Datasets
-
Mole fraction (2)
-
η - Viscosity, Pa*s (2)
-
ρl - Mass density, kg/m3 (4)
-
csound,fluid - Speed of Sound, m/s (2)
-
γ - Surface tension liquid-gas, N/m (4)
-
Tboil - Boiling temperature at pressure P, K (2)
-
Vapor Liquid Equilibrium at Constant Temperature (3)
Mole fraction of Acetone (1)
[ref]
Operational condition: Pressure, kPa =
94 (Liquid)
Mole fraction of Acetone (1) - Liquid |
Mole fraction of Acetone (1) - Gas |
0.0000 |
0.0000 |
0.0240 |
0.1990 |
0.0530 |
0.3490 |
0.0990 |
0.4740 |
0.1440 |
0.5390 |
0.1910 |
0.5800 |
0.2460 |
0.6140 |
0.2960 |
0.6340 |
0.3450 |
0.6500 |
0.3990 |
0.6640 |
0.4530 |
0.6780 |
0.5010 |
0.6880 |
0.5520 |
0.6990 |
0.6090 |
0.7120 |
0.6590 |
0.7250 |
0.7140 |
0.7410 |
0.7680 |
0.7620 |
0.8230 |
0.7900 |
0.8790 |
0.8300 |
0.9350 |
0.8870 |
0.9690 |
0.9380 |
1.0000 |
1.0000 |
Mole fraction of Acetone (1)
[ref]
Operational condition: Pressure, kPa =
94 (Liquid)
Mole fraction of Acetone (1) - Liquid |
Mole fraction of Acetone (1) - Gas |
0.0000 |
0.0000 |
0.0240 |
0.1990 |
0.0530 |
0.3490 |
0.0990 |
0.4740 |
0.1440 |
0.5390 |
0.1910 |
0.5800 |
0.2460 |
0.6140 |
0.2960 |
0.6340 |
0.3450 |
0.6500 |
0.3990 |
0.6640 |
0.4530 |
0.6780 |
0.5010 |
0.6880 |
0.5520 |
0.6990 |
0.6090 |
0.7120 |
0.6590 |
0.7250 |
0.7140 |
0.7410 |
0.7680 |
0.7620 |
0.8230 |
0.7900 |
0.8790 |
0.8300 |
0.9350 |
0.8870 |
0.9690 |
0.9380 |
1.0000 |
1.0000 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Cyclohexane (2) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0003 |
293.15 |
0.0490 |
0.0003 |
293.15 |
0.0917 |
0.0003 |
293.15 |
0.1959 |
0.0004 |
293.15 |
0.2889 |
0.0004 |
293.15 |
0.4092 |
0.0004 |
293.15 |
0.5009 |
0.0005 |
293.15 |
0.5984 |
0.0005 |
293.15 |
0.7007 |
0.0006 |
293.15 |
0.8046 |
0.0007 |
293.15 |
0.9051 |
0.0008 |
293.15 |
0.9580 |
0.0009 |
293.15 |
1.0000 |
0.0010 |
298.15 |
0.0000 |
0.0003 |
298.15 |
0.0490 |
0.0003 |
298.15 |
0.0917 |
0.0003 |
298.15 |
0.1959 |
0.0003 |
298.15 |
0.2889 |
0.0004 |
298.15 |
0.4092 |
0.0004 |
298.15 |
0.5009 |
0.0005 |
298.15 |
0.5984 |
0.0005 |
298.15 |
0.7007 |
0.0006 |
298.15 |
0.8046 |
0.0006 |
298.15 |
0.9051 |
0.0008 |
298.15 |
0.9580 |
0.0008 |
298.15 |
1.0000 |
0.0009 |
303.15 |
0.0000 |
0.0003 |
303.15 |
0.0490 |
0.0003 |
303.15 |
0.0917 |
0.0003 |
303.15 |
0.1959 |
0.0003 |
303.15 |
0.2889 |
0.0004 |
303.15 |
0.4092 |
0.0004 |
303.15 |
0.5009 |
0.0004 |
303.15 |
