Mixture of Diisopropyl ether + Heptane

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Diisopropyl ether

Name
Diisopropyl ether
InChI
InChI=1S/C6H14O/c1-5(2)7-6(3)4/h5-6H,1-4H3
InChI Key
ZAFNJMIOTHYJRJ-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CC(C)OC(C)C
Mol. Weight (g/mol)
102.17
CAS
108-20-3

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. Excess molar enthalpy (molar enthalpy (4)
  3. ν - Kinematic viscosity, m2/s (2)
  4. csound,fluid - Speed of Sound, m/s (2)
  5. Excess molar volume, m3/mol (2)

Viscosity, Pa*s [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Viscosity, Pa*s - Liquid
0.0000 0.0004
0.1462 0.0004
0.2667 0.0004
0.4165 0.0004
0.4774 0.0004
0.5331 0.0004
0.6068 0.0004
0.7371 0.0003
0.8642 0.0003
1.0000 0.0003

Viscosity, Pa*s [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Viscosity, Pa*s - Liquid
0.0000 0.0004
0.1462 0.0004
0.2667 0.0004
0.4165 0.0004
0.4774 0.0004
0.5331 0.0004
0.6068 0.0004
0.7371 0.0003
0.8642 0.0003
1.0000 0.0003

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Fixed Measured
Mole fraction of Heptane (2) - Liquid Pressure, kPa - Liquid Temperature, K - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.5000 101.00 303.15 0.2564

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Heptane (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0890 0.0844
0.1670 0.1443
0.2480 0.1922
0.3040 0.2187
0.3900 0.2456
0.4970 0.2559
0.5840 0.2486
0.6940 0.2173
0.7790 0.1753
0.8650 0.1200
0.9110 0.0837

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Fixed Measured
Mole fraction of Heptane (2) - Liquid Pressure, kPa - Liquid Temperature, K - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.5000 101.00 303.15 0.2564

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Heptane (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0890 0.0844
0.1670 0.1443
0.2480 0.1922
0.3040 0.2187
0.3900 0.2456
0.4970 0.2559
0.5840 0.2486
0.6940 0.2173
0.7790 0.1753
0.8650 0.1200
0.9110 0.0837

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0000 6.6970e-07
283.15 0.0508 6.5780e-07
283.15 0.1002 6.4730e-07
283.15 0.1986 6.2650e-07
283.15 0.2973 6.0680e-07
283.15 0.3992 5.8800e-07
283.15 0.4991 5.6930e-07
283.15 0.5979 5.5330e-07
283.15 0.7009 5.3720e-07
283.15 0.8008 5.2150e-07
283.15 0.8954 5.0910e-07
283.15 0.9500 5.0160e-07
298.15 0.0000 5.7540e-07
298.15 0.0508 5.6580e-07
298.15 0.1002 5.5670e-07
298.15 0.1986 5.3870e-07
298.15 0.2973 5.2180e-07
298.15 0.3992 5.0550e-07
298.15 0.4991 4.9000e-07
298.15 0.5979 4.7790e-07
298.15 0.7009 4.6790e-07
298.15 0.8008 4.5880e-07
298.15 0.8954 4.4960e-07
298.15 0.9500 4.4430e-07
313.15 0.0000 4.9860e-07
313.15 0.0508 4.9100e-07
313.15 0.1002 4.8310e-07
313.15 0.1986 4.7190e-07
313.15 0.2973 4.6100e-07
313.15 0.3992 4.4980e-07
313.15 0.4991 4.3850e-07
313.15 0.5979 4.2730e-07
313.15 0.7009 4.1660e-07
313.15 0.8008 4.0580e-07
313.15 0.8954 3.9600e-07
313.15 0.9500 3.9090e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0000 6.6970e-07
283.15 0.0508 6.5780e-07
283.15 0.1002 6.4730e-07
283.15 0.1986 6.2650e-07
283.15 0.2973 6.0680e-07
283.15 0.3992 5.8800e-07
283.15 0.4991 5.6930e-07
283.15 0.5979 5.5330e-07
283.15 0.7009 5.3720e-07
283.15 0.8008 5.2150e-07
283.15 0.8954 5.0910e-07
283.15 0.9500 5.0160e-07
298.15 0.0000 5.7540e-07
298.15 0.0508 5.6580e-07
298.15 0.1002 5.5670e-07
298.15 0.1986 5.3870e-07
298.15 0.2973 5.2180e-07
298.15 0.3992 5.0550e-07
298.15 0.4991 4.9000e-07
298.15 0.5979 4.7790e-07
298.15 0.7009 4.6790e-07
298.15 0.8008 4.5880e-07
298.15 0.8954 4.4960e-07
298.15 0.9500 4.4430e-07
313.15 0.0000 4.9860e-07
313.15 0.0508 4.9100e-07
313.15 0.1002 4.8310e-07
313.15 0.1986 4.7190e-07
313.15 0.2973 4.6100e-07
313.15 0.3992 4.4980e-07
313.15 0.4991 4.3850e-07
313.15 0.5979 4.2730e-07
313.15 0.7009 4.1660e-07
313.15 0.8008 4.0580e-07
313.15 0.8954 3.9600e-07
313.15 0.9500 3.9090e-07

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Speed of sound, m/s - Liquid
0.0000 1110.5
0.1462 1090.7
0.2667 1072.8
0.4165 1050.6
0.4774 1041.8
0.5331 1033.9
0.6068 1023.9
0.7371 1006.9
0.8642 991.3
1.0000 974.9

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Speed of sound, m/s - Liquid
0.0000 1110.5
0.1462 1090.7
0.2667 1072.8
0.4165 1050.6
0.4774 1041.8
0.5331 1033.9
0.6068 1023.9
0.7371 1006.9
0.8642 991.3
1.0000 974.9

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar volume, m3/mol - Liquid
0.1462 1.6700e-07
0.2667 2.4500e-07
0.4165 3.1600e-07
0.4774 3.2400e-07
0.5331 3.2700e-07
0.6068 3.0100e-07
0.7371 2.6100e-07
0.8642 1.7300e-07

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar volume, m3/mol - Liquid
0.1462 1.6700e-07
0.2667 2.4500e-07
0.4165 3.1600e-07
0.4774 3.2400e-07
0.5331 3.2700e-07
0.6068 3.0100e-07
0.7371 2.6100e-07
0.8642 1.7300e-07

Sources