Datasets
-
Osmotic coefficient (4)
-
Molality, mol/kg (10)
-
η - Viscosity, Pa*s (6)
-
Eutectic temperature, K (2)
-
n0 - Refractive index (Na D-line) (6)
-
ρl - Mass density, kg/m3 (10)
-
λ - Thermal conductivity, W/m/K (2)
-
Tfus - Solid-liquid equilibrium temperature, K (6)
Osmotic coefficient
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
Osmotic coefficient - Liquid |
1.0000 |
0.6430 |
3.0 |
0.6290 |
1.0000 |
0.6400 |
3.0 |
0.6270 |
3.0 |
0.6250 |
1.0000 |
0.6410 |
(Relative) activity of Water (2)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
(Relative) activity of Water (2) - Liquid |
2.659 |
0.9120 |
0.5960 |
0.9810 |
1.191 |
0.9630 |
0.7670 |
0.9760 |
Osmotic coefficient
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
Osmotic coefficient - Liquid |
1.0000 |
0.6430 |
3.0 |
0.6290 |
1.0000 |
0.6400 |
3.0 |
0.6270 |
3.0 |
0.6250 |
1.0000 |
0.6410 |
(Relative) activity of Water (2)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
(Relative) activity of Water (2) - Liquid |
2.659 |
0.9120 |
0.5960 |
0.9810 |
1.191 |
0.9630 |
0.7670 |
0.9760 |
Molality, mol/kg of Ammonium sulfate (1)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
5.803 |
5.772 |
Mass fraction of Ammonium sulfate (1)
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mass fraction of Ammonium sulfate (1) - Liquid |
88.35 |
313.15 |
0.4477 |
Mass fraction of Ammonium sulfate (1)
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mass fraction of Ammonium sulfate (1) - Liquid |
101.33 |
273.15 |
0.4140 |
Mass fraction of Ammonium sulfate (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Temperature, K - Liquid |
Mass fraction of Ammonium sulfate (1) - Liquid |
313.15 |
0.4460 |
353.15 |
0.4810 |
Mass fraction of Ammonium sulfate (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Temperature, K - Liquid |
Mass fraction of Ammonium sulfate (1) - Liquid |
298.15 |
0.4362 |
328.15 |
0.4623 |
353.15 |
0.4850 |
Molality, mol/kg of Ammonium sulfate (1)
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
5.803 |
5.772 |
Mass fraction of Ammonium sulfate (1)
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mass fraction of Ammonium sulfate (1) - Liquid |
88.35 |
313.15 |
0.4477 |
Mass fraction of Ammonium sulfate (1)
[ref]
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mass fraction of Ammonium sulfate (1) - Liquid |
101.33 |
273.15 |
0.4140 |
Mass fraction of Ammonium sulfate (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Temperature, K - Liquid |
Mass fraction of Ammonium sulfate (1) - Liquid |
313.15 |
0.4460 |
353.15 |
0.4810 |
Mass fraction of Ammonium sulfate (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Temperature, K - Liquid |
