Operational condition: Pressure, kPa = 95.2 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Mole fraction of 1-Propanol, 2-methyl- (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.2960 | 0.8810 |
0.3540 | 0.9210 |
0.4560 | 0.9480 |
0.5570 | 0.9530 |
0.6270 | 0.9640 |
0.6770 | 0.9710 |
0.7160 | 0.9720 |
0.7460 | 0.9770 |
0.7710 | 0.9780 |
0.7910 | 0.9820 |
0.8080 | 0.9840 |
0.8220 | 0.9850 |
0.8550 | 0.9880 |
0.8940 | 0.9900 |
0.9550 | 0.9930 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 95.2 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Mole fraction of 1-Propanol, 2-methyl- (1) - Gas |
---|---|
0.0000 | 0.0000 |
0.2960 | 0.8810 |
0.3540 | 0.9210 |
0.4560 | 0.9480 |
0.5570 | 0.9530 |
0.6270 | 0.9640 |
0.6770 | 0.9710 |
0.7160 | 0.9720 |
0.7460 | 0.9770 |
0.7710 | 0.9780 |
0.7910 | 0.9820 |
0.8080 | 0.9840 |
0.8220 | 0.9850 |
0.8550 | 0.9880 |
0.8940 | 0.9900 |
0.9550 | 0.9930 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Acetophenone (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.20 | 0.1005 | 0.6958 |
298.20 | 0.2010 | 1.1021 |
298.20 | 0.3010 | 1.3661 |
298.20 | 0.3512 | 1.4489 |
298.20 | 0.4014 | 1.5109 |
298.20 | 0.4516 | 1.5502 |
298.20 | 0.5017 | 1.5673 |
298.20 | 0.5518 | 1.5614 |
298.20 | 0.6016 | 1.5328 |
298.20 | 0.6513 | 1.4795 |
298.20 | 0.7008 | 1.4005 |
298.20 | 0.8016 | 1.1346 |
298.20 | 0.9010 | 0.6842 |
313.20 | 0.1005 | 0.8039 |
313.20 | 0.2010 | 1.3046 |
313.20 | 0.3010 | 1.63 |
313.20 | 0.3512 | 1.732 |
313.20 | 0.4014 | 1.8068 |
313.20 | 0.4516 | 1.8517 |
313.20 | 0.5017 | 1.8663 |
313.20 | 0.5518 | 1.8521 |
313.20 | 0.6016 | 1.8084 |
313.20 | 0.6513 | 1.7354 |
313.20 | 0.7008 | 1.626 |
313.20 | 0.8016 | 1.2766 |
313.20 | 0.9010 | 0.7414 |
328.20 | 0.1005 | 0.9176 |
328.20 | 0.2010 | 1.4909 |
328.20 | 0.3010 | 1.8798 |
328.20 | 0.3512 | 1.9901 |
328.20 | 0.4014 | 2.0685 |
328.20 | 0.4516 | 2.1068 |
328.20 | 0.5017 | 2.1136 |
328.20 | 0.5518 | 2.0832 |
328.20 | 0.6016 | 2.0162 |
328.20 | 0.6513 | 1.9069 |
328.20 | 0.7008 | 1.7708 |
328.20 | 0.8016 | 1.3564 |
328.20 | 0.9010 | 0.7646 |
338.20 | 0.1005 | 0.9335 |
338.20 | 0.2010 | 1.5373 |
338.20 | 0.3010 | 1.9258 |
338.20 | 0.3512 | 2.0417 |
338.20 | 0.4014 | 2.1219 |
338.20 | 0.4516 | 2.1601 |
338.20 | 0.5017 | 2.1606 |
338.20 | 0.5518 | 2.1247 |
338.20 | 0.6016 | 2.0478 |
338.20 | 0.6513 | 1.937 |
338.20 | 0.7008 | 1.7838 |
338.20 | 0.8016 | 1.3617 |
338.20 | 0.9010 | 0.7759 |
348.20 | 0.1005 | 0.9399 |
348.20 | 0.2010 | 1.5442 |
348.20 | 0.3010 | 1.9341 |
348.20 | 0.3512 | 2.0554 |
348.20 | 0.4014 | 2.131 |
348.20 | 0.4516 | 2.1731 |
348.20 | 0.5017 | 2.1761 |
348.20 | 0.5518 | 2.1332 |
348.20 | 0.6016 | 2.0584 |
348.20 | 0.6513 | 1.9531 |
348.20 | 0.7008 | 1.7899 |
