Datasets
-
Mole fraction (2)
-
ρl - Mass density, kg/m3 (2)
-
csound,fluid - Speed of Sound, m/s (2)
Mole fraction of Acetic acid, methyl ester (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Acetic acid, methyl ester (1) - Liquid |
Mole fraction of Acetic acid, methyl ester (1) - Gas |
| 330.50 |
1.0000 |
1.0000 |
| 331.00 |
0.9909 |
0.9987 |
| 331.50 |
0.9699 |
0.9954 |
| 332.10 |
0.9468 |
0.9923 |
| 332.60 |
0.9244 |
0.9892 |
| 333.40 |
0.8900 |
0.9845 |
| 334.10 |
0.8624 |
0.9818 |
| 334.70 |
0.8370 |
0.9786 |
| 336.50 |
0.7657 |
0.9687 |
| 337.30 |
0.7343 |
0.9639 |
| 338.40 |
0.6973 |
0.9586 |
| 338.60 |
0.6898 |
0.9572 |
| 339.40 |
0.6653 |
0.9528 |
| 340.80 |
0.6223 |
0.9437 |
| 340.70 |
0.6244 |
0.9444 |
| 343.10 |
0.5596 |
0.9286 |
| 345.10 |
0.5111 |
0.9157 |
| 349.10 |
0.4275 |
0.8851 |
| 351.70 |
0.3803 |
0.8619 |
| 353.90 |
0.3449 |
0.8406 |
| 357.70 |
0.2858 |
0.7930 |
| 364.40 |
0.2265 |
0.7213 |
| 368.20 |
0.1728 |
0.6481 |
| 373.60 |
0.1261 |
0.5404 |
| 379.20 |
0.0836 |
0.4128 |
| 380.90 |
0.0717 |
0.3698 |
| 384.10 |
0.0511 |
0.2862 |
| 388.20 |
0.0260 |
0.1611 |
| 390.10 |
0.0153 |
0.0991 |
| 392.90 |
0.0004 |
0.0033 |
| 393.30 |
0.0000 |
0.0000 |
Mole fraction of Acetic acid, methyl ester (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Acetic acid, methyl ester (1) - Liquid |
Mole fraction of Acetic acid, methyl ester (1) - Gas |
| 330.50 |
1.0000 |
1.0000 |
| 331.00 |
0.9909 |
0.9987 |
| 331.50 |
0.9699 |
0.9954 |
| 332.10 |
0.9468 |
0.9923 |
| 332.60 |
0.9244 |
0.9892 |
| 333.40 |
0.8900 |
0.9845 |
| 334.10 |
0.8624 |
0.9818 |
| 334.70 |
0.8370 |
0.9786 |
| 336.50 |
0.7657 |
0.9687 |
| 337.30 |
0.7343 |
0.9639 |
| 338.40 |
0.6973 |
0.9586 |
| 338.60 |
0.6898 |
0.9572 |
| 339.40 |
0.6653 |
0.9528 |
| 340.80 |
0.6223 |
0.9437 |
| 340.70 |
0.6244 |
0.9444 |
| 343.10 |
0.5596 |
0.9286 |
| 345.10 |
0.5111 |
0.9157 |
| 349.10 |
0.4275 |
0.8851 |
| 351.70 |
0.3803 |
0.8619 |
| 353.90 |
0.3449 |
0.8406 |
| 357.70 |
0.2858 |
0.7930 |
| 364.40 |
0.2265 |
0.7213 |
| 368.20 |
0.1728 |
0.6481 |
| 373.60 |
0.1261 |
0.5404 |
| 379.20 |
0.0836 |
0.4128 |
| 380.90 |
0.0717 |
0.3698 |
| 384.10 |
0.0511 |
0.2862 |
| 388.20 |
0.0260 |
0.1611 |
| 390.10 |
0.0153 |
0.0991 |
| 392.90 |
0.0004 |
0.0033 |
| 393.30 |
0.0000 |
