Datasets
-
Mole fraction (2)
-
ρl - Mass density, kg/m3 (2)
-
csound,fluid - Speed of Sound, m/s (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 2-Butanone (2)
[ref]
Fixed |
Measured |
Mole fraction of 2-Butanone (2) - Gas |
Pressure, kPa - Liquid |
Mole fraction of 2-Butanone (2) - Liquid |
0.0000 |
20.00 |
0.0000 |
0.0000 |
101.30 |
0.0000 |
0.0820 |
101.30 |
0.0330 |
0.1310 |
101.30 |
0.0540 |
0.1440 |
20.00 |
0.0340 |
0.1880 |
101.30 |
0.0820 |
0.2700 |
101.30 |
0.1260 |
0.2820 |
20.00 |
0.0750 |
0.3120 |
101.30 |
0.1480 |
0.3780 |
20.00 |
0.1140 |
0.3810 |
101.30 |
0.2110 |
0.4280 |
101.30 |
0.2430 |
0.4490 |
20.00 |
0.1560 |
0.5110 |
101.30 |
0.3200 |
0.5310 |
20.00 |
0.2010 |
0.5500 |
101.30 |
0.3680 |
0.5920 |
20.00 |
0.2510 |
0.6060 |
101.30 |
0.4290 |
0.6210 |
20.00 |
0.3000 |
0.6410 |
101.30 |
0.4740 |
0.6670 |
20.00 |
0.3590 |
0.6900 |
101.30 |
0.5440 |
0.7150 |
20.00 |
0.4150 |
0.7260 |
101.30 |
0.5990 |
0.7410 |
20.00 |
0.4640 |
0.7450 |
101.30 |
0.6260 |
0.7720 |
20.00 |
0.5160 |
0.7890 |
20.00 |
0.5630 |
0.7960 |
101.30 |
0.7050 |
0.8130 |
20.00 |
0.6140 |
0.8360 |
101.30 |
0.7640 |
0.8410 |
20.00 |
0.6680 |
0.8680 |
20.00 |
0.7240 |
0.8760 |
101.30 |
0.8240 |
0.8990 |
20.00 |
0.7770 |
0.9170 |
20.00 |
0.8330 |
0.9180 |
101.30 |
0.8880 |
0.9460 |
20.00 |
0.8920 |
0.9610 |
101.30 |
0.9470 |
0.9770 |
20.00 |
0.9520 |
1.0000 |
20.00 |
1.0000 |
1.0000 |
101.30 |
1.0000 |
Mole fraction of 2-Butanone (2)
[ref]
Fixed |
Measured |
Mole fraction of 2-Butanone (2) - Gas |
Pressure, kPa - Liquid |
Mole fraction of 2-Butanone (2) - Liquid |
0.0000 |
20.00 |
0.0000 |
0.0000 |
101.30 |
0.0000 |
0.0820 |
101.30 |
0.0330 |
0.1310 |
101.30 |
0.0540 |
0.1440 |
20.00 |
0.0340 |
0.1880 |
101.30 |
0.0820 |
0.2700 |
101.30 |
0.1260 |
0.2820 |
20.00 |
0.0750 |
0.3120 |
101.30 |
0.1480 |
0.3780 |
20.00 |
0.1140 |
0.3810 |
101.30 |
0.2110 |
0.4280 |
101.30 |
0.2430 |
0.4490 |
20.00 |
0.1560 |
0.5110 |
101.30 |
0.3200 |
0.5310 |
20.00 |
0.2010 |
0.5500 |
101.30 |
0.3680 |
0.5920 |
20.00 |
0.2510 |
0.6060 |
101.30 |
0.4290 |
0.6210 |
20.00 |
0.3000 |
0.6410 |
101.30 |
0.4740 |
0.6670 |
20.00 |
0.3590 |
0.6900 |
101.30 |
0.5440 |
0.7150 |
20.00 |
0.4150 |
0.7260 |
101.30 |
0.5990 |
0.7410 |
20.00 |
0.4640 |
0.7450 |
101.30 |
0.6260 |
0.7720 |
20.00 |
0.5160 |
0.7890 |
20.00 |
0.5630 |
0.7960 |
101.30 |
0.7050 |
0.8130 |
20.00 |
0.6140 |
0.8360 |