348.20 | 0.8016 | 1.3781 |
348.20 | 0.9010 | 0.7837 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Acetophenone (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.20 | 0.1005 | 0.6958 |
298.20 | 0.2010 | 1.1021 |
298.20 | 0.3010 | 1.3661 |
298.20 | 0.3512 | 1.4489 |
298.20 | 0.4014 | 1.5109 |
298.20 | 0.4516 | 1.5502 |
298.20 | 0.5017 | 1.5673 |
298.20 | 0.5518 | 1.5614 |
298.20 | 0.6016 | 1.5328 |
298.20 | 0.6513 | 1.4795 |
298.20 | 0.7008 | 1.4005 |
298.20 | 0.8016 | 1.1346 |
298.20 | 0.9010 | 0.6842 |
313.20 | 0.1005 | 0.8039 |
313.20 | 0.2010 | 1.3046 |
313.20 | 0.3010 | 1.63 |
313.20 | 0.3512 | 1.732 |
313.20 | 0.4014 | 1.8068 |
313.20 | 0.4516 | 1.8517 |
313.20 | 0.5017 | 1.8663 |
313.20 | 0.5518 | 1.8521 |
313.20 | 0.6016 | 1.8084 |
313.20 | 0.6513 | 1.7354 |
313.20 | 0.7008 | 1.626 |
313.20 | 0.8016 | 1.2766 |
313.20 | 0.9010 | 0.7414 |
328.20 | 0.1005 | 0.9176 |
328.20 | 0.2010 | 1.4909 |
328.20 | 0.3010 | 1.8798 |
328.20 | 0.3512 | 1.9901 |
328.20 | 0.4014 | 2.0685 |
328.20 | 0.4516 | 2.1068 |
328.20 | 0.5017 | 2.1136 |
328.20 | 0.5518 | 2.0832 |
328.20 | 0.6016 | 2.0162 |
328.20 | 0.6513 | 1.9069 |
328.20 | 0.7008 | 1.7708 |
328.20 | 0.8016 | 1.3564 |
328.20 | 0.9010 | 0.7646 |
338.20 | 0.1005 | 0.9335 |
338.20 | 0.2010 | 1.5373 |
338.20 | 0.3010 | 1.9258 |
338.20 | 0.3512 | 2.0417 |
338.20 | 0.4014 | 2.1219 |
338.20 | 0.4516 | 2.1601 |
338.20 | 0.5017 | 2.1606 |
338.20 | 0.5518 | 2.1247 |
338.20 | 0.6016 | 2.0478 |
338.20 | 0.6513 | 1.937 |
338.20 | 0.7008 | 1.7838 |
338.20 | 0.8016 | 1.3617 |
338.20 | 0.9010 | 0.7759 |
348.20 | 0.1005 | 0.9399 |
348.20 | 0.2010 | 1.5442 |
348.20 | 0.3010 | 1.9341 |
348.20 | 0.3512 | 2.0554 |
348.20 | 0.4014 | 2.131 |
348.20 | 0.4516 | 2.1731 |
348.20 | 0.5017 | 2.1761 |
348.20 | 0.5518 | 2.1332 |
348.20 | 0.6016 | 2.0584 |
348.20 | 0.6513 | 1.9531 |
348.20 | 0.7008 | 1.7899 |
348.20 | 0.8016 | 1.3781 |
348.20 | 0.9010 | 0.7837 |
Operational condition: Pressure, kPa = 95.2 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 472.25 |
0.2960 | 403.15 |
0.3540 | 399.31 |
0.4560 | 394.15 |
0.5570 | 391.15 |
0.6270 | 389.15 |
0.6770 | 388.65 |
0.7160 | 388.15 |
0.7460 | 387.15 |
0.7710 | 386.15 |
0.7910 | 385.15 |
0.8080 | 384.65 |
0.8220 | 384.15 |
0.8550 | 383.65 |
0.8940 | 382.65 |
0.9550 | 380.65 |
1.0000 | 379.65 |
Operational condition: Pressure, kPa = 95.2 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 472.25 |
0.2960 | 403.15 |
0.3540 | 399.31 |
0.4560 | 394.15 |
0.5570 | 391.15 |
0.6270 | 389.15 |
0.6770 | 388.65 |
0.7160 | 388.15 |
0.7460 | 387.15 |
0.7710 | 386.15 |
0.7910 | 385.15 |
0.8080 | 384.65 |
0.8220 | 384.15 |
0.8550 | 383.65 |
0.8940 | 382.65 |
0.9550 | 380.65 |
1.0000 | 379.65 |