 1061.12 |
| 308.15 | 0.2000 | 1059.15 |
| 308.15 | 0.2999 | 1057.0 |
| 308.15 | 0.3996 | 1054.57 |
| 308.15 | 0.4999 | 1051.83 |
| 308.15 | 0.5965 | 1049.05 |
| 308.15 | 0.6992 | 1045.62 |
| 308.15 | 0.8004 | 1041.85 |
| 308.15 | 0.8976 | 1037.75 |
| 308.15 | 1.0000 | 1032.44 |
| 313.15 | 0.0000 | 1056.49 |
| 313.15 | 0.1000 | 1055.06 |
| 313.15 | 0.2000 | 1053.12 |
| 313.15 | 0.2999 | 1051.0 |
| 313.15 | 0.3996 | 1048.6 |
| 313.15 | 0.4999 | 1045.9 |
| 313.15 | 0.5965 | 1043.16 |
| 313.15 | 0.6992 | 1039.78 |
| 313.15 | 0.8004 | 1036.06 |
| 313.15 | 0.8976 | 1032.01 |
| 313.15 | 1.0000 | 1026.77 |
| 318.15 | 0.0000 | 1050.38 |
| 318.15 | 0.1000 | 1048.96 |
| 318.15 | 0.2000 | 1047.07 |
| 318.15 | 0.2999 | 1044.99 |
| 318.15 | 0.3996 | 1042.62 |
| 318.15 | 0.4999 | 1039.96 |
| 318.15 | 0.5965 | 1037.26 |
| 318.15 | 0.6992 | 1033.93 |
| 318.15 | 0.8004 | 1030.27 |
| 318.15 | 0.8976 | 1026.28 |
| 318.15 | 1.0000 | 1021.11 |
| 323.15 | 0.0000 | 1044.24 |
| 323.15 | 0.1000 | 1042.87 |
| 323.15 | 0.2000 | 1041.01 |
| 323.15 | 0.2999 | 1038.96 |
| 323.15 | 0.3996 | 1036.63 |
| 323.15 | 0.4999 | 1034.01 |
| 323.15 | 0.5965 | 1031.34 |
| 323.15 | 0.6992 | 1028.06 |
| 323.15 | 0.8004 | 1024.46 |
| 323.15 | 0.8976 | 1020.54 |
| 323.15 | 1.0000 | 1015.44 |
| 328.15 | 0.0000 | 1038.07 |
| 328.15 | 0.1000 | 1036.74 |
| 328.15 | 0.2000 | 1034.94 |
| 328.15 | 0.2999 | 1032.91 |
| 328.15 | 0.3996 | 1030.61 |
| 328.15 | 0.4999 | 1028.04 |
| 328.15 | 0.5965 | 1025.39 |
| 328.15 | 0.6992 | 1022.18 |
| 328.15 | 0.8004 | 1018.64 |
| 328.15 | 0.8976 | 1014.79 |
| 328.15 | 1.0000 | 1009.77 |
| 333.15 | 0.0000 | 1031.9 |
| 333.15 | 0.1000 | 1030.63 |
| 333.15 | 0.2000 | 1028.83 |
| 333.15 | 0.2999 | 1026.84 |
| 333.15 | 0.3996 | 1024.57 |
| 333.15 | 0.4999 | 1022.05 |
| 333.15 | 0.5965 | 1019.44 |
| 333.15 | 0.6992 | 1016.3 |
| 333.15 | 0.8004 | 1012.82 |
| 333.15 | 0.8976 | 1009.03 |
| 333.15 | 1.0000 | 1004.09 |
| 338.15 | 0.0000 | 1025.7 |
| 338.15 | 0.1000 | 1024.48 |
| 338.15 | 0.2000 | 1022.71 |
| 338.15 | 0.2999 | 1020.75 |
| 338.15 | 0.3996 | 1018.52 |
| 338.15 | 0.4999 | 1016.04 |
| 338.15 | 0.5965 | 1013.48 |
| 338.15 | 0.6992 | 1010.39 |
| 338.15 | 0.8004 | 1006.97 |
| 338.15 | 0.8976 | 1003.24 |
| 338.15 | 1.0000 | 998.38 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetic acid (2) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 1080.89 |
| 293.15 | 0.1000 | 1079.28 |
| 293.15 | 0.2000 | 1077.19 |
| 293.15 | 0.2999 | 1074.93 |
| 293.15 | 0.3996 | 1072.42 |
| 293.15 | 0.4999 | 1069.56 |
| 293.15 | 0.5965 | 1066.68 |
| 293.15 | 0.6992 | 1063.1 |
| 293.15 | 0.8004 | 1059.19 |
| 293.15 | 0.8976 | 1054.94 |
| 293.15 | 1.0000 | 1049.42 |
| 298.15 | 0.0000 | 1074.8 |
| 298.15 | 0.1000 | 1073.24 |
| 298.15 | 0.2000 | 1071.18 |
| 298.15 | 0.2999 | 1068.96 |
| 298.15 | 0.3996 | 1066.47 |
| 298.15 | 0.4999 | 1063.66 |
| 298.15 | 0.5965 | 1060.8 |
| 298.15 | 0.6992 | 1057.27 |
| 298.15 | 0.8004 | 1053.41 |