Mass fraction of Ammonium sulfate (1) - Liquid |
298.15 |
0.4362 |
328.15 |
0.4623 |
353.15 |
0.4850 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Mass fraction of Ammonium sulfate (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Viscosity, Pa*s - Liquid |
0.4477 |
313.15 |
88.35 |
0.0020 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0081 |
0.0009 |
298.15 |
0.0099 |
0.0009 |
298.15 |
0.0201 |
0.0009 |
298.15 |
0.0402 |
0.0009 |
298.15 |
0.0599 |
0.0009 |
298.15 |
0.0802 |
0.0009 |
298.15 |
0.1000 |
0.0009 |
308.15 |
0.0081 |
0.0007 |
308.15 |
0.0099 |
0.0007 |
308.15 |
0.0201 |
0.0007 |
308.15 |
0.0402 |
0.0007 |
308.15 |
0.0599 |
0.0007 |
308.15 |
0.0802 |
0.0007 |
308.15 |
0.1000 |
0.0007 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Molality, mol/kg = 4.655 (Liquid)
- Pressure, kPa = 101 (Liquid)
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0021 |
303.15 |
0.0019 |
308.15 |
0.0018 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Mass fraction of Ammonium sulfate (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Viscosity, Pa*s - Liquid |
0.4477 |
313.15 |
88.35 |
0.0020 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0081 |
0.0009 |
298.15 |
0.0099 |
0.0009 |
298.15 |
0.0201 |
0.0009 |
298.15 |
0.0402 |
0.0009 |
298.15 |
0.0599 |
0.0009 |
298.15 |
0.0802 |
0.0009 |
298.15 |
0.1000 |
0.0009 |
308.15 |
0.0081 |
0.0007 |
308.15 |
0.0099 |
0.0007 |
308.15 |
0.0201 |
0.0007 |
308.15 |
0.0402 |
0.0007 |
308.15 |
0.0599 |
0.0007 |
308.15 |
0.0802 |
0.0007 |
308.15 |
0.1000 |
0.0007 |
Viscosity, Pa*s
[ref]
Operational conditions:
- Molality, mol/kg = 4.655 (Liquid)
- Pressure, kPa = 101 (Liquid)
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
298.15 |
0.0021 |
303.15 |
0.0019 |
308.15 |
0.0018 |
Eutectic temperature, K
[ref]
Pressure, kPa - Liquid |
Eutectic temperature, K - Liquid |
100.00 |
254.50 |
Eutectic temperature, K
[ref]
Pressure, kPa - Liquid |
Eutectic temperature, K - Liquid |
100.00 |
254.50 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mass fraction of Ammonium sulfate (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0005 |
1.3326 |
0.0011 |
1.3327 |
0.0053 |
1.3334 |
0.0104 |
1.3342 |
0.0208 |
1.3359 |
0.0412 |
1.3392 |
0.0712 |
1.3439 |
0.1007 |
1.3486 |
0.0000 |
1.3325 |
Refractive index (Na D-line)
[ref]
Fixed |
Measured |
Mass fraction of Ammonium sulfate (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Refractive index (Na D-line) - Liquid |
0.4477 |
313.15 |
88.35 |
1.3978 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
Refractive index (Na D-line) - Liquid |
288.15 |
0.0000 |
1.3334 |
288.15 |
0.2725 |
1.3393 |
288.15 |
0.3995 |
1.3417 |
288.15 |
0.4876 |
1.3435 |
288.15 |