0.5984 |
0.0005 |
303.15 |
0.7007 |
0.0005 |
303.15 |
0.8046 |
0.0006 |
303.15 |
0.9051 |
0.0007 |
303.15 |
0.9580 |
0.0008 |
303.15 |
1.0000 |
0.0008 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Cyclohexane (2) - Liquid |
Viscosity, Pa*s - Liquid |
293.15 |
0.0000 |
0.0003 |
293.15 |
0.0490 |
0.0003 |
293.15 |
0.0917 |
0.0003 |
293.15 |
0.1959 |
0.0004 |
293.15 |
0.2889 |
0.0004 |
293.15 |
0.4092 |
0.0004 |
293.15 |
0.5009 |
0.0005 |
293.15 |
0.5984 |
0.0005 |
293.15 |
0.7007 |
0.0006 |
293.15 |
0.8046 |
0.0007 |
293.15 |
0.9051 |
0.0008 |
293.15 |
0.9580 |
0.0009 |
293.15 |
1.0000 |
0.0010 |
298.15 |
0.0000 |
0.0003 |
298.15 |
0.0490 |
0.0003 |
298.15 |
0.0917 |
0.0003 |
298.15 |
0.1959 |
0.0003 |
298.15 |
0.2889 |
0.0004 |
298.15 |
0.4092 |
0.0004 |
298.15 |
0.5009 |
0.0005 |
298.15 |
0.5984 |
0.0005 |
298.15 |
0.7007 |
0.0006 |
298.15 |
0.8046 |
0.0006 |
298.15 |
0.9051 |
0.0008 |
298.15 |
0.9580 |
0.0008 |
298.15 |
1.0000 |
0.0009 |
303.15 |
0.0000 |
0.0003 |
303.15 |
0.0490 |
0.0003 |
303.15 |
0.0917 |
0.0003 |
303.15 |
0.1959 |
0.0003 |
303.15 |
0.2889 |
0.0004 |
303.15 |
0.4092 |
0.0004 |
303.15 |
0.5009 |
0.0004 |
303.15 |
0.5984 |
0.0005 |
303.15 |
0.7007 |
0.0005 |
303.15 |
0.8046 |
0.0006 |
303.15 |
0.9051 |
0.0007 |
303.15 |
0.9580 |
0.0008 |
303.15 |
1.0000 |
0.0008 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Cyclohexane (2) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0000 |
798.2 |
288.15 |
0.1002 |
790.0 |
288.15 |
0.2001 |
786.6 |
288.15 |
0.2993 |
783.2 |
288.15 |
0.3979 |
781.1 |
288.15 |
0.4964 |
779.7 |
288.15 |
0.6000 |
778.9 |
288.15 |
0.6975 |
778.9 |
288.15 |
0.7993 |
779.4 |
288.15 |
0.8994 |
780.7 |
288.15 |
1.0000 |
783.2 |
298.15 |
0.0000 |
787.0 |
298.15 |
0.1002 |
779.7 |
298.15 |
0.2001 |
775.3 |
298.15 |
0.2993 |
772.3 |
298.15 |
0.3979 |
769.7 |
298.15 |
0.4964 |
769.2 |
298.15 |
0.6000 |
768.6 |
298.15 |
0.6975 |
768.7 |
298.15 |
0.7993 |
769.5 |
298.15 |
0.8994 |
771.1 |
298.15 |
1.0000 |
773.9 |
308.15 |
0.0000 |
775.4 |
308.15 |
0.1002 |
768.4 |
308.15 |
0.2001 |
764.2 |
308.15 |
0.2993 |
761.4 |
308.15 |
0.3979 |
759.6 |
308.15 |
0.4964 |
758.6 |
308.15 |
0.6000 |
758.2 |
308.15 |
0.6975 |
759.9 |
308.15 |
0.7993 |
759.6 |
308.15 |
0.8994 |
761.4 |
308.15 |
1.0000 |
764.4 |
318.15 |
0.0000 |
762.5 |
318.15 |
0.1002 |
756.9 |
318.15 |
0.2001 |
753.0 |
318.15 |
0.2993 |
750.2 |
318.15 |
0.3979 |
