Operational conditions:
Molality, mol/kg of Tributylamine (1) - Liquid | Viscosity, Pa*s - Liquid |
---|---|
0.1229 | 0.0011 |
0.2173 | 0.0010 |
0.3227 | 0.0010 |
0.4476 | 0.0010 |
0.5768 | 0.0010 |
0.7655 | 0.0010 |
0.8789 | 0.0010 |
1.0282 | 0.0010 |
1.1794 | 0.0010 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Viscosity, Pa*s - Liquid |
298.15 | 0.0000 | 0.0014 |
298.15 | 0.1201 | 0.0012 |
298.15 | 0.2122 | 0.0012 |
298.15 | 0.3072 | 0.0012 |
298.15 | 0.4085 | 0.0011 |
298.15 | 0.5014 | 0.0011 |
298.15 | 0.5972 | 0.0011 |
298.15 | 0.6998 | 0.0011 |
298.15 | 0.7999 | 0.0011 |
298.15 | 0.8947 | 0.0011 |
298.15 | 1.0000 | 0.0012 |
303.15 | 0.0000 | 0.0012 |
303.15 | 0.1201 | 0.0011 |
303.15 | 0.2122 | 0.0011 |
303.15 | 0.3072 | 0.0011 |
303.15 | 0.4085 | 0.0010 |
303.15 | 0.5014 | 0.0010 |
303.15 | 0.5972 | 0.0010 |
303.15 | 0.6998 | 0.0010 |
303.15 | 0.7999 | 0.0010 |
303.15 | 0.8947 | 0.0010 |
303.15 | 1.0000 | 0.0011 |
308.15 | 0.0000 | 0.0011 |
308.15 | 0.1201 | 0.0010 |
308.15 | 0.2122 | 0.0010 |
308.15 | 0.3072 | 0.0010 |
308.15 | 0.4085 | 0.0009 |
308.15 | 0.5014 | 0.0009 |
308.15 | 0.5972 | 0.0009 |
308.15 | 0.6998 | 0.0009 |
308.15 | 0.7999 | 0.0009 |
308.15 | 0.8947 | 0.0010 |
308.15 | 1.0000 | 0.0010 |
Operational conditions:
Molality, mol/kg of Tributylamine (1) - Liquid | Viscosity, Pa*s - Liquid |
---|---|
0.1229 | 0.0011 |
0.2173 | 0.0010 |
0.3227 | 0.0010 |
0.4476 | 0.0010 |
0.5768 | 0.0010 |
0.7655 | 0.0010 |
0.8789 | 0.0010 |
1.0282 | 0.0010 |
1.1794 | 0.0010 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Viscosity, Pa*s - Liquid |
298.15 | 0.0000 | 0.0014 |
298.15 | 0.1201 | 0.0012 |
298.15 | 0.2122 | 0.0012 |
298.15 | 0.3072 | 0.0012 |
298.15 | 0.4085 | 0.0011 |
298.15 | 0.5014 | 0.0011 |
298.15 | 0.5972 | 0.0011 |
298.15 | 0.6998 | 0.0011 |
298.15 | 0.7999 | 0.0011 |
298.15 | 0.8947 | 0.0011 |
298.15 | 1.0000 | 0.0012 |
303.15 | 0.0000 | 0.0012 |
303.15 | 0.1201 | 0.0011 |
303.15 | 0.2122 | 0.0011 |
303.15 | 0.3072 | 0.0011 |
303.15 | 0.4085 | 0.0010 |
303.15 | 0.5014 | 0.0010 |
303.15 | 0.5972 | 0.0010 |
303.15 | 0.6998 | 0.0010 |
303.15 | 0.7999 | 0.0010 |
303.15 | 0.8947 | 0.0010 |
303.15 | 1.0000 | 0.0011 |
308.15 | 0.0000 | 0.0011 |
308.15 | 0.1201 | 0.0010 |
308.15 | 0.2122 | 0.0010 |
308.15 | 0.3072 | 0.0010 |
308.15 | 0.4085 | 0.0009 |
