Operational condition: Pressure, kPa = 99.81 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Cyclohexanol (1) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Cyclohexanol (1) - Liquid mixture 1 |
298.20 | 0.0064 | 0.9936 | 0.4381 | 0.5616 |
318.20 | 0.0035 | 0.9963 | 0.2706 | 0.3984 |
318.20 | 0.0031 | 0.9966 | 0.2259 | 0.3356 |
298.20 | 0.0001 | 0.9995 | 0.0404 | 0.0051 |
318.20 | 0.0024 | 0.9972 | 0.1556 | 0.2356 |
318.20 | 0.0020 | 0.9977 | 0.1192 | 0.1691 |
318.20 | 0.0012 | 0.9985 | 0.0841 | 0.0912 |
298.20 | 0.0052 | 0.9946 | 0.3630 | 0.5071 |
318.20 | 0.0001 | 0.9995 | 0.0574 | 0.0063 |
328.20 | 0.0052 | 0.9948 | 0.4479 | 0.5518 |
328.20 | 0.0046 | 0.9953 | 0.4097 | 0.5303 |
308.20 | 0.0022 | 0.9974 | 0.1111 | 0.1689 |
328.20 | 0.0041 | 0.9958 | 0.3786 | 0.4961 |
328.20 | 0.0036 | 0.9962 | 0.3329 | 0.4618 |
328.20 | 0.0033 | 0.9964 | 0.2747 | 0.3955 |
308.20 | 0.0059 | 0.9941 | 0.4406 | 0.5591 |
328.20 | 0.0029 | 0.9968 | 0.2331 | 0.3318 |
328.20 | 0.0023 | 0.9974 | 0.1602 | 0.2370 |
328.20 | 0.0018 | 0.9979 | 0.1261 | 0.1725 |
328.20 | 0.0011 | 0.9986 | 0.0950 | 0.0934 |
298.20 | 0.0046 | 0.9951 | 0.3171 | 0.4694 |
328.20 | 0.0001 | 0.9996 | 0.0661 | 0.0053 |
308.20 | 0.0014 | 0.9983 | 0.0763 | 0.0911 |
338.20 | 0.0051 | 0.9949 | 0.4526 | 0.5471 |
338.20 | 0.0045 | 0.9954 | 0.4120 | 0.5284 |
338.20 | 0.0040 | 0.9959 | 0.3792 | 0.4961 |
338.20 | 0.0036 | 0.9963 | 0.3395 | 0.4579 |
308.20 | 0.0051 | 0.9948 | 0.4036 | 0.5351 |
338.20 | 0.0033 | 0.9965 | 0.2783 | 0.3943 |
338.20 | 0.0027 | 0.9970 | 0.2419 | 0.3327 |
338.20 | 0.0021 | 0.9976 | 0.1660 | 0.2396 |
338.20 | 0.0016 | 0.9981 | 0.1334 | 0.1645 |
338.20 | 0.0009 | 0.9988 | 0.1024 | 0.0866 |
298.20 | 0.0057 | 0.9942 | 0.3992 | 0.5391 |
298.20 | 0.0043 | 0.9954 | 0.2587 | 0.4013 |
338.20 | 0.0002 | 0.9995 | 0.0765 | 0.0058 |
298.20 | 0.0039 | 0.9957 | 0.2137 | 0.3355 |
298.20 | 0.0031 | 0.9965 | 0.1405 | 0.2371 |
298.20 | 0.0025 | 0.9971 | 0.1030 | 0.1677 |
308.20 | 0.0045 | 0.9953 | 0.3694 | 0.5020 |
298.20 | 0.0016 | 0.9980 | 0.0676 | 0.0903 |
308.20 | 0.0040 | 0.9958 | 0.3250 | 0.4640 |
308.20 | 0.0038 | 0.9960 | 0.2660 | 0.3980 |
308.20 | 0.0034 | 0.9962 | 0.2194 | 0.3346 |
308.20 | 0.0001 | 0.9995 | 0.0473 | 0.0056 |
308.20 | 0.0027 | 0.9969 | 0.1492 | 0.2363 |
318.20 | 0.0053 | 0.9947 | 0.4452 | 0.5546 |
318.20 | 0.0048 | 0.9951 | 0.4066 | 0.5327 |
318.20 | 0.0042 | 0.9957 | 0.3737 | 0.4989 |
318.20 | 0.0037 | 0.9960 | 0.3295 | 0.4627 |