0.8025 |
1.3491 |
288.15 |
1.1984 |
1.3555 |
288.15 |
1.6036 |
1.3614 |
288.15 |
1.9924 |
1.3666 |
288.15 |
2.3812 |
1.3713 |
288.15 |
2.8008 |
1.3759 |
288.15 |
3.1997 |
1.3801 |
288.15 |
3.6186 |
1.3838 |
288.15 |
3.9973 |
1.3871 |
288.15 |
4.3955 |
1.3902 |
288.15 |
4.7625 |
1.3929 |
288.15 |
5.1808 |
1.3957 |
288.15 |
5.6 |
1.3984 |
298.15 |
0.0000 |
1.3325 |
298.15 |
0.2725 |
1.3381 |
298.15 |
0.3995 |
1.3408 |
298.15 |
0.4876 |
1.3423 |
298.15 |
0.8025 |
1.348 |
298.15 |
1.1984 |
1.3543 |
298.15 |
1.6036 |
1.3602 |
298.15 |
1.9924 |
1.3654 |
298.15 |
2.3812 |
1.3701 |
298.15 |
2.8008 |
1.3747 |
298.15 |
3.1997 |
1.3787 |
298.15 |
3.6186 |
1.3826 |
298.15 |
3.9973 |
1.386 |
298.15 |
4.3955 |
1.389 |
298.15 |
4.7625 |
1.3917 |
298.15 |
5.1808 |
1.3945 |
298.15 |
5.6 |
1.3971 |
308.15 |
0.0000 |
1.3313 |
308.15 |
0.2725 |
1.337 |
308.15 |
0.3995 |
1.3394 |
308.15 |
0.4876 |
1.341 |
308.15 |
0.8025 |
1.3467 |
308.15 |
1.1984 |
1.353 |
308.15 |
1.6036 |
1.3589 |
308.15 |
1.9924 |
1.364 |
308.15 |
2.3812 |
1.3688 |
308.15 |
2.8008 |
1.3734 |
308.15 |
3.1997 |
1.3774 |
308.15 |
3.6186 |
1.3813 |
308.15 |
3.9973 |
1.3845 |
308.15 |
4.3955 |
1.3876 |
308.15 |
4.7625 |
1.3903 |
308.15 |
5.1808 |
1.3932 |
308.15 |
5.6 |
1.3958 |
308.15 |
5.876 |
1.3975 |
318.15 |
0.0000 |
1.3298 |
318.15 |
0.2725 |
1.3354 |
318.15 |
0.3995 |
1.3381 |
318.15 |
0.4876 |
1.3396 |
318.15 |
0.8025 |
1.3452 |
318.15 |
1.1984 |
1.3516 |
318.15 |
1.6036 |
1.3574 |
318.15 |
1.9924 |
1.3625 |
318.15 |
2.3812 |
1.3673 |
318.15 |
2.8008 |
1.3721 |
318.15 |
3.1997 |
1.3761 |
318.15 |
3.6186 |
1.3801 |
318.15 |
3.9973 |
1.3833 |
318.15 |
4.3955 |
1.3865 |
318.15 |
4.7625 |
1.3892 |
318.15 |
5.1808 |
1.392 |
318.15 |
5.6 |
1.3946 |
318.15 |
5.876 |
1.3962 |
318.15 |
6.3279 |
1.3983 |
Refractive index (Na D-line)
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mass fraction of Ammonium sulfate (1) - Liquid |
Refractive index (Na D-line) - Liquid |
0.0005 |
1.3326 |
0.0011 |
1.3327 |
0.0053 |
1.3334 |
0.0104 |
1.3342 |
0.0208 |
1.3359 |
0.0412 |
1.3392 |
0.0712 |
1.3439 |
0.1007 |
1.3486 |
0.0000 |
1.3325 |
Refractive index (Na D-line)
[ref]
Fixed |
Measured |
Mass fraction of Ammonium sulfate (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Refractive index (Na D-line) - Liquid |
0.4477 |
313.15 |
88.35 |
1.3978 |
Refractive index (Na D-line)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
Refractive index (Na D-line) - Liquid |
288.15 |
0.0000 |
1.3334 |
288.15 |
0.2725 |
1.3393 |
288.15 |
0.3995 |
1.3417 |
288.15 |
0.4876 |
1.3435 |
288.15 |
0.8025 |
1.3491 |
288.15 |
1.1984 |
1.3555 |
288.15 |
1.6036 |
1.3614 |
288.15 |
1.9924 |
1.3666 |
288.15 |
2.3812 |
1.3713 |
288.15 |
2.8008 |
1.3759 |