308.15 | 0.5014 | 0.0009 |
308.15 | 0.5972 | 0.0009 |
308.15 | 0.6998 | 0.0009 |
308.15 | 0.7999 | 0.0009 |
308.15 | 0.8947 | 0.0010 |
308.15 | 1.0000 | 0.0010 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Refractive index (Na D-line) - Liquid |
298.15 | 0.0000 | 1.4274 |
298.15 | 0.1201 | 1.4266 |
298.15 | 0.2122 | 1.4259 |
298.15 | 0.3072 | 1.425 |
298.15 | 0.4085 | 1.4244 |
298.15 | 0.5014 | 1.4234 |
298.15 | 0.5972 | 1.4226 |
298.15 | 0.6998 | 1.4217 |
298.15 | 0.7999 | 1.421 |
298.15 | 0.8947 | 1.4205 |
298.15 | 1.0000 | 1.4201 |
303.15 | 0.0000 | 1.4251 |
303.15 | 0.1201 | 1.424 |
303.15 | 0.2122 | 1.4236 |
303.15 | 0.3072 | 1.4226 |
303.15 | 0.4085 | 1.4218 |
303.15 | 0.5014 | 1.4209 |
303.15 | 0.5972 | 1.4201 |
303.15 | 0.6998 | 1.4192 |
303.15 | 0.7999 | 1.4185 |
303.15 | 0.8947 | 1.418 |
303.15 | 1.0000 | 1.417 |
308.15 | 0.0000 | 1.4226 |
308.15 | 0.1201 | 1.4215 |
308.15 | 0.2122 | 1.421 |
308.15 | 0.3072 | 1.4201 |
308.15 | 0.4085 | 1.4196 |
308.15 | 0.5014 | 1.4184 |
308.15 | 0.5972 | 1.4174 |
308.15 | 0.6998 | 1.4168 |
308.15 | 0.7999 | 1.416 |
308.15 | 0.8947 | 1.4154 |
308.15 | 1.0000 | 1.4143 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Refractive index (Na D-line) - Liquid |
298.15 | 0.0000 | 1.4274 |
298.15 | 0.1201 | 1.4266 |
298.15 | 0.2122 | 1.4259 |
298.15 | 0.3072 | 1.425 |
298.15 | 0.4085 | 1.4244 |
298.15 | 0.5014 | 1.4234 |
298.15 | 0.5972 | 1.4226 |
298.15 | 0.6998 | 1.4217 |
298.15 | 0.7999 | 1.421 |
298.15 | 0.8947 | 1.4205 |
298.15 | 1.0000 | 1.4201 |
303.15 | 0.0000 | 1.4251 |
303.15 | 0.1201 | 1.424 |
303.15 | 0.2122 | 1.4236 |
303.15 | 0.3072 | 1.4226 |
303.15 | 0.4085 | 1.4218 |
303.15 | 0.5014 | 1.4209 |
303.15 | 0.5972 | 1.4201 |
303.15 | 0.6998 | 1.4192 |
303.15 | 0.7999 | 1.4185 |
303.15 | 0.8947 | 1.418 |
303.15 | 1.0000 | 1.417 |
308.15 | 0.0000 | 1.4226 |
308.15 | 0.1201 | 1.4215 |
308.15 | 0.2122 | 1.421 |
308.15 | 0.3072 | 1.4201 |
308.15 | 0.4085 | 1.4196 |
308.15 | 0.5014 | 1.4184 |
308.15 | 0.5972 | 1.4174 |
308.15 | 0.6998 | 1.4168 |
308.15 | 0.7999 | 1.416 |
308.15 | 0.8947 | 1.4154 |
308.15 | 1.0000 | 1.4143 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 0.0000 | 774.4 |
298.15 | 0.1201 | 785.1 |
298.15 | 0.2122 | 794.7 |
298.15 | 0.3072 | 806.0 |
298.15 | 0.4085 | 820.5 |
