Mixture of Acetonitrile + Hexane, 1-ethoxy-

Excel

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

Hexane, 1-ethoxy-

Name
Hexane, 1-ethoxy-
InChI
InChI=1S/C8H18O/c1-3-5-6-7-8-9-4-2/h3-8H2,1-2H3
InChI Key
ZXHQLEQLZPJIFG-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCCCOCC
Mol. Weight (g/mol)
130.23
CAS
5756-43-4
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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 (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0307 0.1173
298.15 0.0596 0.2542
298.15 0.0868 0.3712
298.15 0.1125 0.4693
298.15 0.1368 0.5540
298.15 0.1816 0.6942
298.15 0.2220 0.8025
298.15 0.2586 0.8869
298.15 0.2919 0.9552
298.15 0.3223 1.0093
298.15 0.3759 1.0863
298.15 0.4217 1.134
298.15 0.4612 1.1617
298.15 0.5038 1.1791
298.15 0.5401 1.1826
298.15 0.5715 1.1791
298.15 0.5988 1.1684
298.15 0.6274 1.1508
298.15 0.6521 1.1302
298.15 0.6738 1.1083
298.15 0.6959 1.0814
298.15 0.7006 1.065
298.15 0.7152 1.0518
298.15 0.7222 1.033
298.15 0.7322 1.0245
298.15 0.7452 0.9939
298.15 0.7473 0.9980
298.15 0.7608 0.9727
298.15 0.7698 0.9457
298.15 0.7960 0.8866
298.15 0.8241 0.8131
298.15 0.8419 0.7604
298.15 0.8604 0.6998
298.15 0.8799 0.6298
298.15 0.9002 0.5484
298.15 0.9215 0.4531
298.15 0.9514 0.3005
298.15 0.9832 0.1106
298.15 0.9362 0.3809
298.15 0.9670 0.2109
308.15 0.0303 0.1392
308.15 0.0588 0.2814
308.15 0.0857 0.4014
308.15 0.1111 0.5044
308.15 0.1352 0.5937
308.15 0.1795 0.7407
308.15 0.2196 0.8547
308.15 0.2559 0.9437
308.15 0.2889 1.0143
308.15 0.3192 1.0704
308.15 0.3726 1.1507
308.15 0.4182 1.1999
308.15 0.4577 1.2288
308.15 0.5002 1.246
308.15 0.5366 1.2494
308.15 0.5680 1.2437
308.15 0.5954 1.2319
308.15 0.6241 1.213
308.15 0.6489 1.1909
308.15 0.6707 1.1671
308.15 0.6929 1.138
308.15 0.7087 1.1066
308.15 0.7123 1.1085
308.15 0.7294 1.0796
308.15 0.7300 1.0707
308.15 0.7446 1.0511
308.15 0.7526 1.0272
308.15 0.7582 1.0234
308.15 0.7767 0.9742
308.15 0.8023 0.9094
308.15 0.8297 0.8300
308.15 0.8470 0.7737
308.15 0.8651 0.7093
308.15 0.8840 0.6355
308.15 0.9037 0.5509
308.15 0.9243 0.4532
308.15 0.9385 0.3804
308.15 0.9531 0.3003
308.15 0.9683 0.2103
308.15 0.9839 0.1099

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 (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
298.15 0.0307 0.1173
298.15 0.0596 0.2542
298.15 0.0868 0.3712
298.15 0.1125 0.4693
298.15 0.1368 0.5540
298.15 0.1816 0.6942
298.15 0.2220 0.8025
298.15 0.2586 0.8869
298.15 0.2919 0.9552
298.15 0.3223 1.0093
298.15 0.3759 1.0863
298.15 0.4217 1.134
298.15 0.4612 1.1617
298.15 0.5038 1.1791
298.15 0.5401 1.1826
298.15 0.5715 1.1791
298.15 0.5988 1.1684
298.15 0.6274 1.1508
298.15 0.6521 1.1302
298.15 0.6738 1.1083
298.15 0.6959 1.0814
298.15 0.7006 1.065
298.15 0.7152 1.0518
298.15 0.7222 1.033
298.15 0.7322 1.0245
298.15 0.7452 0.9939
298.15 0.7473 0.9980
298.15 0.7608 0.9727
298.15 0.7698 0.9457
298.15 0.7960 0.8866
298.15 0.8241 0.8131
298.15 0.8419 0.7604
298.15 0.8604 0.6998
298.15 0.8799 0.6298
298.15 0.9002 0.5484
298.15 0.9215 0.4531
298.15 0.9514 0.3005
298.15 0.9832 0.1106
298.15 0.9362 0.3809
298.15 0.9670 0.2109
308.15 0.0303 0.1392
308.15 0.0588 0.2814
308.15 0.0857 0.4014
308.15 0.1111 0.5044
308.15 0.1352 0.5937
308.15 0.1795 0.7407
308.15 0.2196 0.8547
308.15 0.2559 0.9437
308.15 0.2889 1.0143
308.15 0.3192 1.0704
308.15 0.3726 1.1507
308.15 0.4182 1.1999
308.15 0.4577 1.2288
308.15 0.5002 1.246
308.15 0.5366 1.2494
308.15 0.5680 1.2437
308.15 0.5954 1.2319
308.15 0.6241 1.213
308.15 0.6489 1.1909
308.15 0.6707 1.1671
308.15 0.6929 1.138
308.15 0.7087 1.1066
308.15 0.7123 1.1085
308.15 0.7294 1.0796
308.15 0.7300 1.0707
308.15 0.7446 1.0511
308.15 0.7526 1.0272
308.15 0.7582 1.0234
308.15 0.7767 0.9742
308.15 0.8023 0.9094
308.15 0.8297 0.8300
308.15 0.8470 0.7737
308.15 0.8651 0.7093
308.15 0.8840 0.6355
308.15 0.9037 0.5509
308.15 0.9243 0.4532
308.15 0.9385 0.3804
308.15 0.9531 0.3003
308.15 0.9683 0.2103
308.15 0.9839 0.1099

Liquid-liquid equilibrium temperature, K [ref]

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

Mole fraction of Acetonitrile (1) - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.3570 236.43
0.3906 240.56
0.4301 244.81
0.4631 247.14
0.5006 249.33
0.5409 251.04
0.5762 252.15
0.5772 252.02
0.6155 252.95
0.6547 253.47
0.6865 253.91
0.7184 254.16
0.7515 253.99
0.7834 253.74
0.8115 253.16
0.8403 250.99
0.8592 249.15
0.8793 246.18
0.8945 242.59
0.9018 239.90
0.9106 236.73
0.9182 234.41

Liquid-liquid equilibrium temperature, K [ref]

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

Mole fraction of Acetonitrile (1) - Liquid mixture 1 Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.3570 236.43
0.3906 240.56
0.4301 244.81
0.4631 247.14
0.5006 249.33
0.5409 251.04
0.5762 252.15
0.5772 252.02
0.6155 252.95
0.6547 253.47
0.6865 253.91
0.7184 254.16
0.7515 253.99
0.7834 253.74
0.8115 253.16
0.8403 250.99
0.8592 249.15
0.8793 246.18
0.8945 242.59
0.9018 239.90
0.9106 236.73
0.9182 234.41

Sources