748.6 |
318.15 |
0.4964 |
747.8 |
318.15 |
0.6000 |
747.6 |
318.15 |
0.6975 |
748.3 |
318.15 |
0.7993 |
749.6 |
318.15 |
0.8994 |
751.6 |
318.15 |
1.0000 |
754.8 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Cyclohexane (2) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
791.11 |
293.15 |
0.0490 |
788.1 |
293.15 |
0.0917 |
785.55 |
293.15 |
0.1959 |
780.98 |
293.15 |
0.2889 |
777.95 |
293.15 |
0.4092 |
775.47 |
293.15 |
0.5009 |
774.37 |
293.15 |
0.5984 |
773.83 |
293.15 |
0.7007 |
773.87 |
293.15 |
0.8046 |
774.59 |
293.15 |
0.9051 |
776.04 |
293.15 |
0.9580 |
777.27 |
293.15 |
1.0000 |
778.62 |
298.15 |
0.0000 |
785.41 |
298.15 |
0.0490 |
782.46 |
298.15 |
0.0917 |
779.94 |
298.15 |
0.1959 |
775.47 |
298.15 |
0.2889 |
772.5 |
298.15 |
0.4092 |
770.14 |
298.15 |
0.5009 |
769.13 |
298.15 |
0.5984 |
768.69 |
298.15 |
0.7007 |
768.83 |
298.15 |
0.8046 |
769.66 |
298.15 |
0.9051 |
771.22 |
298.15 |
0.9580 |
772.53 |
298.15 |
1.0000 |
773.92 |
303.15 |
0.0000 |
779.66 |
303.15 |
0.0490 |
776.76 |
303.15 |
0.0917 |
774.28 |
303.15 |
0.1959 |
769.9 |
303.15 |
0.2889 |
767.02 |
303.15 |
0.4092 |
764.77 |
303.15 |
0.5009 |
763.86 |
303.15 |
0.5984 |
763.5 |
303.15 |
0.7007 |
763.75 |
303.15 |
0.8046 |
764.7 |
303.15 |
0.9051 |
766.38 |
303.15 |
0.9580 |
767.75 |
303.15 |
1.0000 |
769.19 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Cyclohexane (2) - Liquid |
Mass density, kg/m3 - Liquid |
288.15 |
0.0000 |
798.2 |
288.15 |
0.1002 |
790.0 |
288.15 |
0.2001 |
786.6 |
288.15 |
0.2993 |
783.2 |
288.15 |
0.3979 |
781.1 |
288.15 |
0.4964 |
779.7 |
288.15 |
0.6000 |
778.9 |
288.15 |
0.6975 |
778.9 |
288.15 |
0.7993 |
779.4 |
288.15 |
0.8994 |
780.7 |
288.15 |
1.0000 |
783.2 |
298.15 |
0.0000 |
787.0 |
298.15 |
0.1002 |
779.7 |
298.15 |
0.2001 |
775.3 |
298.15 |
0.2993 |
772.3 |
298.15 |
0.3979 |
769.7 |
298.15 |
0.4964 |
769.2 |
298.15 |
0.6000 |
768.6 |
298.15 |
0.6975 |
768.7 |
298.15 |
0.7993 |
769.5 |
298.15 |
0.8994 |
771.1 |
298.15 |
1.0000 |
773.9 |
308.15 |
0.0000 |
775.4 |
308.15 |
0.1002 |
768.4 |
308.15 |
0.2001 |
764.2 |
308.15 |
0.2993 |
761.4 |
308.15 |
0.3979 |
759.6 |
308.15 |
0.4964 |
758.6 |
308.15 |
0.6000 |
758.2 |
308.15 |
0.6975 |
759.9 |
308.15 |
0.7993 |
759.6 |
308.15 |
0.8994 |
761.4 |
308.15 |
1.0000 |
764.4 |
318.15 |
0.0000 |
762.5 |
318.15 |
0.1002 |
756.9 |
318.15 |
0.2001 |
753.0 |
318.15 |
0.2993 |
750.2 |
318.15 |
