Mixture of Propane, 2-methoxy-2-methyl- + Pentane, 3-methyl-

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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

Pentane, 3-methyl-

Name
Pentane, 3-methyl-
InChI
InChI=1S/C6H14/c1-4-6(3)5-2/h6H,4-5H2,1-3H3
InChI Key
PFEOZHBOMNWTJB-UHFFFAOYSA-N
Formula
C6H14
SMILES
CCC(C)CC
Mol. Weight (g/mol)
86.18
CAS
96-14-0
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. ν - Kinematic viscosity, m2/s (2)

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

Operational conditions:

Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0499 0.0572
0.0999 0.1084
0.1501 0.1597
0.2000 0.2016
0.2495 0.2338
0.3004 0.2632
0.3502 0.2857
0.3999 0.3014
0.4505 0.3115
0.4997 0.3145
0.5500 0.3100
0.5996 0.3001
0.6502 0.2861
0.7003 0.2638
0.7500 0.2347
0.7999 0.1991
0.8501 0.1577
0.8999 0.1099
0.9500 0.0537

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

Operational conditions:

Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0499 0.0572
0.0999 0.1084
0.1501 0.1597
0.2000 0.2016
0.2495 0.2338
0.3004 0.2632
0.3502 0.2857
0.3999 0.3014
0.4505 0.3115
0.4997 0.3145
0.5500 0.3100
0.5996 0.3001
0.6502 0.2861
0.7003 0.2638
0.7500 0.2347
0.7999 0.1991
0.8501 0.1577
0.8999 0.1099
0.9500 0.0537

Kinematic viscosity, m2/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0480 4.9150e-07
283.15 0.0967 4.9060e-07
283.15 0.1961 4.8930e-07
283.15 0.2982 4.8950e-07
283.15 0.3995 4.9060e-07
283.15 0.4983 4.9230e-07
283.15 0.5992 4.9540e-07
283.15 0.6984 4.9950e-07
283.15 0.7978 5.0480e-07
283.15 0.8996 5.1130e-07
283.15 0.9491 5.1450e-07
283.15 1.0000 5.1910e-07
298.15 0.0480 4.3610e-07
298.15 0.0967 4.3570e-07
298.15 0.1961 4.3480e-07
298.15 0.2982 4.3470e-07
298.15 0.3995 4.3510e-07
298.15 0.4983 4.3610e-07
298.15 0.5992 4.3790e-07
298.15 0.6984 4.4060e-07
298.15 0.7978 4.4350e-07
298.15 0.8996 4.4780e-07
298.15 0.9491 4.5020e-07
298.15 1.0000 4.5290e-07
313.15 0.0480 3.8700e-07
313.15 0.0967 3.8590e-07
313.15 0.1961 3.8430e-07
313.15 0.2982 3.8360e-07
313.15 0.3995 3.8340e-07
313.15 0.4983 3.8360e-07
313.15 0.5992 3.8500e-07
313.15 0.6984 3.8630e-07
313.15 0.7978 3.8880e-07
313.15 0.8996 3.9180e-07
313.15 0.9491 3.9370e-07
313.15 1.0000 3.9610e-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- (1) - Liquid Kinematic viscosity, m2/s - Liquid
283.15 0.0480 4.9150e-07
283.15 0.0967 4.9060e-07
283.15 0.1961 4.8930e-07
283.15 0.2982 4.8950e-07
283.15 0.3995 4.9060e-07
283.15 0.4983 4.9230e-07
283.15 0.5992 4.9540e-07
283.15 0.6984 4.9950e-07
283.15 0.7978 5.0480e-07
283.15 0.8996 5.1130e-07
283.15 0.9491 5.1450e-07
283.15 1.0000 5.1910e-07
298.15 0.0480 4.3610e-07
298.15 0.0967 4.3570e-07
298.15 0.1961 4.3480e-07
298.15 0.2982 4.3470e-07
298.15 0.3995 4.3510e-07
298.15 0.4983 4.3610e-07
298.15 0.5992 4.3790e-07
298.15 0.6984 4.4060e-07
298.15 0.7978 4.4350e-07
298.15 0.8996 4.4780e-07
298.15 0.9491 4.5020e-07
298.15 1.0000 4.5290e-07
313.15 0.0480 3.8700e-07
313.15 0.0967 3.8590e-07
313.15 0.1961 3.8430e-07
313.15 0.2982 3.8360e-07
313.15 0.3995 3.8340e-07
313.15 0.4983 3.8360e-07
313.15 0.5992 3.8500e-07
313.15 0.6984 3.8630e-07
313.15 0.7978 3.8880e-07
313.15 0.8996 3.9180e-07
313.15 0.9491 3.9370e-07
313.15 1.0000 3.9610e-07

Sources