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 |
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 |
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 |
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 |