0.3979 |
748.6 |
318.15 |
0.4964 |
747.8 |
318.15 |
0.6000 |
747.6 |
318.15 |
0.6975 |
748.3 |
318.15 |
0.7993 |
749.6 |
318.15 |
0.8994 |
751.6 |
318.15 |
1.0000 |
754.8 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Cyclohexane (2) - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
0.0000 |
791.11 |
293.15 |
0.0490 |
788.1 |
293.15 |
0.0917 |
785.55 |
293.15 |
0.1959 |
780.98 |
293.15 |
0.2889 |
777.95 |
293.15 |
0.4092 |
775.47 |
293.15 |
0.5009 |
774.37 |
293.15 |
0.5984 |
773.83 |
293.15 |
0.7007 |
773.87 |
293.15 |
0.8046 |
774.59 |
293.15 |
0.9051 |
776.04 |
293.15 |
0.9580 |
777.27 |
293.15 |
1.0000 |
778.62 |
298.15 |
0.0000 |
785.41 |
298.15 |
0.0490 |
782.46 |
298.15 |
0.0917 |
779.94 |
298.15 |
0.1959 |
775.47 |
298.15 |
0.2889 |
772.5 |
298.15 |
0.4092 |
770.14 |
298.15 |
0.5009 |
769.13 |
298.15 |
0.5984 |
768.69 |
298.15 |
0.7007 |
768.83 |
298.15 |
0.8046 |
769.66 |
298.15 |
0.9051 |
771.22 |
298.15 |
0.9580 |
772.53 |
298.15 |
1.0000 |
773.92 |
303.15 |
0.0000 |
779.66 |
303.15 |
0.0490 |
776.76 |
303.15 |
0.0917 |
774.28 |
303.15 |
0.1959 |
769.9 |
303.15 |
0.2889 |
767.02 |
303.15 |
0.4092 |
764.77 |
303.15 |
0.5009 |
763.86 |
303.15 |
0.5984 |
763.5 |
303.15 |
0.7007 |
763.75 |
303.15 |
0.8046 |
764.7 |
303.15 |
0.9051 |
766.38 |
303.15 |
0.9580 |
767.75 |
303.15 |
1.0000 |
769.19 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Cyclohexane (2) - Liquid |
Speed of sound, m/s - Liquid |
293.15 |
0.0000 |
1185.0 |
293.15 |
0.0490 |
1182.0 |
293.15 |
0.0917 |
1180.0 |
293.15 |
0.1959 |
1181.0 |
293.15 |
0.2889 |
1184.0 |
293.15 |
0.4092 |
1193.0 |
293.15 |
0.5009 |
1201.0 |
293.15 |
0.5984 |
1212.0 |
293.15 |
0.7007 |
1225.0 |
293.15 |
0.8046 |
1241.0 |
293.15 |
0.9051 |
1258.0 |
293.15 |
0.9580 |
1269.0 |
293.15 |
1.0000 |
1279.0 |
298.15 |
0.0000 |
1162.0 |
298.15 |
0.0490 |
1160.0 |
298.15 |
0.0917 |
1158.0 |
298.15 |
0.1959 |
1158.0 |
298.15 |
0.2889 |
1161.0 |
298.15 |
0.4092 |
1169.0 |
298.15 |
0.5009 |
1178.0 |
298.15 |
0.5984 |
1188.0 |
298.15 |
0.7007 |
1201.0 |
298.15 |
0.8046 |
1216.0 |
298.15 |
0.9051 |
1234.0 |
298.15 |
0.9580 |
1245.0 |
298.15 |
1.0000 |
1254.0 |
303.15 |
0.0000 |
1140.0 |
303.15 |
0.0490 |
1137.0 |
303.15 |
0.0917 |
1135.0 |
303.15 |
0.1959 |
1135.0 |
303.15 |
0.2889 |
1138.0 |
303.15 |
0.4092 |
1146.0 |
303.15 |
0.5009 |
1154.0 |
303.15 |
0.5984 |
1164.0 |
303.15 |
0.7007 |
1177.0 |
303.15 |