0.0000 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Mass density, kg/m3 - Liquid |
| 288.15 |
0.0000 |
940.883 |
| 288.15 |
0.0207 |
940.053 |
| 288.15 |
0.0464 |
939.345 |
| 288.15 |
0.1088 |
937.89 |
| 288.15 |
0.1939 |
935.816 |
| 288.15 |
0.2843 |
933.707 |
| 288.15 |
0.3772 |
932.0 |
| 288.15 |
0.4897 |
930.444 |
| 288.15 |
0.5760 |
929.443 |
| 288.15 |
0.7024 |
928.089 |
| 288.15 |
0.7922 |
927.337 |
| 288.15 |
0.8772 |
926.778 |
| 288.15 |
0.9355 |
926.432 |
| 288.15 |
0.9667 |
926.133 |
| 288.15 |
1.0000 |
925.9 |
| 293.15 |
0.0000 |
934.389 |
| 293.15 |
0.0207 |
933.582 |
| 293.15 |
0.0464 |
932.934 |
| 293.15 |
0.1088 |
931.615 |
| 293.15 |
0.1939 |
929.703 |
| 293.15 |
0.2843 |
927.777 |
| 293.15 |
0.3772 |
926.311 |
| 293.15 |
0.4897 |
925.001 |
| 293.15 |
0.5760 |
924.044 |
| 293.15 |
0.7024 |
922.902 |
| 293.15 |
0.7922 |
922.299 |
| 293.15 |
0.8772 |
921.881 |
| 293.15 |
0.9355 |
921.626 |
| 293.15 |
0.9667 |
921.378 |
| 293.15 |
1.0000 |
921.196 |
| 298.15 |
0.0000 |
927.817 |
| 298.15 |
0.0207 |
927.069 |
| 298.15 |
0.0464 |
926.466 |
| 298.15 |
0.1088 |
925.284 |
| 298.15 |
0.1939 |
923.547 |
| 298.15 |
0.2843 |
921.803 |
| 298.15 |
0.3772 |
920.59 |
| 298.15 |
0.4897 |
919.404 |
| 298.15 |
0.5760 |
918.604 |
| 298.15 |
0.7024 |
917.676 |
| 298.15 |
0.7922 |
917.224 |
| 298.15 |
0.8772 |
916.944 |
| 298.15 |
0.9355 |
916.78 |
| 298.15 |
0.9667 |
916.583 |
| 298.15 |
1.0000 |
916.449 |
| 303.15 |
0.0000 |
921.188 |
| 303.15 |
0.0207 |
920.495 |
| 303.15 |
0.0464 |
919.946 |
| 303.15 |
0.1088 |
918.901 |
| 303.15 |
0.1939 |
917.338 |
| 303.15 |
0.2843 |
915.78 |
| 303.15 |
0.3772 |
914.766 |
| 303.15 |
0.4897 |
913.8 |
| 303.15 |
0.5760 |
913.22 |
| 303.15 |
0.7024 |
912.405 |
| 303.15 |
0.7922 |
912.101 |
| 303.15 |
0.8772 |
911.965 |
| 303.15 |
0.9355 |
911.892 |
| 303.15 |
0.9667 |
911.739 |
| 303.15 |
1.0000 |
911.655 |
| 308.15 |
0.0000 |
914.498 |
| 308.15 |
0.0207 |
913.861 |
| 308.15 |
0.0464 |
913.38 |
| 308.15 |
0.1088 |
912.46 |
| 308.15 |
0.1939 |
911.075 |
| 308.15 |
0.2843 |
909.706 |
| 308.15 |
0.3772 |
908.911 |
| 308.15 |
0.4897 |
908.176 |
| 308.15 |
0.5760 |
907.711 |
| 308.15 |
0.7024 |
907.151 |
| 308.15 |
0.7922 |
906.934 |
| 308.15 |
0.8772 |
906.94 |
| 308.15 |
0.9355 |
906.957 |
| 308.15 |
0.9667 |
906.849 |
| 308.15 |
1.0000 |