288.15 |
3.1997 |
1.3801 |
288.15 |
3.6186 |
1.3838 |
288.15 |
3.9973 |
1.3871 |
288.15 |
4.3955 |
1.3902 |
288.15 |
4.7625 |
1.3929 |
288.15 |
5.1808 |
1.3957 |
288.15 |
5.6 |
1.3984 |
298.15 |
0.0000 |
1.3325 |
298.15 |
0.2725 |
1.3381 |
298.15 |
0.3995 |
1.3408 |
298.15 |
0.4876 |
1.3423 |
298.15 |
0.8025 |
1.348 |
298.15 |
1.1984 |
1.3543 |
298.15 |
1.6036 |
1.3602 |
298.15 |
1.9924 |
1.3654 |
298.15 |
2.3812 |
1.3701 |
298.15 |
2.8008 |
1.3747 |
298.15 |
3.1997 |
1.3787 |
298.15 |
3.6186 |
1.3826 |
298.15 |
3.9973 |
1.386 |
298.15 |
4.3955 |
1.389 |
298.15 |
4.7625 |
1.3917 |
298.15 |
5.1808 |
1.3945 |
298.15 |
5.6 |
1.3971 |
308.15 |
0.0000 |
1.3313 |
308.15 |
0.2725 |
1.337 |
308.15 |
0.3995 |
1.3394 |
308.15 |
0.4876 |
1.341 |
308.15 |
0.8025 |
1.3467 |
308.15 |
1.1984 |
1.353 |
308.15 |
1.6036 |
1.3589 |
308.15 |
1.9924 |
1.364 |
308.15 |
2.3812 |
1.3688 |
308.15 |
2.8008 |
1.3734 |
308.15 |
3.1997 |
1.3774 |
308.15 |
3.6186 |
1.3813 |
308.15 |
3.9973 |
1.3845 |
308.15 |
4.3955 |
1.3876 |
308.15 |
4.7625 |
1.3903 |
308.15 |
5.1808 |
1.3932 |
308.15 |
5.6 |
1.3958 |
308.15 |
5.876 |
1.3975 |
318.15 |
0.0000 |
1.3298 |
318.15 |
0.2725 |
1.3354 |
318.15 |
0.3995 |
1.3381 |
318.15 |
0.4876 |
1.3396 |
318.15 |
0.8025 |
1.3452 |
318.15 |
1.1984 |
1.3516 |
318.15 |
1.6036 |
1.3574 |
318.15 |
1.9924 |
1.3625 |
318.15 |
2.3812 |
1.3673 |
318.15 |
2.8008 |
1.3721 |
318.15 |
3.1997 |
1.3761 |
318.15 |
3.6186 |
1.3801 |
318.15 |
3.9973 |
1.3833 |
318.15 |
4.3955 |
1.3865 |
318.15 |
4.7625 |
1.3892 |
318.15 |
5.1808 |
1.392 |
318.15 |
5.6 |
1.3946 |
318.15 |
5.876 |
1.3962 |
318.15 |
6.3279 |
1.3983 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mass fraction of Ammonium sulfate (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0005 |
997.4 |
0.0011 |
997.7 |
0.0053 |
1000.3 |
0.0104 |
1003.3 |
0.0208 |
1009.4 |
0.0412 |
1021.2 |
0.0712 |
1038.4 |
0.1007 |
1055.3 |
0.0000 |
997.1 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mass fraction of Ammonium sulfate (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
0.4477 |
313.15 |
88.35 |
1247.0 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ammonium sulfate (1) - Liquid |
Mass density, kg/m3 - Liquid |
313.15 |
0.4460 |
1238.0 |
353.15 |
0.4810 |
1242.0 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.3027 |
1023.03 |
283.15 |
0.6334 |
1045.95 |
283.15 |
1.2913 |
1086.01 |
283.15 |
1.9176 |
1118.86 |
283.15 |
2.6017 |
1150.0 |
283.15 |
3.229 |
1174.83 |
283.15 |
3.8967 |
1198.13 |
283.15 |
4.5345 |
1217.84 |
283.15 |
5.1716 |
1235.25 |
288.15 |
0.3027 |
1022.14 |
288.15 |
0.6334 |
1044.87 |
288.15 |
1.2913 |
1084.61 |
288.15 |
1.9176 |
1117.26 |
288.15 |
2.6017 |
1148.26 |
288.15 |
3.229 |
