Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.9176 |
| 293.15 | 0.0928 | 0.4919 |
| 293.15 | 0.1871 | 0.2698 |
| 293.15 | 0.2841 | 0.1532 |
| 293.15 | 0.3804 | 0.0853 |
| 293.15 | 0.4787 | 0.0501 |
| 293.15 | 0.5789 | 0.0305 |
| 293.15 | 0.6816 | 0.0188 |
| 293.15 | 0.7855 | 0.0124 |
| 293.15 | 0.8923 | 0.0085 |
| 293.15 | 1.0000 | 0.0058 |
| 303.15 | 0.0000 | 0.4047 |
| 303.15 | 0.0928 | 0.2283 |
| 303.15 | 0.1871 | 0.1266 |
| 303.15 | 0.2841 | 0.0697 |
| 303.15 | 0.3804 | 0.0419 |
| 303.15 | 0.4787 | 0.0264 |
| 303.15 | 0.5789 | 0.0175 |
| 303.15 | 0.6816 | 0.0107 |
| 303.15 | 0.7855 | 0.0082 |
| 303.15 | 0.8923 | 0.0060 |
| 303.15 | 1.0000 | 0.0042 |
| 313.15 | 0.0000 | 0.2039 |
| 313.15 | 0.0928 | 0.1126 |
| 313.15 | 0.1871 | 0.0677 |
| 313.15 | 0.2841 | 0.0408 |
| 313.15 | 0.3804 | 0.0259 |
| 313.15 | 0.4787 | 0.0164 |
| 313.15 | 0.5789 | 0.0108 |
| 313.15 | 0.6816 | 0.0074 |
| 313.15 | 0.7855 | 0.0052 |
| 313.15 | 0.8923 | 0.0040 |
| 313.15 | 1.0000 | 0.0032 |
| 323.15 | 0.0000 | 0.1083 |
| 323.15 | 0.0928 | 0.0697 |
| 323.15 | 0.1871 | 0.0444 |
| 323.15 | 0.2841 | 0.0285 |
| 323.15 | 0.3804 | 0.0176 |
| 323.15 | 0.4787 | 0.0128 |
| 323.15 | 0.5789 | 0.0088 |
| 323.15 | 0.6816 | 0.0058 |
| 323.15 | 0.7855 | 0.0043 |
| 323.15 | 0.8923 | 0.0034 |
| 323.15 | 1.0000 | 0.0025 |
| 333.15 | 0.0000 | 0.0642 |
| 333.15 | 0.0928 | 0.0435 |
| 333.15 | 0.1871 | 0.0283 |
| 333.15 | 0.2841 | 0.0184 |
| 333.15 | 0.3804 | 0.0126 |
| 333.15 | 0.4787 | 0.0090 |
| 333.15 | 0.5789 | 0.0065 |
| 333.15 | 0.6816 | 0.0047 |
| 333.15 | 0.7855 | 0.0035 |
| 333.15 | 0.8923 | 0.0027 |
| 333.15 | 1.0000 | 0.0020 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.9176 |
| 293.15 | 0.0928 | 0.4919 |
| 293.15 | 0.1871 | 0.2698 |
| 293.15 | 0.2841 | 0.1532 |
| 293.15 | 0.3804 | 0.0853 |
| 293.15 | 0.4787 | 0.0501 |
| 293.15 | 0.5789 | 0.0305 |
| 293.15 | 0.6816 | 0.0188 |
| 293.15 | 0.7855 | 0.0124 |
| 293.15 | 0.8923 | 0.0085 |
| 293.15 | 1.0000 | 0.0058 |
| 303.15 | 0.0000 | 0.4047 |
| 303.15 | 0.0928 | 0.2283 |
| 303.15 | 0.1871 | 0.1266 |
| 303.15 | 0.2841 | 0.0697 |
| 303.15 | 0.3804 | 0.0419 |
| 303.15 | 0.4787 | 0.0264 |
| 303.15 | 0.5789 | 0.0175 |
| 303.15 | 0.6816 | 0.0107 |
| 303.15 | 0.7855 | 0.0082 |
| 303.15 | 0.8923 | 0.0060 |
| 303.15 | 1.0000 | 0.0042 |
| 313.15 | 0.0000 | 0.2039 |
| 313.15 | 0.0928 | 0.1126 |
| 313.15 | 0.1871 | 0.0677 |
| 313.15 | 0.2841 | 0.0408 |
| 313.15 | 0.3804 | 0.0259 |
| 313.15 | 0.4787 | 0.0164 |
| 313.15 | 0.5789 | 0.0108 |
| 313.15 | 0.6816 | 0.0074 |
| 313.15 | 0.7855 | 0.0052 |
| 313.15 | 0.8923 | 0.0040 |
| 313.15 | 1.0000 | 0.0032 |
| 323.15 | 0.0000 | 0.1083 |
| 323.15 | 0.0928 | 0.0697 |
| 323.15 | 0.1871 | 0.0444 |
| 323.15 | 0.2841 | 0.0285 |
| 323.15 | 0.3804 | 0.0176 |
| 323.15 | 0.4787 | 0.0128 |
| 323.15 | 0.5789 | 0.0088 |
| 323.15 | 0.6816 | 0.0058 |
| 323.15 | 0.7855 | 0.0043 |
| 323.15 | 0.8923 | 0.0034 |
| 323.15 | 1.0000 | 0.0025 |
| 333.15 | 0.0000 | 0.0642 |
| 333.15 | 0.0928 | 0.0435 |
| 333.15 | 0.1871 | 0.0283 |
| 333.15 | 0.2841 | 0.0184 |
| 333.15 | 0.3804 | 0.0126 |
| 333.15 | 0.4787 | 0.0090 |
| 333.15 | 0.5789 | 0.0065 |
| 333.15 | 0.6816 | 0.0047 |
| 333.15 | 0.7855 | 0.0035 |
| 333.15 | 0.8923 | 0.0027 |
| 333.15 | 1.0000 | 0.0020 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 1124.3 |
| 293.15 | 0.0928 | 1105.1 |
| 293.15 | 0.1871 | 1086.3 |
| 293.15 | 0.2841 | 1067.9 |
| 293.15 | 0.3804 | 1050.4 |
| 293.15 | 0.4787 | 1033.3 |
| 293.15 | 0.5789 | 1016.5 |
| 293.15 | 0.6816 | 999.9 |
| 293.15 | 0.7855 | 983.9 |
| 293.15 | 0.8923 | 968.1 |
| 293.15 | 1.0000 | 952.9 |
| 303.15 | 0.0000 | 1118.5 |
| 303.15 | 0.0928 | 1098.9 |
| 303.15 | 0.1871 | 1079.9 |
| 303.15 | 0.2841 | 1061.0 |
| 303.15 | 0.3804 | 1043.1 |
| 303.15 | 0.4787 | 1025.6 |
| 303.15 | 0.5789 | 1008.5 |
| 303.15 | 0.6816 | 991.7 |
| 303.15 | 0.7855 | 975.2 |
| 303.15 | 0.8923 | 959.1 |
| 303.15 | 1.0000 | 943.5 |
| 313.15 | 0.0000 | 1112.8 |
| 313.15 | 0.0928 | 1093.1 |
| 313.15 | 0.1871 | 1073.9 |
| 313.15 | 0.2841 | 1054.8 |
| 313.15 | 0.3804 | 1036.7 |
| 313.15 | 0.4787 | 1018.9 |
| 313.15 | 0.5789 | 1001.6 |
| 313.15 | 0.6816 | 984.6 |
| 313.15 | 0.7855 | 967.9 |
| 313.15 | 0.8923 | 951.5 |
| 313.15 | 1.0000 | 935.7 |
| 323.15 | 0.0000 | 1107.1 |
| 323.15 | 0.0928 | 1087.2 |
| 323.15 | 0.1871 | 1067.5 |
| 323.15 | 0.2841 | 1048.1 |
| 323.15 | 0.3804 | 1029.5 |
| 323.15 | 0.4787 | 1011.4 |
| 323.15 | 0.5789 | 993.7 |
| 323.15 | 0.6816 | 976.4 |
| 323.15 | 0.7855 | 959.5 |
| 323.15 | 0.8923 | 942.7 |
| 323.15 | 1.0000 | 926.6 |
| 333.15 | 0.0000 | 1101.5 |
| 333.15 | 0.0928 | 1081.4 |
| 333.15 | 0.1871 | 1061.6 |
| 333.15 | 0.2841 | 1041.8 |
| 333.15 | 0.3804 | 1022.9 |
| 333.15 | 0.4787 | 1004.5 |
| 333.15 | 0.5789 | 986.6 |
| 333.15 | 0.6816 | 969.0 |
| 333.15 | 0.7855 | 951.9 |
| 333.15 | 0.8923 | 934.9 |
| 333.15 | 1.0000 | 918.5 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-(2-butoxyethoxy)- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 1124.3 |
| 293.15 | 0.0928 | 1105.1 |
| 293.15 | 0.1871 | 1086.3 |
| 293.15 | 0.2841 | 1067.9 |
| 293.15 | 0.3804 | 1050.4 |
| 293.15 | 0.4787 | 1033.3 |
| 293.15 | 0.5789 | 1016.5 |
| 293.15 | 0.6816 | 999.9 |
| 293.15 | 0.7855 | 983.9 |
| 293.15 | 0.8923 | 968.1 |
| 293.15 | 1.0000 | 952.9 |
| 303.15 | 0.0000 | 1118.5 |
| 303.15 | 0.0928 | 1098.9 |
| 303.15 | 0.1871 | 1079.9 |
| 303.15 | 0.2841 | 1061.0 |
| 303.15 | 0.3804 | 1043.1 |
| 303.15 | 0.4787 | 1025.6 |
| 303.15 | 0.5789 | 1008.5 |
| 303.15 | 0.6816 | 991.7 |
| 303.15 | 0.7855 | 975.2 |
| 303.15 | 0.8923 | 959.1 |
| 303.15 | 1.0000 | 943.5 |
| 313.15 | 0.0000 | 1112.8 |
| 313.15 | 0.0928 | 1093.1 |
| 313.15 | 0.1871 | 1073.9 |
| 313.15 | 0.2841 | 1054.8 |
| 313.15 | 0.3804 | 1036.7 |
| 313.15 | 0.4787 | 1018.9 |
| 313.15 | 0.5789 | 1001.6 |
| 313.15 | 0.6816 | 984.6 |
| 313.15 | 0.7855 | 967.9 |
| 313.15 | 0.8923 | 951.5 |
| 313.15 | 1.0000 | 935.7 |
| 323.15 | 0.0000 | 1107.1 |
| 323.15 | 0.0928 | 1087.2 |
| 323.15 | 0.1871 | 1067.5 |
| 323.15 | 0.2841 | 1048.1 |
| 323.15 | 0.3804 | 1029.5 |
| 323.15 | 0.4787 | 1011.4 |
| 323.15 | 0.5789 | 993.7 |
| 323.15 | 0.6816 | 976.4 |
| 323.15 | 0.7855 | 959.5 |
| 323.15 | 0.8923 | 942.7 |
| 323.15 | 1.0000 | 926.6 |
| 333.15 | 0.0000 | 1101.5 |
| 333.15 | 0.0928 | 1081.4 |
| 333.15 | 0.1871 | 1061.6 |
| 333.15 | 0.2841 | 1041.8 |
| 333.15 | 0.3804 | 1022.9 |
| 333.15 | 0.4787 | 1004.5 |
| 333.15 | 0.5789 | 986.6 |
| 333.15 | 0.6816 | 969.0 |
| 333.15 | 0.7855 | 951.9 |
| 333.15 | 0.8923 | 934.9 |
| 333.15 | 1.0000 | 918.5 |