906.816 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Mass density, kg/m3 - Liquid |
| 288.15 |
0.0000 |
940.883 |
| 288.15 |
0.0207 |
940.053 |
| 288.15 |
0.0464 |
939.345 |
| 288.15 |
0.1088 |
937.89 |
| 288.15 |
0.1939 |
935.816 |
| 288.15 |
0.2843 |
933.707 |
| 288.15 |
0.3772 |
932.0 |
| 288.15 |
0.4897 |
930.444 |
| 288.15 |
0.5760 |
929.443 |
| 288.15 |
0.7024 |
928.089 |
| 288.15 |
0.7922 |
927.337 |
| 288.15 |
0.8772 |
926.778 |
| 288.15 |
0.9355 |
926.432 |
| 288.15 |
0.9667 |
926.133 |
| 288.15 |
1.0000 |
925.9 |
| 293.15 |
0.0000 |
934.389 |
| 293.15 |
0.0207 |
933.582 |
| 293.15 |
0.0464 |
932.934 |
| 293.15 |
0.1088 |
931.615 |
| 293.15 |
0.1939 |
929.703 |
| 293.15 |
0.2843 |
927.777 |
| 293.15 |
0.3772 |
926.311 |
| 293.15 |
0.4897 |
925.001 |
| 293.15 |
0.5760 |
924.044 |
| 293.15 |
0.7024 |
922.902 |
| 293.15 |
0.7922 |
922.299 |
| 293.15 |
0.8772 |
921.881 |
| 293.15 |
0.9355 |
921.626 |
| 293.15 |
0.9667 |
921.378 |
| 293.15 |
1.0000 |
921.196 |
| 298.15 |
0.0000 |
927.817 |
| 298.15 |
0.0207 |
927.069 |
| 298.15 |
0.0464 |
926.466 |
| 298.15 |
0.1088 |
925.284 |
| 298.15 |
0.1939 |
923.547 |
| 298.15 |
0.2843 |
921.803 |
| 298.15 |
0.3772 |
920.59 |
| 298.15 |
0.4897 |
919.404 |
| 298.15 |
0.5760 |
918.604 |
| 298.15 |
0.7024 |
917.676 |
| 298.15 |
0.7922 |
917.224 |
| 298.15 |
0.8772 |
916.944 |
| 298.15 |
0.9355 |
916.78 |
| 298.15 |
0.9667 |
916.583 |
| 298.15 |
1.0000 |
916.449 |
| 303.15 |
0.0000 |
921.188 |
| 303.15 |
0.0207 |
920.495 |
| 303.15 |
0.0464 |
919.946 |
| 303.15 |
0.1088 |
918.901 |
| 303.15 |
0.1939 |
917.338 |
| 303.15 |
0.2843 |
915.78 |
| 303.15 |
0.3772 |
914.766 |
| 303.15 |
0.4897 |
913.8 |
| 303.15 |
0.5760 |
913.22 |
| 303.15 |
0.7024 |
912.405 |
| 303.15 |
0.7922 |
912.101 |
| 303.15 |
0.8772 |
911.965 |
| 303.15 |
0.9355 |
911.892 |
| 303.15 |
0.9667 |
911.739 |
| 303.15 |
1.0000 |
911.655 |
| 308.15 |
0.0000 |
914.498 |
| 308.15 |
0.0207 |
913.861 |
| 308.15 |
0.0464 |
913.38 |
| 308.15 |
0.1088 |
912.46 |
| 308.15 |
0.1939 |
911.075 |
| 308.15 |
0.2843 |
909.706 |
| 308.15 |
0.3772 |
908.911 |
| 308.15 |
0.4897 |
908.176 |
| 308.15 |
0.5760 |
907.711 |
| 308.15 |
0.7024 |
907.151 |
| 308.15 |
0.7922 |
906.934 |
| 308.15 |
0.8772 |
906.94 |
| 308.15 |
0.9355 |
906.957 |
| 308.15 |
0.9667 |
906.849 |
| 308.15 |
1.0000 |