0.8046 |
1192.0 |
303.15 |
0.9051 |
1210.0 |
303.15 |
0.9580 |
1220.0 |
303.15 |
1.0000 |
1230.0 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101.325 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Cyclohexane (2) - Liquid |
Speed of sound, m/s - Liquid |
293.15 |
0.0000 |
1185.0 |
293.15 |
0.0490 |
1182.0 |
293.15 |
0.0917 |
1180.0 |
293.15 |
0.1959 |
1181.0 |
293.15 |
0.2889 |
1184.0 |
293.15 |
0.4092 |
1193.0 |
293.15 |
0.5009 |
1201.0 |
293.15 |
0.5984 |
1212.0 |
293.15 |
0.7007 |
1225.0 |
293.15 |
0.8046 |
1241.0 |
293.15 |
0.9051 |
1258.0 |
293.15 |
0.9580 |
1269.0 |
293.15 |
1.0000 |
1279.0 |
298.15 |
0.0000 |
1162.0 |
298.15 |
0.0490 |
1160.0 |
298.15 |
0.0917 |
1158.0 |
298.15 |
0.1959 |
1158.0 |
298.15 |
0.2889 |
1161.0 |
298.15 |
0.4092 |
1169.0 |
298.15 |
0.5009 |
1178.0 |
298.15 |
0.5984 |
1188.0 |
298.15 |
0.7007 |
1201.0 |
298.15 |
0.8046 |
1216.0 |
298.15 |
0.9051 |
1234.0 |
298.15 |
0.9580 |
1245.0 |
298.15 |
1.0000 |
1254.0 |
303.15 |
0.0000 |
1140.0 |
303.15 |
0.0490 |
1137.0 |
303.15 |
0.0917 |
1135.0 |
303.15 |
0.1959 |
1135.0 |
303.15 |
0.2889 |
1138.0 |
303.15 |
0.4092 |
1146.0 |
303.15 |
0.5009 |
1154.0 |
303.15 |
0.5984 |
1164.0 |
303.15 |
0.7007 |
1177.0 |
303.15 |
0.8046 |
1192.0 |
303.15 |
0.9051 |
1210.0 |
303.15 |
0.9580 |
1220.0 |
303.15 |
1.0000 |
1230.0 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
303.15 (Liquid)
Mole fraction of Acetone (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0470 |
0.0238 |
0.0910 |
0.0236 |
0.1850 |
0.0231 |
0.2980 |
0.0227 |
0.4030 |
0.0224 |
0.5130 |
0.0222 |
0.6210 |
0.0221 |
0.7360 |
0.0221 |
0.8420 |
0.0221 |
0.9430 |
0.0224 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Cyclohexane (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
287.81 |
0.0000 |
0.0239 |
287.81 |
0.1002 |
0.0235 |
287.81 |
0.2001 |
0.0232 |
287.81 |
0.2993 |
0.0232 |
287.81 |
0.3979 |
0.0233 |
287.81 |
0.4964 |
0.0236 |
287.81 |
0.6000 |
0.0239 |
287.81 |
0.6975 |
0.0243 |
287.81 |
0.7993 |
0.0247 |
287.81 |
0.8994 |
0.0251 |
287.81 |
1.0000 |
0.0253 |
297.82 |
0.0000 |
0.0228 |
297.82 |
0.1002 |
0.0222 |
297.82 |
0.2001 |
0.0220 |
297.82 |
0.2993 |
0.0220 |
297.82 |
0.3979 |
0.0221 |
297.82 |
0.4964 |
0.0222 |
297.82 |
0.6000 |
0.0225 |
297.82 |
0.6975 |
0.0228 |
297.82 |
0.7993 |
0.0232 |
297.82 |
0.8994 |
0.0238 |
297.82 |
1.0000 |
0.0242 |
307.86 |
0.0000 |
0.0216 |
307.86 |