101.30 |
0.7640 |
0.8410 |
20.00 |
0.6680 |
0.8680 |
20.00 |
0.7240 |
0.8760 |
101.30 |
0.8240 |
0.8990 |
20.00 |
0.7770 |
0.9170 |
20.00 |
0.8330 |
0.9180 |
101.30 |
0.8880 |
0.9460 |
20.00 |
0.8920 |
0.9610 |
101.30 |
0.9470 |
0.9770 |
20.00 |
0.9520 |
1.0000 |
20.00 |
1.0000 |
1.0000 |
101.30 |
1.0000 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Butanone (2) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
293.15 |
803.476 |
0.0000 |
298.15 |
799.471 |
0.0000 |
303.15 |
795.437 |
0.0000 |
308.15 |
791.372 |
0.0000 |
313.15 |
787.262 |
0.0000 |
318.15 |
783.104 |
0.0000 |
323.15 |
778.897 |
0.0715 |
293.15 |
803.777 |
0.0715 |
298.15 |
799.63 |
0.0715 |
303.15 |
795.449 |
0.0715 |
308.15 |
791.232 |
0.0715 |
313.15 |
786.978 |
0.0715 |
318.16 |
782.677 |
0.0715 |
323.16 |
778.324 |
0.2005 |
293.15 |
804.182 |
0.2005 |
298.15 |
799.805 |
0.2005 |
303.15 |
795.395 |
0.2005 |
308.15 |
790.95 |
0.2005 |
313.15 |
786.464 |
0.2005 |
318.15 |
781.936 |
0.2005 |
323.15 |
777.356 |
0.3006 |
293.15 |
804.352 |
0.3006 |
298.15 |
799.821 |
0.3006 |
303.15 |
795.256 |
0.3006 |
308.15 |
790.663 |
0.3006 |
313.15 |
786.028 |
0.3006 |
318.15 |
781.346 |
0.3006 |
323.15 |
776.616 |
0.3996 |
293.15 |
804.467 |
0.3996 |
298.15 |
799.804 |
0.3996 |
303.15 |
795.106 |
0.3996 |
308.15 |
790.37 |
0.3996 |
313.15 |
785.6 |
0.3996 |
318.15 |
780.785 |
0.3996 |
323.15 |
775.92 |
0.5024 |
293.15 |
804.599 |
0.5024 |
298.15 |
799.814 |
0.5024 |
303.15 |
794.989 |
0.5024 |
308.15 |
790.125 |
0.5024 |
313.15 |
785.227 |
0.5024 |
318.15 |
780.284 |
0.5024 |
323.16 |
775.293 |
0.5993 |
293.15 |
804.707 |
0.5993 |
298.15 |
799.809 |
0.5993 |
303.15 |
794.877 |
0.5993 |
308.15 |
789.907 |
0.5993 |
313.15 |
784.898 |
0.5993 |
318.15 |
779.842 |
0.5993 |
323.15 |
774.741 |
0.6994 |
293.15 |
804.703 |
0.6994 |
298.15 |
799.703 |
0.6994 |
303.15 |
794.67 |
0.6994 |
308.15 |
789.597 |
0.6994 |
313.15 |
784.493 |
0.6994 |
318.16 |
779.342 |
0.6994 |
323.16 |
774.15 |
0.7995 |
293.15 |
804.771 |
0.7995 |
298.15 |
799.68 |
0.7995 |
303.15 |
794.556 |
0.7995 |
308.15 |
789.393 |
0.7995 |
313.15 |
784.201 |
0.7995 |
318.15 |
778.968 |
0.7995 |
323.15 |
773.693 |
0.8990 |
293.15 |
804.821 |
0.8990 |
298.15 |
799.65 |
0.8990 |
303.15 |
794.445 |
0.8990 |
308.15 |
789.215 |
0.8990 |
313.15 |
783.949 |
0.8990 |
318.15 |
778.645 |
0.8990 |
323.16 |
773.301 |
1.0000 |
