Mixture of n-Hexane + Propane, 2-methoxy-2-methyl-

Excel

n-Hexane

Name
n-Hexane
InChI
InChI=1S/C6H14/c1-3-5-6-4-2/h3-6H2,1-2H3
InChI Key
VLKZOEOYAKHREP-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCCCCC
Mol. Weight (g/mol)
86.18
CAS
110-54-3

Propane, 2-methoxy-2-methyl-

Name
Propane, 2-methoxy-2-methyl-
InChI
InChI=1S/C5H12O/c1-5(2,3)6-4/h1-4H3
InChI Key
BZLVMXJERCGZMT-UHFFFAOYSA-N
Formula
C5H12O
SMILES
COC(C)(C)C
Mol. Weight (g/mol)
88.15
CAS
1634-04-4
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. ν - Kinematic viscosity, m2/s (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)

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

Operational conditions:

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000 0.0000
0.0504 0.0718
0.1002 0.1334
0.1497 0.1883
0.2008 0.2372
0.2491 0.2755
0.2994 0.3090
0.3486 0.3368
0.4002 0.3581
0.4484 0.3695
0.4997 0.3741
0.5493 0.3703
0.6006 0.3590
0.6496 0.3412
0.7001 0.3133
0.7500 0.2808
0.7992 0.2380
0.8501 0.1893
0.9007 0.1321
0.9506 0.0706
1.0000 0.0000

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

Operational conditions:

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000 0.0000
0.0504 0.0718
0.1002 0.1334
0.1497 0.1883
0.2008 0.2372
0.2491 0.2755
0.2994 0.3090
0.3486 0.3368
0.4002 0.3581
0.4484 0.3695
0.4997 0.3741
0.5493 0.3703
0.6006 0.3590
0.6496 0.3412
0.7001 0.3133
0.7500 0.2808
0.7992 0.2380
0.8501 0.1893
0.9007 0.1321
0.9506 0.0706
1.0000 0.0000

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0479 5.0970e-07
283.15 0.0974 5.0740e-07
283.15 0.1983 5.0340e-07
283.15 0.2988 5.0040e-07
283.15 0.3979 4.9900e-07
283.15 0.4975 4.9900e-07
283.15 0.5974 4.9960e-07
283.15 0.6968 5.0250e-07
283.15 0.7911 5.0590e-07
283.15 0.8976 5.1250e-07
283.15 0.9486 5.1470e-07
298.15 0.0479 4.4780e-07
298.15 0.0974 4.4650e-07
298.15 0.1983 4.4420e-07
298.15 0.2988 4.4270e-07
298.15 0.3979 4.4180e-07
298.15 0.4975 4.4130e-07
298.15 0.5974 4.4190e-07
298.15 0.6968 4.4310e-07
298.15 0.7911 4.4500e-07
298.15 0.8976 4.4840e-07
298.15 0.9486 4.5050e-07
313.15 0.0479 4.0170e-07
313.15 0.0974 3.9940e-07
313.15 0.1983 3.9600e-07
313.15 0.2988 3.9320e-07
313.15 0.3979 3.9100e-07
313.15 0.4975 3.8970e-07
313.15 0.5974 3.8950e-07
313.15 0.6968 3.8950e-07
313.15 0.7911 3.9130e-07
313.15 0.8976 3.9260e-07
313.15 0.9486 3.9400e-07

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0479 5.0970e-07
283.15 0.0974 5.0740e-07
283.15 0.1983 5.0340e-07
283.15 0.2988 5.0040e-07
283.15 0.3979 4.9900e-07
283.15 0.4975 4.9900e-07
283.15 0.5974 4.9960e-07
283.15 0.6968 5.0250e-07
283.15 0.7911 5.0590e-07
283.15 0.8976 5.1250e-07
283.15 0.9486 5.1470e-07
298.15 0.0479 4.4780e-07
298.15 0.0974 4.4650e-07
298.15 0.1983 4.4420e-07
298.15 0.2988 4.4270e-07
298.15 0.3979 4.4180e-07
298.15 0.4975 4.4130e-07
298.15 0.5974 4.4190e-07
298.15 0.6968 4.4310e-07
298.15 0.7911 4.4500e-07
298.15 0.8976 4.4840e-07
298.15 0.9486 4.5050e-07
313.15 0.0479 4.0170e-07
313.15 0.0974 3.9940e-07
313.15 0.1983 3.9600e-07
313.15 0.2988 3.9320e-07
313.15 0.3979 3.9100e-07
313.15 0.4975 3.8970e-07
313.15 0.5974 3.8950e-07
313.15 0.6968 3.8950e-07
313.15 0.7911 3.9130e-07
313.15 0.8976 3.9260e-07
313.15 0.9486 3.9400e-07

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.2947 46.48
0.6971 55.28

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Propane, 2-methoxy-2-methyl- (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.2947 46.48
0.6971 55.28

Sources