298.15 | 0.5014 | 836.6 |
298.15 | 0.5972 | 856.9 |
298.15 | 0.6998 | 884.0 |
298.15 | 0.7999 | 917.9 |
298.15 | 0.8947 | 960.6 |
298.15 | 1.0000 | 1027.6 |
303.15 | 0.0000 | 770.1 |
303.15 | 0.1201 | 780.9 |
303.15 | 0.2122 | 790.2 |
303.15 | 0.3072 | 801.6 |
303.15 | 0.4085 | 815.9 |
303.15 | 0.5014 | 832.1 |
303.15 | 0.5972 | 852.1 |
303.15 | 0.6998 | 879.2 |
303.15 | 0.7999 | 912.6 |
303.15 | 0.8947 | 955.2 |
303.15 | 1.0000 | 1021.9 |
308.15 | 0.0000 | 766.2 |
308.15 | 0.1201 | 776.8 |
308.15 | 0.2122 | 785.9 |
308.15 | 0.3072 | 797.1 |
308.15 | 0.4085 | 811.4 |
308.15 | 0.5014 | 827.5 |
308.15 | 0.5972 | 847.4 |
308.15 | 0.6998 | 874.1 |
308.15 | 0.7999 | 907.4 |
308.15 | 0.8947 | 949.9 |
308.15 | 1.0000 | 1016.2 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of 1,4-Dioxane (2) - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 0.0000 | 774.4 |
298.15 | 0.1201 | 785.1 |
298.15 | 0.2122 | 794.7 |
298.15 | 0.3072 | 806.0 |
298.15 | 0.4085 | 820.5 |
298.15 | 0.5014 | 836.6 |
298.15 | 0.5972 | 856.9 |
298.15 | 0.6998 | 884.0 |
298.15 | 0.7999 | 917.9 |
298.15 | 0.8947 | 960.6 |
298.15 | 1.0000 | 1027.6 |
303.15 | 0.0000 | 770.1 |
303.15 | 0.1201 | 780.9 |
303.15 | 0.2122 | 790.2 |
303.15 | 0.3072 | 801.6 |
303.15 | 0.4085 | 815.9 |
303.15 | 0.5014 | 832.1 |
303.15 | 0.5972 | 852.1 |
303.15 | 0.6998 | 879.2 |
303.15 | 0.7999 | 912.6 |
303.15 | 0.8947 | 955.2 |
303.15 | 1.0000 | 1021.9 |
308.15 | 0.0000 | 766.2 |
308.15 | 0.1201 | 776.8 |
308.15 | 0.2122 | 785.9 |
308.15 | 0.3072 | 797.1 |
308.15 | 0.4085 | 811.4 |
308.15 | 0.5014 | 827.5 |
308.15 | 0.5972 | 847.4 |
308.15 | 0.6998 | 874.1 |
308.15 | 0.7999 | 907.4 |
308.15 | 0.8947 | 949.9 |
308.15 | 1.0000 | 1016.2 |
Operational conditions:
Mole fraction of 1,4-Dioxane (2) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0000 | 1261.0 |
0.1201 | 1253.0 |
0.2122 | 1254.0 |
0.3072 | 1257.0 |
0.4085 | 1264.0 |
0.5014 | 1272.0 |
0.5972 | 1281.0 |
0.6998 | 1292.0 |
0.7999 | 1305.0 |
0.8947 | 1320.0 |
1.0000 | 1343.0 |
Operational conditions:
Mole fraction of 1,4-Dioxane (2) - Liquid | Speed of sound, m/s - Liquid |
---|---|
0.0000 | 1261.0 |
0.1201 | 1253.0 |
0.2122 | 1254.0 |
0.3072 | 1257.0 |
0.4085 | 1264.0 |
0.5014 | 1272.0 |
0.5972 | 1281.0 |
0.6998 | 1292.0 |
0.7999 | 1305.0 |
0.8947 | 1320.0 |
1.0000 | 1343.0 |