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 |
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 |
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 |
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 |