293.15 |
804.834 |
1.0000 |
298.15 |
799.597 |
1.0000 |
303.15 |
794.334 |
1.0000 |
308.15 |
789.044 |
1.0000 |
313.15 |
783.72 |
1.0000 |
318.15 |
778.362 |
1.0000 |
323.15 |
772.966 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Butanone (2) - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
0.0000 |
293.15 |
803.476 |
0.0000 |
298.15 |
799.471 |
0.0000 |
303.15 |
795.437 |
0.0000 |
308.15 |
791.372 |
0.0000 |
313.15 |
787.262 |
0.0000 |
318.15 |
783.104 |
0.0000 |
323.15 |
778.897 |
0.0715 |
293.15 |
803.777 |
0.0715 |
298.15 |
799.63 |
0.0715 |
303.15 |
795.449 |
0.0715 |
308.15 |
791.232 |
0.0715 |
313.15 |
786.978 |
0.0715 |
318.16 |
782.677 |
0.0715 |
323.16 |
778.324 |
0.2005 |
293.15 |
804.182 |
0.2005 |
298.15 |
799.805 |
0.2005 |
303.15 |
795.395 |
0.2005 |
308.15 |
790.95 |
0.2005 |
313.15 |
786.464 |
0.2005 |
318.15 |
781.936 |
0.2005 |
323.15 |
777.356 |
0.3006 |
293.15 |
804.352 |
0.3006 |
298.15 |
799.821 |
0.3006 |
303.15 |
795.256 |
0.3006 |
308.15 |
790.663 |
0.3006 |
313.15 |
786.028 |
0.3006 |
318.15 |
781.346 |
0.3006 |
323.15 |
776.616 |
0.3996 |
293.15 |
804.467 |
0.3996 |
298.15 |
799.804 |
0.3996 |
303.15 |
795.106 |
0.3996 |
308.15 |
790.37 |
0.3996 |
313.15 |
785.6 |
0.3996 |
318.15 |
780.785 |
0.3996 |
323.15 |
775.92 |
0.5024 |
293.15 |
804.599 |
0.5024 |
298.15 |
799.814 |
0.5024 |
303.15 |
794.989 |
0.5024 |
308.15 |
790.125 |
0.5024 |
313.15 |
785.227 |
0.5024 |
318.15 |
780.284 |
0.5024 |
323.16 |
775.293 |
0.5993 |
293.15 |
804.707 |
0.5993 |
298.15 |
799.809 |
0.5993 |
303.15 |
794.877 |
0.5993 |
308.15 |
789.907 |
0.5993 |
313.15 |
784.898 |
0.5993 |
318.15 |
779.842 |
0.5993 |
323.15 |
774.741 |
0.6994 |
293.15 |
804.703 |
0.6994 |
298.15 |
799.703 |
0.6994 |
303.15 |
794.67 |
0.6994 |
308.15 |
789.597 |
0.6994 |
313.15 |
784.493 |
0.6994 |
318.16 |
779.342 |
0.6994 |
323.16 |
774.15 |
0.7995 |
293.15 |
804.771 |
0.7995 |
298.15 |
799.68 |
0.7995 |
303.15 |
794.556 |
0.7995 |
308.15 |
789.393 |
0.7995 |
313.15 |
784.201 |
0.7995 |
318.15 |
778.968 |
0.7995 |
323.15 |
773.693 |
0.8990 |
293.15 |
804.821 |
0.8990 |
298.15 |
799.65 |
0.8990 |
303.15 |
794.445 |
0.8990 |
308.15 |
789.215 |
0.8990 |
313.15 |
783.949 |
0.8990 |
318.15 |
778.645 |
0.8990 |
323.16 |
773.301 |
1.0000 |
293.15 |
804.834 |
1.0000 |
298.15 |
799.597 |
1.0000 |
303.15 |
794.334 |
1.0000 |
308.15 |
789.044 |
1.0000 |