1173.04 |
288.15 |
3.8967 |
1196.29 |
288.15 |
4.5345 |
1215.96 |
288.15 |
5.1716 |
1233.44 |
293.15 |
0.3027 |
1021.04 |
293.15 |
0.6334 |
1043.51 |
293.15 |
1.2913 |
1083.03 |
293.15 |
1.9176 |
1115.56 |
293.15 |
2.6017 |
1146.37 |
293.15 |
3.229 |
1171.11 |
293.15 |
3.8967 |
1194.34 |
293.15 |
4.5345 |
1213.98 |
293.15 |
5.1716 |
1231.52 |
298.15 |
0.3027 |
1019.68 |
298.15 |
0.6334 |
1042.0 |
298.15 |
1.2913 |
1081.31 |
298.15 |
1.9176 |
1113.7 |
298.15 |
2.6017 |
1144.48 |
298.15 |
3.229 |
1169.22 |
298.15 |
3.8967 |
1192.44 |
298.15 |
4.5345 |
1212.12 |
298.15 |
5.1716 |
1229.67 |
298.15 |
5.8906 |
1247.4 |
Mass density, kg/m3
[ref]
Operational conditions:
- Molality, mol/kg = 4.655 (Liquid)
- Pressure, kPa = 101 (Liquid)
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
1217.66 |
298.15 |
1215.79 |
303.15 |
1213.89 |
308.15 |
1211.94 |
313.15 |
1209.97 |
Mass density, kg/m3
[ref]
Operational conditions:
- Pressure, kPa = 100 (Liquid)
- Temperature, K = 298.15 (Liquid)
Mass fraction of Ammonium sulfate (1) - Liquid |
Mass density, kg/m3 - Liquid |
0.0005 |
997.4 |
0.0011 |
997.7 |
0.0053 |
1000.3 |
0.0104 |
1003.3 |
0.0208 |
1009.4 |
0.0412 |
1021.2 |
0.0712 |
1038.4 |
0.1007 |
1055.3 |
0.0000 |
997.1 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mass fraction of Ammonium sulfate (1) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
0.4477 |
313.15 |
88.35 |
1247.0 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mass fraction of Ammonium sulfate (1) - Liquid |
Mass density, kg/m3 - Liquid |
313.15 |
0.4460 |
1238.0 |
353.15 |
0.4810 |
1242.0 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
0.3027 |
1023.03 |
283.15 |
0.6334 |
1045.95 |
283.15 |
1.2913 |
1086.01 |
283.15 |
1.9176 |
1118.86 |
283.15 |
2.6017 |
1150.0 |
283.15 |
3.229 |
1174.83 |
283.15 |
3.8967 |
1198.13 |
283.15 |
4.5345 |
1217.84 |
283.15 |
5.1716 |
1235.25 |
288.15 |
0.3027 |
1022.14 |
288.15 |
0.6334 |
1044.87 |
288.15 |
1.2913 |
1084.61 |
288.15 |
1.9176 |
1117.26 |
288.15 |
2.6017 |
1148.26 |
288.15 |
3.229 |
1173.04 |
288.15 |
3.8967 |
1196.29 |
288.15 |
4.5345 |
1215.96 |
288.15 |
5.1716 |
1233.44 |
293.15 |
0.3027 |
1021.04 |
293.15 |
0.6334 |
1043.51 |
293.15 |
1.2913 |
1083.03 |
293.15 |
1.9176 |
1115.56 |
293.15 |
2.6017 |
1146.37 |
293.15 |
3.229 |
1171.11 |
293.15 |
3.8967 |
1194.34 |
293.15 |
4.5345 |
1213.98 |
293.15 |
5.1716 |
1231.52 |
298.15 |
0.3027 |
1019.68 |
298.15 |
0.6334 |
1042.0 |
298.15 |
1.2913 |
1081.31 |
298.15 |
1.9176 |
1113.7 |
298.15 |
2.6017 |
1144.48 |
298.15 |
3.229 |
1169.22 |
298.15 |
3.8967 |
1192.44 |
298.15 |
4.5345 |
1212.12 |
298.15 |
5.1716 |
1229.67 |
298.15 |
5.8906 |
1247.4 |
Mass density, kg/m3
[ref]
Operational conditions:
- Molality, mol/kg = 4.655 (Liquid)
- Pressure, kPa = 101 (Liquid)
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
293.15 |
1217.66 |
298.15 |
1215.79 |
303.15 |
1213.89 |
308.15 |
1211.94 |
313.15 |
1209.97 |
Thermal conductivity, W/m/K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
Temperature, K - Liquid |
Thermal conductivity, W/m/K - Liquid |
0.3983 |
280.78 |
0.5646 |
0.3983 |
285.94 |
0.5743 |
0.3983 |
291.15 |
0.5861 |
0.3983 |
296.52 |
0.5974 |
0.3983 |
301.77 |
0.6078 |
0.3983 |
306.78 |
0.6184 |
0.3983 |
316.98 |
0.6345 |
0.3983 |
327.13 |
0.6431 |
0.3983 |
337.25 |
0.6534 |
0.8409 |
280.76 |
0.5624 |
0.8409 |
285.92 |
0.5723 |
0.8409 |
290.98 |
0.5810 |
0.8409 |
296.32 |
0.5917 |
0.8409 |
301.62 |
0.6037 |
0.8409 |
306.85 |
0.6131 |
0.8409 |
317.20 |
0.6265 |
0.8409 |
327.33 |
0.6389 |
0.8409 |
337.42 |
0.6479 |
1.3355 |
280.54 |
0.5560 |
1.3355 |
285.77 |
0.5650 |
1.3355 |
291.03 |
0.5764 |
1.3355 |
296.31 |
0.5859 |
1.3355 |
301.55 |
0.5957 |
1.3355 |
306.89 |
0.6049 |
1.3355 |
317.16 |
0.6185 |
1.3355 |
327.17 |
0.6289 |
1.3355 |
337.53 |
0.6382 |
1.8919 |
280.56 |
0.5505 |
1.8919 |
285.76 |
0.5603 |
1.8919 |
290.93 |
0.5701 |
1.8919 |
296.24 |
0.5797 |
1.8919 |
301.38 |
0.5883 |
1.8919 |
307.13 |
0.5965 |
1.8919 |
317.15 |
0.6108 |
1.8919 |
327.19 |
0.6229 |
1.8919 |
337.51 |
0.6321 |
2.5226 |
280.12 |
0.5450 |
2.5226 |
285.20 |
0.5527 |
2.5226 |
290.07 |
0.5598 |
2.5226 |
296.03 |
0.5703 |
2.5226 |
300.88 |
0.5811 |
2.5226 |
306.38 |
0.5902 |
2.5226 |
316.85 |
0.6019 |
2.5226 |
326.60 |
0.6147 |
2.5226 |
336.88 |
0.6254 |
3.2433 |
280.06 |
0.5371 |
3.2433 |
285.25 |
0.5462 |
3.2433 |
290.46 |
0.5563 |
3.2433 |
295.88 |
0.5661 |
3.2433 |
301.14 |
0.5748 |
3.2433 |
306.43 |
0.5826 |
3.2433 |
316.59 |
0.5931 |
3.2433 |
326.74 |
0.6051 |
3.2433 |
337.13 |
0.6177 |
4.0749 |
279.83 |
0.5254 |
4.0749 |
285.32 |
0.5358 |
4.0749 |
290.55 |
0.5468 |
4.0749 |
296.06 |
0.5575 |
4.0749 |
301.22 |
0.5652 |
4.0749 |
306.30 |
0.5731 |
4.0749 |
316.52 |
0.5884 |
4.0749 |
326.73 |
0.5973 |
4.0749 |
337.18 |
0.6087 |
5.0452 |
280.09 |
0.5181 |
5.0452 |
285.70 |
0.5309 |
5.0452 |
290.79 |
0.5383 |
5.0452 |
296.14 |
0.5477 |
5.0452 |
301.34 |
0.5567 |
5.0452 |
306.57 |
0.5654 |
5.0452 |
316.80 |
0.5794 |
5.0452 |
326.94 |
0.5914 |
5.0452 |
337.07 |
0.6002 |
Thermal conductivity, W/m/K
[ref]
Operational condition: Pressure, kPa =
101 (Liquid)
Fixed |
Measured |
Molality, mol/kg of Ammonium sulfate (1) - Liquid |
Temperature, K - Liquid |
Thermal conductivity, W/m/K - Liquid |
0.3983 |
280.78 |
0.5646 |
0.3983 |
285.94 |
0.5743 |
0.3983 |
291.15 |
0.5861 |
0.3983 |
296.52 |
0.5974 |
0.3983 |
301.77 |
0.6078 |
0.3983 |
306.78 |
0.6184 |
0.3983 |
316.98 |