0.1002 |
0.0210 |
307.86 |
0.2001 |
0.0208 |
307.86 |
0.2993 |
0.0208 |
307.86 |
0.3979 |
0.0209 |
307.86 |
0.4964 |
0.0211 |
307.86 |
0.6000 |
0.0214 |
307.86 |
0.6975 |
0.0216 |
307.86 |
0.7993 |
0.0221 |
307.86 |
0.8994 |
0.0226 |
307.86 |
1.0000 |
0.0230 |
317.86 |
0.0000 |
0.0203 |
317.86 |
0.1002 |
0.0199 |
317.86 |
0.2001 |
0.0196 |
317.86 |
0.2993 |
0.0196 |
317.86 |
0.3979 |
0.0197 |
317.86 |
0.4964 |
0.0200 |
317.86 |
0.6000 |
0.0203 |
317.86 |
0.6975 |
0.0206 |
317.86 |
0.7993 |
0.0210 |
317.86 |
0.8994 |
0.0215 |
317.86 |
1.0000 |
0.0218 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
303.15 (Liquid)
Mole fraction of Acetone (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0470 |
0.0238 |
0.0910 |
0.0236 |
0.1850 |
0.0231 |
0.2980 |
0.0227 |
0.4030 |
0.0224 |
0.5130 |
0.0222 |
0.6210 |
0.0221 |
0.7360 |
0.0221 |
0.8420 |
0.0221 |
0.9430 |
0.0224 |
Surface tension liquid-gas, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Cyclohexane (2) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
287.81 |
0.0000 |
0.0239 |
287.81 |
0.1002 |
0.0235 |
287.81 |
0.2001 |
0.0232 |
287.81 |
0.2993 |
0.0232 |
287.81 |
0.3979 |
0.0233 |
287.81 |
0.4964 |
0.0236 |
287.81 |
0.6000 |
0.0239 |
287.81 |
0.6975 |
0.0243 |
287.81 |
0.7993 |
0.0247 |
287.81 |
0.8994 |
0.0251 |
287.81 |
1.0000 |
0.0253 |
297.82 |
0.0000 |
0.0228 |
297.82 |
0.1002 |
0.0222 |
297.82 |
0.2001 |
0.0220 |
297.82 |
0.2993 |
0.0220 |
297.82 |
0.3979 |
0.0221 |
297.82 |
0.4964 |
0.0222 |
297.82 |
0.6000 |
0.0225 |
297.82 |
0.6975 |
0.0228 |
297.82 |
0.7993 |
0.0232 |
297.82 |
0.8994 |
0.0238 |
297.82 |
1.0000 |
0.0242 |
307.86 |
0.0000 |
0.0216 |
307.86 |
0.1002 |
0.0210 |
307.86 |
0.2001 |
0.0208 |
307.86 |
0.2993 |
0.0208 |
307.86 |
0.3979 |
0.0209 |
307.86 |
0.4964 |
0.0211 |
307.86 |
0.6000 |
0.0214 |
307.86 |
0.6975 |
0.0216 |
307.86 |
0.7993 |
0.0221 |
307.86 |
0.8994 |
0.0226 |
307.86 |
1.0000 |
0.0230 |
317.86 |
0.0000 |
0.0203 |
317.86 |
0.1002 |
0.0199 |
317.86 |
0.2001 |
0.0196 |
317.86 |
0.2993 |
0.0196 |
317.86 |
0.3979 |
0.0197 |
317.86 |
0.4964 |
0.0200 |
317.86 |
0.6000 |
0.0203 |
317.86 |
0.6975 |
0.0206 |
317.86 |
0.7993 |
0.0210 |
317.86 |
0.8994 |
0.0215 |
317.86 |
1.0000 |
0.0218 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
94 (Liquid)
Mole fraction of Acetone (1) - Gas |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
351.37 |
0.1990 |
345.05 |