Operational condition: Pressure, kPa = 99.81 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Cyclohexanol (1) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Cyclohexanol (1) - Liquid mixture 1 |
298.20 | 0.0064 | 0.9936 | 0.4381 | 0.5616 |
318.20 | 0.0035 | 0.9963 | 0.2706 | 0.3984 |
318.20 | 0.0031 | 0.9966 | 0.2259 | 0.3356 |
298.20 | 0.0001 | 0.9995 | 0.0404 | 0.0051 |
318.20 | 0.0024 | 0.9972 | 0.1556 | 0.2356 |
318.20 | 0.0020 | 0.9977 | 0.1192 | 0.1691 |
318.20 | 0.0012 | 0.9985 | 0.0841 | 0.0912 |
298.20 | 0.0052 | 0.9946 | 0.3630 | 0.5071 |
318.20 | 0.0001 | 0.9995 | 0.0574 | 0.0063 |
328.20 | 0.0052 | 0.9948 | 0.4479 | 0.5518 |
328.20 | 0.0046 | 0.9953 | 0.4097 | 0.5303 |
308.20 | 0.0022 | 0.9974 | 0.1111 | 0.1689 |
328.20 | 0.0041 | 0.9958 | 0.3786 | 0.4961 |
328.20 | 0.0036 | 0.9962 | 0.3329 | 0.4618 |
328.20 | 0.0033 | 0.9964 | 0.2747 | 0.3955 |
308.20 | 0.0059 | 0.9941 | 0.4406 | 0.5591 |
328.20 | 0.0029 | 0.9968 | 0.2331 | 0.3318 |
328.20 | 0.0023 | 0.9974 | 0.1602 | 0.2370 |
328.20 | 0.0018 | 0.9979 | 0.1261 | 0.1725 |
328.20 | 0.0011 | 0.9986 | 0.0950 | 0.0934 |
298.20 | 0.0046 | 0.9951 | 0.3171 | 0.4694 |
328.20 | 0.0001 | 0.9996 | 0.0661 | 0.0053 |
308.20 | 0.0014 | 0.9983 | 0.0763 | 0.0911 |
338.20 | 0.0051 | 0.9949 | 0.4526 | 0.5471 |
338.20 | 0.0045 | 0.9954 | 0.4120 | 0.5284 |
338.20 | 0.0040 | 0.9959 | 0.3792 | 0.4961 |
338.20 | 0.0036 | 0.9963 | 0.3395 | 0.4579 |
308.20 | 0.0051 | 0.9948 | 0.4036 | 0.5351 |
338.20 | 0.0033 | 0.9965 | 0.2783 | 0.3943 |
338.20 | 0.0027 | 0.9970 | 0.2419 | 0.3327 |
338.20 | 0.0021 | 0.9976 | 0.1660 | 0.2396 |
338.20 | 0.0016 | 0.9981 | 0.1334 | 0.1645 |
338.20 | 0.0009 | 0.9988 | 0.1024 | 0.0866 |
298.20 | 0.0057 | 0.9942 | 0.3992 | 0.5391 |
298.20 | 0.0043 | 0.9954 | 0.2587 | 0.4013 |
338.20 | 0.0002 | 0.9995 | 0.0765 | 0.0058 |
298.20 | 0.0039 | 0.9957 | 0.2137 | 0.3355 |
298.20 | 0.0031 | 0.9965 | 0.1405 | 0.2371 |
298.20 | 0.0025 | 0.9971 | 0.1030 | 0.1677 |
308.20 | 0.0045 | 0.9953 | 0.3694 | 0.5020 |
298.20 | 0.0016 | 0.9980 | 0.0676 | 0.0903 |
308.20 | 0.0040 | 0.9958 | 0.3250 | 0.4640 |
308.20 | 0.0038 | 0.9960 | 0.2660 | 0.3980 |
308.20 | 0.0034 | 0.9962 | 0.2194 | 0.3346 |
308.20 | 0.0001 | 0.9995 | 0.0473 | 0.0056 |
308.20 | 0.0027 | 0.9969 | 0.1492 | 0.2363 |
318.20 | 0.0053 | 0.9947 | 0.4452 | 0.5546 |
318.20 | 0.0048 | 0.9951 | 0.4066 | 0.5327 |
318.20 | 0.0042 | 0.9957 | 0.3737 | 0.4989 |
318.20 | 0.0037 | 0.9960 | 0.3295 | 0.4627 |