313.15 |
783.72 |
1.0000 |
318.15 |
778.362 |
1.0000 |
323.15 |
772.966 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Butanone (2) - Liquid |
Temperature, K - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
293.15 |
1222.55 |
0.0000 |
298.15 |
1205.64 |
0.0000 |
303.15 |
1188.77 |
0.0000 |
308.15 |
1172.01 |
0.0000 |
313.15 |
1155.35 |
0.0000 |
318.15 |
1138.65 |
0.0000 |
323.15 |
1121.93 |
0.0715 |
293.15 |
1223.57 |
0.0715 |
298.15 |
1206.22 |
0.0715 |
303.15 |
1188.64 |
0.0715 |
308.15 |
1171.17 |
0.0715 |
313.15 |
1153.83 |
0.0715 |
318.16 |
1136.56 |
0.0715 |
323.16 |
1119.36 |
0.2005 |
293.15 |
1223.86 |
0.2005 |
298.15 |
1205.46 |
0.2005 |
303.15 |
1187.12 |
0.2005 |
308.15 |
1168.9 |
0.2005 |
313.15 |
1150.81 |
0.2005 |
318.15 |
1132.85 |
0.2005 |
323.15 |
1115.06 |
0.3006 |
293.15 |
1223.04 |
0.3006 |
298.15 |
1204.22 |
0.3006 |
303.15 |
1185.39 |
0.3006 |
308.15 |
1166.65 |
0.3006 |
313.15 |
1147.98 |
0.3006 |
318.15 |
1129.37 |
0.3006 |
323.15 |
1110.82 |
0.3996 |
293.15 |
1221.91 |
0.3996 |
298.15 |
1202.65 |
0.3996 |
303.15 |
1183.46 |
0.3996 |
308.15 |
1164.31 |
0.3996 |
313.15 |
1145.23 |
0.3996 |
318.15 |
1126.21 |
0.3996 |
323.15 |
1107.24 |
0.5024 |
293.15 |
1220.74 |
0.5024 |
298.15 |
1201.25 |
0.5024 |
303.15 |
1181.62 |
0.5024 |
308.15 |
1162.06 |
0.5024 |
313.15 |
1142.57 |
0.5024 |
318.15 |
1123.14 |
0.5024 |
323.16 |
1103.75 |
0.5993 |
293.15 |
1219.89 |
0.5993 |
298.15 |
1199.95 |
0.5993 |
303.15 |
1180.01 |
0.5993 |
308.15 |
1160.11 |
0.5993 |
313.15 |
1140.29 |
0.5993 |
318.15 |
1120.5 |
0.5993 |
323.15 |
1100.75 |
0.6994 |
293.15 |
1218.82 |
0.6994 |
298.15 |
1198.45 |
0.6994 |
303.15 |
1178.1 |
0.6994 |
308.15 |
1157.82 |
0.6994 |
313.15 |
1137.61 |
0.6994 |
318.16 |
1117.43 |
0.6994 |
323.16 |
1097.31 |
0.7995 |
293.15 |
1217.75 |
0.7995 |
298.15 |
1197.05 |
0.7995 |
303.15 |
1176.35 |
0.7995 |
308.15 |
1155.72 |
0.7995 |
313.15 |
1135.15 |
0.7995 |
318.15 |
1114.61 |
0.7995 |
323.15 |
1094.15 |
0.8990 |
293.15 |
1215.98 |
0.8990 |
298.15 |
1194.93 |
0.8990 |
303.15 |
1173.85 |
0.8990 |
308.15 |
1152.85 |
0.8990 |
313.15 |
1131.94 |
0.8990 |
318.15 |
1111.1 |
0.8990 |
323.16 |
1090.29 |
1.0000 |
293.15 |
1213.35 |
1.0000 |
298.15 |
1192.06 |
1.0000 |
303.15 |
1170.77 |
1.0000 |
308.15 |
1149.56 |
1.0000 |
313.15 |
1128.44 |
1.0000 |
318.15 |
1107.39 |
1.0000 |
323.15 |
1086.41 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Mole fraction of 2-Butanone (2) - Liquid |
Temperature, K - Liquid |
Speed of sound, m/s - Liquid |
0.0000 |
293.15 |
1222.55 |
0.0000 |
298.15 |
1205.64 |
0.0000 |
303.15 |
1188.77 |
0.0000 |
308.15 |
1172.01 |
0.0000 |
313.15 |
1155.35 |
0.0000 |
318.15 |
1138.65 |
0.0000 |
323.15 |
1121.93 |
0.0715 |
293.15 |
1223.57 |
0.0715 |
298.15 |
1206.22 |
0.0715 |
303.15 |
1188.64 |
0.0715 |
308.15 |
1171.17 |
0.0715 |
313.15 |
1153.83 |
0.0715 |
318.16 |
1136.56 |
0.0715 |
323.16 |
1119.36 |
0.2005 |
293.15 |
1223.86 |
0.2005 |
298.15 |
1205.46 |
0.2005 |
303.15 |
1187.12 |
0.2005 |
308.15 |
1168.9 |
0.2005 |
313.15 |
1150.81 |
0.2005 |
318.15 |
1132.85 |
0.2005 |
323.15 |
1115.06 |
0.3006 |
293.15 |
1223.04 |
0.3006 |
298.15 |
1204.22 |
0.3006 |
303.15 |
1185.39 |
0.3006 |
308.15 |
1166.65 |
0.3006 |
313.15 |
1147.98 |
0.3006 |
318.15 |
1129.37 |
0.3006 |
323.15 |
1110.82 |
0.3996 |
293.15 |
1221.91 |
0.3996 |
298.15 |
1202.65 |
0.3996 |
303.15 |
1183.46 |
0.3996 |
308.15 |
1164.31 |
0.3996 |
313.15 |
1145.23 |
0.3996 |
318.15 |
1126.21 |
0.3996 |
323.15 |
1107.24 |
0.5024 |
293.15 |
1220.74 |
0.5024 |
298.15 |
1201.25 |
0.5024 |
303.15 |
1181.62 |
0.5024 |
308.15 |
1162.06 |
0.5024 |
313.15 |
1142.57 |
0.5024 |
318.15 |
1123.14 |
0.5024 |
323.16 |
1103.75 |
0.5993 |
293.15 |
1219.89 |
0.5993 |
298.15 |
1199.95 |
0.5993 |
303.15 |
1180.01 |
0.5993 |
308.15 |
1160.11 |
0.5993 |
313.15 |
1140.29 |
0.5993 |
318.15 |
1120.5 |
0.5993 |
323.15 |
1100.75 |
0.6994 |
293.15 |
1218.82 |
0.6994 |
298.15 |
1198.45 |
0.6994 |
303.15 |
1178.1 |
0.6994 |
308.15 |
1157.82 |
0.6994 |
313.15 |
1137.61 |
0.6994 |
318.16 |
1117.43 |
0.6994 |
323.16 |
1097.31 |
0.7995 |
293.15 |
1217.75 |
0.7995 |
298.15 |
1197.05 |
0.7995 |
303.15 |
1176.35 |
0.7995 |
308.15 |
1155.72 |
0.7995 |
313.15 |
1135.15 |
0.7995 |
318.15 |
1114.61 |
0.7995 |
323.15 |
1094.15 |
0.8990 |
293.15 |
1215.98 |
0.8990 |
298.15 |
1194.93 |
0.8990 |
303.15 |
1173.85 |
0.8990 |
308.15 |
1152.85 |
0.8990 |
313.15 |
1131.94 |
0.8990 |
318.15 |
1111.1 |
0.8990 |
323.16 |
1090.29 |
1.0000 |
293.15 |
1213.35 |
1.0000 |
298.15 |
1192.06 |
1.0000 |
303.15 |
1170.77 |
1.0000 |
308.15 |
1149.56 |
1.0000 |
313.15 |
1128.44 |
1.0000 |
318.15 |
1107.39 |
1.0000 |
323.15 |
1086.41 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 2-Butanone (2) - Gas |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
