Mixture of Pentane, 1-propoxy- + Acetonitrile

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Pentane, 1-propoxy-

Name
Pentane, 1-propoxy-
InChI
InChI=1S/C8H18O/c1-3-5-6-8-9-7-4-2/h3-8H2,1-2H3
InChI Key
DMUSSSYUUUYJRM-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCCOCCC
Mol. Weight (g/mol)
130.23
CAS
18641-82-2

Acetonitrile

Name
Acetonitrile
InChI
InChI=1S/C2H3N/c1-2-3/h1H3
InChI Key
WEVYAHXRMPXWCK-UHFFFAOYSA-N
Formula
C2H3N
SMILES
CC#N
Mol. Weight (g/mol)
41.05
CAS
75-05-8
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Liquid-liquid equilibrium temperature, K (2)

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetonitrile (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0310 0.1717
298.15 0.0602 0.3244
298.15 0.0876 0.4509
298.15 0.1135 0.5585
298.15 0.1379 0.6498
298.15 0.1830 0.7996
298.15 0.2236 0.9145
298.15 0.2604 1.0027
298.15 0.2938 1.0729
298.15 0.3243 1.1277
298.15 0.3781 1.2034
298.15 0.4240 1.2471
298.15 0.4635 1.2718
298.15 0.5061 1.2833
298.15 0.5424 1.2821
298.15 0.5738 1.2726
298.15 0.6011 1.2581
298.15 0.6296 1.2365
298.15 0.6542 1.2123
298.15 0.6758 1.1864
298.15 0.6979 1.1559
298.15 0.7171 1.1254
298.15 0.7340 1.0959
298.15 0.7491 1.0666
298.15 0.7625 1.0387
298.15 0.7644 1.012
298.15 0.7829 0.9712
298.15 0.8022 0.9231
298.15 0.8226 0.8669
298.15 0.8440 0.8000
298.15 0.8666 0.7215
298.15 0.8807 0.6666
298.15 0.8953 0.6057
298.15 0.9104 0.5373
298.15 0.9260 0.4601
298.15 0.9421 0.3725
298.15 0.9531 0.3098
298.15 0.9644 0.2413
298.15 0.9760 0.1671
298.15 0.9879 0.0866
308.15 0.0305 0.1786
308.15 0.0592 0.3344
308.15 0.0863 0.4648
308.15 0.1118 0.5747
308.15 0.1360 0.6699
308.15 0.1806 0.8235
308.15 0.2208 0.9417
308.15 0.2572 1.0341
308.15 0.2904 1.107
308.15 0.3207 1.164
308.15 0.3742 1.2442
308.15 0.4199 1.2923
308.15 0.4594 1.3198
308.15 0.5020 1.3327
308.15 0.5383 1.3335
308.15 0.5697 1.3248
308.15 0.6022 1.3072
308.15 0.6301 1.2848
308.15 0.6543 1.2594
308.15 0.6756 1.2328
308.15 0.6944 1.2056
308.15 0.7137 1.1739
308.15 0.7173 1.1562
308.15 0.7308 1.1426
308.15 0.7382 1.1174
308.15 0.7459 1.112
308.15 0.7595 1.0824
308.15 0.7603 1.0707
308.15 0.7838 1.0141
308.15 0.8089 0.9455
308.15 0.8355 0.8619
308.15 0.8524 0.8027
308.15 0.8699 0.7352
308.15 0.8882 0.6586
308.15 0.9072 0.5704
308.15 0.9271 0.4687
308.15 0.9409 0.3924
308.15 0.9695 0.2154
308.15 0.9845 0.1129
308.15 0.9550 0.3082

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Acetonitrile (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0310 0.1717
298.15 0.0602 0.3244
298.15 0.0876 0.4509
298.15 0.1135 0.5585
298.15 0.1379 0.6498
298.15 0.1830 0.7996
298.15 0.2236 0.9145
298.15 0.2604 1.0027
298.15 0.2938 1.0729
298.15 0.3243 1.1277
298.15 0.3781 1.2034
298.15 0.4240 1.2471
298.15 0.4635 1.2718
298.15 0.5061 1.2833
298.15 0.5424 1.2821
298.15 0.5738 1.2726
298.15 0.6011 1.2581
298.15 0.6296 1.2365
298.15 0.6542 1.2123
298.15 0.6758 1.1864
298.15 0.6979 1.1559
298.15 0.7171 1.1254
298.15 0.7340 1.0959
298.15 0.7491 1.0666
298.15 0.7625 1.0387
298.15 0.7644 1.012
298.15 0.7829 0.9712
298.15 0.8022 0.9231
298.15 0.8226 0.8669
298.15 0.8440 0.8000
298.15 0.8666 0.7215
298.15 0.8807 0.6666
298.15 0.8953 0.6057
298.15 0.9104 0.5373
298.15 0.9260 0.4601
298.15 0.9421 0.3725
298.15 0.9531 0.3098
298.15 0.9644 0.2413
298.15 0.9760 0.1671
298.15 0.9879 0.0866
308.15 0.0305 0.1786
308.15 0.0592 0.3344
308.15 0.0863 0.4648
308.15 0.1118 0.5747
308.15 0.1360 0.6699
308.15 0.1806 0.8235
308.15 0.2208 0.9417
308.15 0.2572 1.0341
308.15 0.2904 1.107
308.15 0.3207 1.164
308.15 0.3742 1.2442
308.15 0.4199 1.2923
308.15 0.4594 1.3198
308.15 0.5020 1.3327
308.15 0.5383 1.3335
308.15 0.5697 1.3248
308.15 0.6022 1.3072
308.15 0.6301 1.2848
308.15 0.6543 1.2594
308.15 0.6756 1.2328
308.15 0.6944 1.2056
308.15 0.7137 1.1739
308.15 0.7173 1.1562
308.15 0.7308 1.1426
308.15 0.7382 1.1174
308.15 0.7459 1.112
308.15 0.7595 1.0824
308.15 0.7603 1.0707
308.15 0.7838 1.0141
308.15 0.8089 0.9455
308.15 0.8355 0.8619
308.15 0.8524 0.8027
308.15 0.8699 0.7352
308.15 0.8882 0.6586
308.15 0.9072 0.5704
308.15 0.9271 0.4687
308.15 0.9409 0.3924
308.15 0.9695 0.2154
308.15 0.9845 0.1129
308.15 0.9550 0.3082

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Mole fraction of Acetonitrile (2) - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.3031 251.65
0.3237 254.32
0.3470 257.41
0.3639 259.33
0.3928 261.81
0.4243 264.21
0.4605 266.55
0.4967 268.27
0.5319 269.71
0.5649 270.09
0.5672 270.43
0.6086 270.94
0.6450 271.28
0.6820 271.46
0.7180 271.51
0.7540 271.37
0.7908 270.58
0.8256 268.72
0.8506 266.23
0.8692 263.38
0.8882 259.70
0.8987 257.09
0.9084 253.75
0.9165 250.68
0.9282 245.33

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Mole fraction of Acetonitrile (2) - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.3031 251.65
0.3237 254.32
0.3470 257.41
0.3639 259.33
0.3928 261.81
0.4243 264.21
0.4605 266.55
0.4967 268.27
0.5319 269.71
0.5649 270.09
0.5672 270.43
0.6086 270.94
0.6450 271.28
0.6820 271.46
0.7180 271.51
0.7540 271.37
0.7908 270.58
0.8256 268.72
0.8506 266.23
0.8692 263.38
0.8882 259.70
0.8987 257.09
0.9084 253.75
0.9165 250.68
0.9282 245.33

Sources