906.816 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Speed of sound, m/s - Liquid |
| 288.15 |
0.0000 |
1200.38 |
| 288.15 |
0.0207 |
1202.73 |
| 288.15 |
0.0464 |
1204.44 |
| 288.15 |
0.1088 |
1209.23 |
| 288.15 |
0.1939 |
1215.18 |
| 288.15 |
0.2843 |
1221.96 |
| 288.15 |
0.3772 |
1229.5 |
| 288.15 |
0.4897 |
1240.5 |
| 288.15 |
0.5760 |
1249.8 |
| 288.15 |
0.7024 |
1263.31 |
| 288.15 |
0.7922 |
1273.63 |
| 288.15 |
0.8772 |
1284.13 |
| 288.15 |
0.9355 |
1291.02 |
| 288.15 |
0.9667 |
1294.47 |
| 288.15 |
1.0000 |
1298.14 |
| 293.15 |
0.0000 |
1178.95 |
| 293.15 |
0.0207 |
1180.34 |
| 293.15 |
0.0464 |
1182.35 |
| 293.15 |
0.1088 |
1187.72 |
| 293.15 |
0.1939 |
1193.7 |
| 293.15 |
0.2843 |
1200.89 |
| 293.15 |
0.3772 |
1209.01 |
| 293.15 |
0.4897 |
1220.8 |
| 293.15 |
0.5760 |
1230.25 |
| 293.15 |
0.7024 |
1244.0 |
| 293.15 |
0.7922 |
1254.7 |
| 293.15 |
0.8772 |
1265.55 |
| 293.15 |
0.9355 |
1272.67 |
| 293.15 |
0.9667 |
1276.26 |
| 293.15 |
1.0000 |
1280.08 |
| 298.15 |
0.0000 |
1155.93 |
| 298.15 |
0.0207 |
1157.5 |
| 298.15 |
0.0464 |
1159.18 |
| 298.15 |
0.1088 |
1165.35 |
| 298.15 |
0.1939 |
1171.76 |
| 298.15 |
0.2843 |
1179.38 |
| 298.15 |
0.3772 |
1188.04 |
| 298.15 |
0.4897 |
1200.02 |
| 298.15 |
0.5760 |
1209.99 |
| 298.15 |
0.7024 |
1224.24 |
| 298.15 |
0.7922 |
1235.33 |
| 298.15 |
0.8772 |
1246.5 |
| 298.15 |
0.9355 |
1253.87 |
| 298.15 |
0.9667 |
1257.61 |
| 298.15 |
1.0000 |
1261.54 |
| 303.15 |
0.0000 |
1132.98 |
| 303.15 |
0.0207 |
1134.72 |
| 303.15 |
0.0464 |
1136.54 |
| 303.15 |
0.1088 |
1143.03 |
| 303.15 |
0.1939 |
1149.87 |
| 303.15 |
0.2843 |
1157.93 |
| 303.15 |
0.3772 |
1166.79 |
| 303.15 |
0.4897 |
1179.4 |
| 303.15 |
0.5760 |
1189.68 |
| 303.15 |
0.7024 |
1204.55 |
| 303.15 |
0.7922 |
1215.98 |
| 303.15 |
0.8772 |
1227.52 |
| 303.15 |
0.9355 |
1235.14 |
| 303.15 |
0.9667 |
1238.97 |
| 303.15 |
1.0000 |
1243.03 |
| 308.15 |
0.0000 |
1110.02 |
| 308.15 |
0.0207 |
1111.93 |
| 308.15 |
0.0464 |
1114.41 |
| 308.15 |
0.1088 |
1120.75 |
| 308.15 |
0.1939 |
1128.01 |
| 308.15 |
0.2843 |
1136.48 |
| 308.15 |
0.3772 |
1145.5 |
| 308.15 |
0.4897 |
1159.01 |
| 308.15 |
0.5760 |
1169.61 |
| 308.15 |
0.7024 |
1184.88 |
| 308.15 |
0.7922 |
1196.66 |
| 308.15 |
0.8772 |
1208.53 |
| 308.15 |
0.9355 |
1216.39 |
| 308.15 |
0.9667 |
1220.3 |
| 308.15 |
1.0000 |
1224.5 |
Speed of sound, m/s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Speed of sound, m/s - Liquid |
| 288.15 |
0.0000 |
1200.38 |
| 288.15 |
0.0207 |
1202.73 |
| 288.15 |
0.0464 |
1204.44 |
| 288.15 |
0.1088 |
1209.23 |
| 288.15 |
0.1939 |
1215.18 |
| 288.15 |
0.2843 |
1221.96 |
| 288.15 |
0.3772 |
1229.5 |
| 288.15 |
0.4897 |
1240.5 |
| 288.15 |
0.5760 |
1249.8 |
| 288.15 |
0.7024 |
1263.31 |
| 288.15 |
0.7922 |
1273.63 |
| 288.15 |
0.8772 |
1284.13 |
| 288.15 |
0.9355 |
1291.02 |
| 288.15 |
0.9667 |
1294.47 |
| 288.15 |
1.0000 |
1298.14 |
| 293.15 |
0.0000 |
1178.95 |
| 293.15 |
0.0207 |
1180.34 |
| 293.15 |
0.0464 |
1182.35 |
| 293.15 |
0.1088 |
1187.72 |
| 293.15 |
0.1939 |
1193.7 |
| 293.15 |
0.2843 |
1200.89 |
| 293.15 |
0.3772 |
1209.01 |
| 293.15 |
0.4897 |
1220.8 |
| 293.15 |
0.5760 |
1230.25 |
| 293.15 |
0.7024 |
1244.0 |
| 293.15 |
0.7922 |
1254.7 |
| 293.15 |
0.8772 |
1265.55 |
| 293.15 |
0.9355 |
1272.67 |
| 293.15 |
0.9667 |
1276.26 |
| 293.15 |
1.0000 |
1280.08 |
| 298.15 |
0.0000 |
1155.93 |
| 298.15 |
0.0207 |
1157.5 |
| 298.15 |
0.0464 |
1159.18 |
| 298.15 |
0.1088 |
1165.35 |
| 298.15 |
0.1939 |
1171.76 |
| 298.15 |
0.2843 |
1179.38 |
| 298.15 |
0.3772 |
1188.04 |
| 298.15 |
0.4897 |
1200.02 |
| 298.15 |
0.5760 |
1209.99 |
| 298.15 |
0.7024 |
1224.24 |
| 298.15 |
0.7922 |
1235.33 |
| 298.15 |
0.8772 |
1246.5 |
| 298.15 |
0.9355 |
1253.87 |
| 298.15 |
0.9667 |
1257.61 |
| 298.15 |
1.0000 |
1261.54 |
| 303.15 |
0.0000 |
1132.98 |
| 303.15 |
0.0207 |
1134.72 |
| 303.15 |
0.0464 |
1136.54 |
| 303.15 |
0.1088 |
1143.03 |
| 303.15 |
0.1939 |
1149.87 |
| 303.15 |
0.2843 |
1157.93 |
| 303.15 |
0.3772 |
1166.79 |
| 303.15 |
0.4897 |
1179.4 |
| 303.15 |
0.5760 |
1189.68 |
| 303.15 |
0.7024 |
1204.55 |
| 303.15 |
0.7922 |
1215.98 |
| 303.15 |
0.8772 |
1227.52 |
| 303.15 |
0.9355 |
1235.14 |
| 303.15 |
0.9667 |
1238.97 |
| 303.15 |
1.0000 |
1243.03 |
| 308.15 |
0.0000 |
1110.02 |
| 308.15 |
0.0207 |
1111.93 |
| 308.15 |
0.0464 |
1114.41 |
| 308.15 |
0.1088 |
1120.75 |
| 308.15 |
0.1939 |
1128.01 |
| 308.15 |
0.2843 |
1136.48 |
| 308.15 |
0.3772 |
1145.5 |
| 308.15 |
0.4897 |
1159.01 |
| 308.15 |
0.5760 |
1169.61 |
| 308.15 |
0.7024 |
1184.88 |
| 308.15 |
0.7922 |
1196.66 |
| 308.15 |
0.8772 |
1208.53 |
| 308.15 |
0.9355 |
1216.39 |
| 308.15 |
0.9667 |
1220.3 |
| 308.15 |
1.0000 |
1224.5 |
Sources