20.00 |
332.67 |
0.0000 |
101.30 |
370.21 |
0.0820 |
101.30 |
368.67 |
0.1310 |
101.30 |
367.82 |
0.1440 |
20.00 |
330.55 |
0.1880 |
101.30 |
366.95 |
0.2700 |
101.30 |
365.44 |
0.2820 |
20.00 |
327.89 |
0.3120 |
101.30 |
364.86 |
0.3780 |
20.00 |
325.75 |
0.3810 |
101.30 |
363.13 |
0.4280 |
101.30 |
362.27 |
0.4490 |
20.00 |
323.80 |
0.5110 |
101.30 |
360.69 |
0.5310 |
20.00 |
322.14 |
0.5500 |
101.30 |
359.79 |
0.5920 |
20.00 |
320.54 |
0.6060 |
101.30 |
358.77 |
0.6210 |
20.00 |
319.16 |
0.6410 |
101.30 |
358.07 |
0.6670 |
20.00 |
317.91 |
0.6900 |
101.30 |
357.07 |
0.7150 |
20.00 |
316.81 |
0.7260 |
101.30 |
356.37 |
0.7410 |
20.00 |
315.87 |
0.7450 |
101.30 |
356.06 |
0.7720 |
20.00 |
315.03 |
0.7890 |
20.00 |
314.37 |
0.7960 |
101.30 |
355.20 |
0.8130 |
20.00 |
313.67 |
0.8360 |
101.30 |
354.60 |
0.8410 |
20.00 |
312.99 |
0.8680 |
20.00 |
312.37 |
0.8760 |
101.30 |
354.06 |
0.8990 |
20.00 |
311.76 |
0.9170 |
20.00 |
311.17 |
0.9180 |
101.30 |
353.54 |
0.9460 |
20.00 |
310.61 |
0.9610 |
101.30 |
353.15 |
0.9770 |
20.00 |
310.07 |
1.0000 |
20.00 |
309.55 |
1.0000 |
101.30 |
352.68 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 2-Butanone (2) - Gas |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0000 |
20.00 |
332.67 |
0.0000 |
101.30 |
370.21 |
0.0820 |
101.30 |
368.67 |
0.1310 |
101.30 |
367.82 |
0.1440 |
20.00 |
330.55 |
0.1880 |
101.30 |
366.95 |
0.2700 |
101.30 |
365.44 |
0.2820 |
20.00 |
327.89 |
0.3120 |
101.30 |
364.86 |
0.3780 |
20.00 |
325.75 |
0.3810 |
101.30 |
363.13 |
0.4280 |
101.30 |
362.27 |
0.4490 |
20.00 |
323.80 |
0.5110 |
101.30 |
360.69 |
0.5310 |
20.00 |
322.14 |
0.5500 |
101.30 |
359.79 |
0.5920 |
20.00 |
320.54 |
0.6060 |
101.30 |
358.77 |
0.6210 |
20.00 |
319.16 |
0.6410 |
101.30 |
358.07 |
0.6670 |
20.00 |
317.91 |
0.6900 |
101.30 |
357.07 |
0.7150 |
20.00 |
316.81 |
0.7260 |
101.30 |
356.37 |
0.7410 |
20.00 |
315.87 |
0.7450 |
101.30 |
356.06 |
0.7720 |
20.00 |
315.03 |
0.7890 |
20.00 |
314.37 |
0.7960 |
101.30 |
355.20 |
0.8130 |
20.00 |
313.67 |
0.8360 |
101.30 |
354.60 |
0.8410 |
20.00 |
312.99 |
0.8680 |
20.00 |
312.37 |
0.8760 |
101.30 |
354.06 |
0.8990 |
20.00 |
311.76 |
0.9170 |
20.00 |
311.17 |
0.9180 |
101.30 |
353.54 |
0.9460 |
20.00 |
310.61 |
0.9610 |
101.30 |
353.15 |
0.9770 |
20.00 |
310.07 |
1.0000 |
20.00 |
309.55 |
1.0000 |
101.30 |
352.68 |
Sources