| 298.15 | 0.8976 | 1049.21 |
| 298.15 | 1.0000 | 1043.76 |
| 303.15 | 0.0000 | 1068.7 |
| 303.15 | 0.1000 | 1067.18 |
| 303.15 | 0.2000 | 1065.17 |
| 303.15 | 0.2999 | 1062.98 |
| 303.15 | 0.3996 | 1060.53 |
| 303.15 | 0.4999 | 1057.75 |
| 303.15 | 0.5965 | 1054.93 |
| 303.15 | 0.6992 | 1051.45 |
| 303.15 | 0.8004 | 1047.64 |
| 303.15 | 0.8976 | 1043.48 |
| 303.15 | 1.0000 | 1038.1 |
| 308.15 | 0.0000 | 1062.61 |
| 308.15 | 0.1000 | 1061.12 |
| 308.15 | 0.2000 | 1059.15 |
| 308.15 | 0.2999 | 1057.0 |
| 308.15 | 0.3996 | 1054.57 |
| 308.15 | 0.4999 | 1051.83 |
| 308.15 | 0.5965 | 1049.05 |
| 308.15 | 0.6992 | 1045.62 |
| 308.15 | 0.8004 | 1041.85 |
| 308.15 | 0.8976 | 1037.75 |
| 308.15 | 1.0000 | 1032.44 |
| 313.15 | 0.0000 | 1056.49 |
| 313.15 | 0.1000 | 1055.06 |
| 313.15 | 0.2000 | 1053.12 |
| 313.15 | 0.2999 | 1051.0 |
| 313.15 | 0.3996 | 1048.6 |
| 313.15 | 0.4999 | 1045.9 |
| 313.15 | 0.5965 | 1043.16 |
| 313.15 | 0.6992 | 1039.78 |
| 313.15 | 0.8004 | 1036.06 |
| 313.15 | 0.8976 | 1032.01 |
| 313.15 | 1.0000 | 1026.77 |
| 318.15 | 0.0000 | 1050.38 |
| 318.15 | 0.1000 | 1048.96 |
| 318.15 | 0.2000 | 1047.07 |
| 318.15 | 0.2999 | 1044.99 |
| 318.15 | 0.3996 | 1042.62 |
| 318.15 | 0.4999 | 1039.96 |
| 318.15 | 0.5965 | 1037.26 |
| 318.15 | 0.6992 | 1033.93 |
| 318.15 | 0.8004 | 1030.27 |
| 318.15 | 0.8976 | 1026.28 |
| 318.15 | 1.0000 | 1021.11 |
| 323.15 | 0.0000 | 1044.24 |
| 323.15 | 0.1000 | 1042.87 |
| 323.15 | 0.2000 | 1041.01 |
| 323.15 | 0.2999 | 1038.96 |
| 323.15 | 0.3996 | 1036.63 |
| 323.15 | 0.4999 | 1034.01 |
| 323.15 | 0.5965 | 1031.34 |
| 323.15 | 0.6992 | 1028.06 |
| 323.15 | 0.8004 | 1024.46 |
| 323.15 | 0.8976 | 1020.54 |
| 323.15 | 1.0000 | 1015.44 |
| 328.15 | 0.0000 | 1038.07 |
| 328.15 | 0.1000 | 1036.74 |
| 328.15 | 0.2000 | 1034.94 |
| 328.15 | 0.2999 | 1032.91 |
| 328.15 | 0.3996 | 1030.61 |
| 328.15 | 0.4999 | 1028.04 |
| 328.15 | 0.5965 | 1025.39 |
| 328.15 | 0.6992 | 1022.18 |
| 328.15 | 0.8004 | 1018.64 |
| 328.15 | 0.8976 | 1014.79 |
| 328.15 | 1.0000 | 1009.77 |
| 333.15 | 0.0000 | 1031.9 |
| 333.15 | 0.1000 | 1030.63 |
| 333.15 | 0.2000 | 1028.83 |
| 333.15 | 0.2999 | 1026.84 |
| 333.15 | 0.3996 | 1024.57 |
| 333.15 | 0.4999 | 1022.05 |
| 333.15 | 0.5965 | 1019.44 |
| 333.15 | 0.6992 | 1016.3 |
| 333.15 | 0.8004 | 1012.82 |
| 333.15 | 0.8976 | 1009.03 |
| 333.15 | 1.0000 | 1004.09 |
| 338.15 | 0.0000 | 1025.7 |
| 338.15 | 0.1000 | 1024.48 |
| 338.15 | 0.2000 | 1022.71 |
| 338.15 | 0.2999 | 1020.75 |
| 338.15 | 0.3996 | 1018.52 |
| 338.15 | 0.4999 | 1016.04 |
| 338.15 | 0.5965 | 1013.48 |
| 338.15 | 0.6992 | 1010.39 |
| 338.15 | 0.8004 | 1006.97 |
| 338.15 | 0.8976 | 1003.24 |
| 338.15 | 1.0000 | 998.38 |
Sources
- Evaluation of Excess Molar Enthalpies for a Quaternary Mixture System of Acetic Anhydride, Ethanol, Acetic Acid, and Ethyl Acetate
- Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
- Heat Capacities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures