Operational conditions:
| Temperature, K - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
|---|---|
| 303.15 | 68.03 |
| 308.15 | 68.43 |
| 313.15 | 68.83 |
| 318.15 | 69.33 |
| 323.15 | 69.83 |
| 328.15 | 70.36 |
| 333.15 | 71.03 |
| 338.15 | 71.53 |
| 343.15 | 72.09 |
| 348.15 | 72.69 |
| 353.15 | 73.26 |
Operational conditions:
| Temperature, K - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
|---|---|
| 303.15 | 68.03 |
| 308.15 | 68.43 |
| 313.15 | 68.83 |
| 318.15 | 69.33 |
| 323.15 | 69.83 |
| 328.15 | 70.36 |
| 333.15 | 71.03 |
| 338.15 | 71.53 |
| 343.15 | 72.09 |
| 348.15 | 72.69 |
| 353.15 | 73.26 |
Operational conditions:
| Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 298.15 | 0.0504 |
| 303.15 | 0.0407 |
| 308.15 | 0.0320 |
| 313.15 | 0.0263 |
| 318.15 | 0.0220 |
| 323.15 | 0.0185 |
| 328.15 | 0.0158 |
| 333.15 | 0.0135 |
| 338.15 | 0.0115 |
| 343.15 | 0.0100 |
Operational conditions:
| Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
|---|---|
| 298.15 | 0.0504 |
| 303.15 | 0.0407 |
| 308.15 | 0.0320 |
| 313.15 | 0.0263 |
| 318.15 | 0.0220 |
| 323.15 | 0.0185 |
| 328.15 | 0.0158 |
| 333.15 | 0.0135 |
| 338.15 | 0.0115 |
| 343.15 | 0.0100 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Electrical conductivity, S/m - Liquid |
| 298.15 | 0.3400 | 0.5120 |
| 303.15 | 0.3400 | 0.6627 |
| 308.15 | 0.3400 | 0.7940 |
| 313.15 | 0.3400 | 0.9283 |
| 318.15 | 0.3400 | 1.0955 |
| 323.15 | 0.3400 | 1.2539 |
| 328.15 | 0.3400 | 1.433 |
| 333.15 | 0.3400 | 1.6161 |
| 338.15 | 0.3400 | 1.7779 |
| 343.15 | 0.3400 | 1.9417 |
| 348.15 | 0.3400 | 2.1347 |
| 353.15 | 0.3400 | 2.3097 |
| 298.15 | 0.2500 | 0.5429 |
| 303.15 | 0.2500 | 0.6878 |
| 308.15 | 0.2500 | 0.8305 |
| 313.15 | 0.2500 | 0.9486 |
| 318.15 | 0.2500 | 1.1339 |
| 323.15 | 0.2500 | 1.3147 |
| 328.15 | 0.2500 | 1.4769 |
| 333.15 | 0.2500 | 1.6664 |
| 338.15 | 0.2500 | 1.8395 |
| 343.15 | 0.2500 | 1.99 |
| 348.15 | 0.2500 | 2.1924 |
| 353.15 | 0.2500 | 2.3667 |
| 298.15 | 0.2000 | 0.5661 |
| 303.15 | 0.2000 | 0.6994 |
| 308.15 | 0.2000 | 0.8245 |
| 313.15 | 0.2000 | 0.9699 |
| 318.15 | 0.2000 | 1.1579 |
| 323.15 | 0.2000 | 1.3408 |
| 328.15 | 0.2000 | 1.5086 |
| 333.15 | 0.2000 | 1.7137 |
| 338.15 | 0.2000 | 1.8755 |
| 343.15 | 0.2000 | 2.0286 |
| 348.15 | 0.2000 | 2.2262 |
| 353.15 | 0.2000 | 2.4053 |
Operational conditions:
| Temperature, K - Liquid | Electrical conductivity, S/m - Liquid |
|---|---|
| 298.15 | 0.4700 |
| 303.15 | 0.5650 |
| 308.15 | 0.6800 |
| 313.15 | 0.8100 |
| 318.15 | 0.9600 |
| 323.15 | 1.12 |
| 328.15 | 1.29 |
| 333.15 | 1.48 |
| 338.15 | 1.68 |
| 343.15 | 1.88 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Electrical conductivity, S/m - Liquid |
| 298.15 | 0.3400 | 0.5120 |
| 303.15 | 0.3400 | 0.6627 |
| 308.15 | 0.3400 | 0.7940 |
| 313.15 | 0.3400 | 0.9283 |
| 318.15 | 0.3400 | 1.0955 |
| 323.15 | 0.3400 | 1.2539 |
| 328.15 | 0.3400 | 1.433 |
| 333.15 | 0.3400 | 1.6161 |
| 338.15 | 0.3400 | 1.7779 |
| 343.15 | 0.3400 | 1.9417 |
| 348.15 | 0.3400 | 2.1347 |
| 353.15 | 0.3400 | 2.3097 |
| 298.15 | 0.2500 | 0.5429 |
| 303.15 | 0.2500 | 0.6878 |
| 308.15 | 0.2500 | 0.8305 |
| 313.15 | 0.2500 | 0.9486 |
| 318.15 | 0.2500 | 1.1339 |
| 323.15 | 0.2500 | 1.3147 |
| 328.15 | 0.2500 | 1.4769 |
| 333.15 | 0.2500 | 1.6664 |
| 338.15 | 0.2500 | 1.8395 |
| 343.15 | 0.2500 | 1.99 |
| 348.15 | 0.2500 | 2.1924 |
| 353.15 | 0.2500 | 2.3667 |
| 298.15 | 0.2000 | 0.5661 |
| 303.15 | 0.2000 | 0.6994 |
| 308.15 | 0.2000 | 0.8245 |
| 313.15 | 0.2000 | 0.9699 |
| 318.15 | 0.2000 | 1.1579 |
| 323.15 | 0.2000 | 1.3408 |
| 328.15 | 0.2000 | 1.5086 |
| 333.15 | 0.2000 | 1.7137 |
| 338.15 | 0.2000 | 1.8755 |
| 343.15 | 0.2000 | 2.0286 |
| 348.15 | 0.2000 | 2.2262 |
| 353.15 | 0.2000 | 2.4053 |
Operational conditions:
| Temperature, K - Liquid | Electrical conductivity, S/m - Liquid |
|---|---|
| 298.15 | 0.4700 |
| 303.15 | 0.5650 |
| 308.15 | 0.6800 |
| 313.15 | 0.8100 |
| 318.15 | 0.9600 |
| 323.15 | 1.12 |
| 328.15 | 1.29 |
| 333.15 | 1.48 |
| 338.15 | 1.68 |
| 343.15 | 1.88 |
Operational conditions:
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.2800 | 1.465 |
| 0.2500 | 1.462 |
| 0.2000 | 1.4574 |
Operational conditions:
| Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 298.15 | 1.4677 |
| 303.15 | 1.4663 |
| 308.15 | 1.465 |
| 313.15 | 1.4636 |
| 318.15 | 1.4619 |
| 323.15 | 1.4605 |
| 328.15 | 1.4594 |
| 333.15 | 1.4577 |
| 338.15 | 1.4566 |
| 343.15 | 1.4553 |
Operational conditions:
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.2800 | 1.465 |
| 0.2500 | 1.462 |
| 0.2000 | 1.4574 |
Operational conditions:
| Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 298.15 | 1.4677 |
| 303.15 | 1.4663 |
| 308.15 | 1.465 |
| 313.15 | 1.4636 |
| 318.15 | 1.4619 |
| 323.15 | 1.4605 |
| 328.15 | 1.4594 |
| 333.15 | 1.4577 |
| 338.15 | 1.4566 |
| 343.15 | 1.4553 |
Operational conditions:
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.2800 | 1100.6 |
| 0.2500 | 1101.8 |
| 0.2000 | 1103.7 |
Operational conditions:
| Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 298.15 | 1099.9 |
| 303.15 | 1096.8 |
| 308.15 | 1093.8 |
| 313.15 | 1090.9 |
| 318.15 | 1087.9 |
| 323.15 | 1084.8 |
| 328.15 | 1081.8 |
| 333.15 | 1078.8 |
| 338.15 | 1075.9 |
| 343.15 | 1072.8 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.2000 | 298.15 | 1103.7 |
| 0.2000 | 303.15 | 1100.4 |
| 0.2000 | 308.15 | 1097.3 |
| 0.2000 | 313.15 | 1094.2 |
| 0.2000 | 318.15 | 1091.0 |
| 0.2000 | 323.15 | 1087.7 |
| 0.2000 | 328.15 | 1084.6 |
| 0.2000 | 333.15 | 1081.5 |
| 0.2000 | 338.15 | 1078.2 |
| 0.2000 | 343.15 | 1075.0 |
| 0.2000 | 348.15 | 1071.8 |
| 0.2000 | 353.15 | 1068.3 |
| 0.2000 | 358.15 | 1065.4 |
| 0.2000 | 363.15 | 1062.2 |
| 0.2000 | 368.15 | 1059.0 |
| 0.2500 | 303.15 | 1098.6 |
| 0.2500 | 313.15 | 1092.6 |
| 0.2500 | 323.15 | 1086.2 |
| 0.2500 | 333.15 | 1079.7 |
| 0.2500 | 343.15 | 1074.0 |
| 0.2500 | 353.15 | 1067.5 |
| 0.2500 | 363.15 | 1060.0 |
| 0.3300 | 298.15 | 1099.5 |
| 0.3300 | 303.15 | 1096.5 |
| 0.3300 | 308.15 | 1093.3 |
| 0.3300 | 313.15 | 1090.3 |
| 0.3300 | 318.15 | 1087.1 |
| 0.3300 | 323.15 | 1084.0 |
| 0.3300 | 328.15 | 1080.9 |
| 0.3300 | 333.15 | 1077.8 |
| 0.3300 | 338.15 | 1074.8 |
| 0.3300 | 343.15 | 1071.7 |
| 0.3300 | 348.15 | 1068.6 |
| 0.3300 | 353.15 | 1065.5 |
| 0.3300 | 358.15 | 1062.4 |
| 0.3300 | 363.15 | 1059.0 |
| 0.3300 | 368.15 | 1056.2 |
Operational conditions:
| Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 298.15 | 1100.0 |
| 303.15 | 1097.0 |
| 308.15 | 1093.0 |
| 313.15 | 1090.0 |
| 318.15 | 1087.0 |
| 323.15 | 1084.0 |
| 328.15 | 1081.0 |
Operational conditions:
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.2800 | 1100.6 |
| 0.2500 | 1101.8 |
| 0.2000 | 1103.7 |
Operational conditions:
| Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 298.15 | 1099.9 |
| 303.15 | 1096.8 |
| 308.15 | 1093.8 |
| 313.15 | 1090.9 |
| 318.15 | 1087.9 |
| 323.15 | 1084.8 |
| 328.15 | 1081.8 |
| 333.15 | 1078.8 |
| 338.15 | 1075.9 |
| 343.15 | 1072.8 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.2000 | 298.15 | 1103.7 |
| 0.2000 | 303.15 | 1100.4 |
| 0.2000 | 308.15 | 1097.3 |
| 0.2000 | 313.15 | 1094.2 |
| 0.2000 | 318.15 | 1091.0 |
| 0.2000 | 323.15 | 1087.7 |
| 0.2000 | 328.15 | 1084.6 |
| 0.2000 | 333.15 | 1081.5 |
| 0.2000 | 338.15 | 1078.2 |
| 0.2000 | 343.15 | 1075.0 |
| 0.2000 | 348.15 | 1071.8 |
| 0.2000 | 353.15 | 1068.3 |
| 0.2000 | 358.15 | 1065.4 |
| 0.2000 | 363.15 | 1062.2 |
| 0.2000 | 368.15 | 1059.0 |
| 0.2500 | 303.15 | 1098.6 |
| 0.2500 | 313.15 | 1092.6 |
| 0.2500 | 323.15 | 1086.2 |
| 0.2500 | 333.15 | 1079.7 |
| 0.2500 | 343.15 | 1074.0 |
| 0.2500 | 353.15 | 1067.5 |
| 0.2500 | 363.15 | 1060.0 |
| 0.3300 | 298.15 | 1099.5 |
| 0.3300 | 303.15 | 1096.5 |
| 0.3300 | 308.15 | 1093.3 |
| 0.3300 | 313.15 | 1090.3 |
| 0.3300 | 318.15 | 1087.1 |
| 0.3300 | 323.15 | 1084.0 |
| 0.3300 | 328.15 | 1080.9 |
| 0.3300 | 333.15 | 1077.8 |
| 0.3300 | 338.15 | 1074.8 |
| 0.3300 | 343.15 | 1071.7 |
| 0.3300 | 348.15 | 1068.6 |
| 0.3300 | 353.15 | 1065.5 |
| 0.3300 | 358.15 | 1062.4 |
| 0.3300 | 363.15 | 1059.0 |
| 0.3300 | 368.15 | 1056.2 |
Operational conditions:
| Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 298.15 | 1100.0 |
| 303.15 | 1097.0 |
| 308.15 | 1093.0 |
| 313.15 | 1090.0 |
| 318.15 | 1087.0 |
| 323.15 | 1084.0 |
| 328.15 | 1081.0 |
Operational condition: Mole fraction = 0.25 (Liquid)
| Temperature, K - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 298.15 | 0.0513 |
| 303.15 | 0.0507 |
| 308.15 | 0.0502 |
| 313.15 | 0.0496 |
| 318.15 | 0.0491 |
| 323.15 | 0.0487 |
| 328.15 | 0.0481 |
Operational condition: Mole fraction = 0.25 (Liquid)
| Temperature, K - Liquid | Surface tension liquid-gas, N/m - Liquid |
|---|---|
| 298.15 | 0.0513 |
| 303.15 | 0.0507 |
| 308.15 | 0.0502 |
| 313.15 | 0.0496 |
| 318.15 | 0.0491 |
| 323.15 | 0.0487 |
| 328.15 | 0.0481 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.2800 | 240.03 |
| 0.2500 | 250.90 |
| 0.2000 | 251.48 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.2800 | 240.03 |
| 0.2500 | 250.90 |
| 0.2000 | 251.48 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.3300 | 242.12 |
| 0.2500 | 250.90 |
| 0.2000 | 251.48 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.2800 | 240.03 |
| 0.2500 | 250.90 |
| 0.2000 | 251.48 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.2800 | 240.03 |
| 0.2500 | 250.90 |
| 0.2000 | 251.48 |
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-diethylamino-, hydrochloride (2) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.3300 | 242.12 |
| 0.2500 | 250.90 |
| 0.2000 | 251.48 |