0.3490 |
339.48 |
0.4740 |
334.38 |
0.5390 |
331.43 |
0.5800 |
329.52 |
0.6140 |
328.01 |
0.6340 |
327.05 |
0.6500 |
326.40 |
0.6640 |
325.85 |
0.6780 |
325.39 |
0.6880 |
325.05 |
0.6990 |
324.80 |
0.7120 |
324.57 |
0.7250 |
324.38 |
0.7410 |
324.28 |
0.7620 |
324.28 |
0.7900 |
324.33 |
0.8300 |
324.65 |
0.8870 |
325.36 |
0.9380 |
326.11 |
1.0000 |
327.16 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
94 (Liquid)
Mole fraction of Acetone (1) - Gas |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
351.37 |
0.1990 |
345.05 |
0.3490 |
339.48 |
0.4740 |
334.38 |
0.5390 |
331.43 |
0.5800 |
329.52 |
0.6140 |
328.01 |
0.6340 |
327.05 |
0.6500 |
326.40 |
0.6640 |
325.85 |
0.6780 |
325.39 |
0.6880 |
325.05 |
0.6990 |
324.80 |
0.7120 |
324.57 |
0.7250 |
324.38 |
0.7410 |
324.28 |
0.7620 |
324.28 |
0.7900 |
324.33 |
0.8300 |
324.65 |
0.8870 |
325.36 |
0.9380 |
326.11 |
1.0000 |
327.16 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
298.15 (VLE)
Fixed |
Measured |
P [kPa] - VLE |
x1[mol/mol] of Acetone (1) - Liquid |
y1[mol/mol] of Acetone (1) - Vapour |
30.919 |
0.2077 |
0.6184 |
32.383 |
0.2868 |
0.6452 |
33.22 |
0.3520 |
0.6609 |
33.739 |
0.4158 |
0.6737 |
34.181 |
0.4847 |
0.6867 |
34.552 |
0.5654 |
0.7025 |
34.765 |
0.6311 |
0.7156 |
34.874 |
0.6809 |
0.7272 |
34.944 |
0.7316 |
0.7403 |
34.832 |
0.7990 |
0.7681 |
34.526 |
0.8610 |
0.7976 |
33.795 |
0.9209 |
0.8536 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
308.15 (VLE)
Fixed |
Measured |
P [kPa] - VLE |
x1[mol/mol] of Acetone (1) - Liquid |
y1[mol/mol] of Acetone (1) - Vapour |
19.625 |
0.0000 |
0.0000 |
37.877 |
0.0980 |
0.4820 |
45.476 |
0.1980 |
0.6010 |
47.969 |
0.2830 |
0.6350 |
49.489 |
0.3870 |
0.6650 |
50.316 |
0.4890 |
0.6860 |
50.969 |
0.5980 |
0.7090 |
51.302 |
0.7000 |
0.7320 |
51.409 |
0.7710 |
0.7540 |
50.196 |
0.8950 |
0.8410 |
45.863 |
1.0000 |
1.0000 |
Vapor Liquid Equilibrium at Constant Temperature
[ref]
Operational condition: Temperature, K =
318.15 (VLE)
Fixed |
Measured |
P [kPa] - VLE |
x1[mol/mol] of Acetone (1) - Liquid |
y1[mol/mol] of Acetone (1) - Vapour |
29.464 |
0.0000 |
0.0000 |
53.236 |
0.0940 |
0.4580 |
65.088 |
0.1970 |
0.5870 |
69.168 |
0.2810 |
0.6290 |
71.607 |
0.3840 |
0.6580 |
72.901 |
0.4910 |
0.6800 |
74.154 |
0.5980 |
0.7040 |
75.087 |
0.7000 |
0.7340 |
74.781 |
0.7710 |
0.7590 |
73.181 |
0.8950 |
0.8510 |
67.461 |
1.0000 |
1.0000 |
Sources