0.6345 |
0.3983 |
327.13 |
0.6431 |
0.3983 |
337.25 |
0.6534 |
0.8409 |
280.76 |
0.5624 |
0.8409 |
285.92 |
0.5723 |
0.8409 |
290.98 |
0.5810 |
0.8409 |
296.32 |
0.5917 |
0.8409 |
301.62 |
0.6037 |
0.8409 |
306.85 |
0.6131 |
0.8409 |
317.20 |
0.6265 |
0.8409 |
327.33 |
0.6389 |
0.8409 |
337.42 |
0.6479 |
1.3355 |
280.54 |
0.5560 |
1.3355 |
285.77 |
0.5650 |
1.3355 |
291.03 |
0.5764 |
1.3355 |
296.31 |
0.5859 |
1.3355 |
301.55 |
0.5957 |
1.3355 |
306.89 |
0.6049 |
1.3355 |
317.16 |
0.6185 |
1.3355 |
327.17 |
0.6289 |
1.3355 |
337.53 |
0.6382 |
1.8919 |
280.56 |
0.5505 |
1.8919 |
285.76 |
0.5603 |
1.8919 |
290.93 |
0.5701 |
1.8919 |
296.24 |
0.5797 |
1.8919 |
301.38 |
0.5883 |
1.8919 |
307.13 |
0.5965 |
1.8919 |
317.15 |
0.6108 |
1.8919 |
327.19 |
0.6229 |
1.8919 |
337.51 |
0.6321 |
2.5226 |
280.12 |
0.5450 |
2.5226 |
285.20 |
0.5527 |
2.5226 |
290.07 |
0.5598 |
2.5226 |
296.03 |
0.5703 |
2.5226 |
300.88 |
0.5811 |
2.5226 |
306.38 |
0.5902 |
2.5226 |
316.85 |
0.6019 |
2.5226 |
326.60 |
0.6147 |
2.5226 |
336.88 |
0.6254 |
3.2433 |
280.06 |
0.5371 |
3.2433 |
285.25 |
0.5462 |
3.2433 |
290.46 |
0.5563 |
3.2433 |
295.88 |
0.5661 |
3.2433 |
301.14 |
0.5748 |
3.2433 |
306.43 |
0.5826 |
3.2433 |
316.59 |
0.5931 |
3.2433 |
326.74 |
0.6051 |
3.2433 |
337.13 |
0.6177 |
4.0749 |
279.83 |
0.5254 |
4.0749 |
285.32 |
0.5358 |
4.0749 |
290.55 |
0.5468 |
4.0749 |
296.06 |
0.5575 |
4.0749 |
301.22 |
0.5652 |
4.0749 |
306.30 |
0.5731 |
4.0749 |
316.52 |
0.5884 |
4.0749 |
326.73 |
0.5973 |
4.0749 |
337.18 |
0.6087 |
5.0452 |
280.09 |
0.5181 |
5.0452 |
285.70 |
0.5309 |
5.0452 |
290.79 |
0.5383 |
5.0452 |
296.14 |
0.5477 |
5.0452 |
301.34 |
0.5567 |
5.0452 |
306.57 |
0.5654 |
5.0452 |
316.80 |
0.5794 |
5.0452 |
326.94 |
0.5914 |
5.0452 |
337.07 |
0.6002 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mass fraction of Ammonium sulfate (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.4382 |
303.15 |
0.4475 |
313.15 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Mass fraction of Ammonium sulfate (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.4272 |
298.15 |
0.4623 |
328.15 |
0.4850 |
353.15 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mass fraction of Ammonium sulfate (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
272.60 |
0.1000 |
265.20 |
0.2000 |
262.60 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mass fraction of Ammonium sulfate (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.4382 |
303.15 |
0.4475 |
313.15 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
95 (Liquid)
Mass fraction of Ammonium sulfate (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.4272 |
298.15 |
0.4623 |
328.15 |
0.4850 |
353.15 |
Solid-liquid equilibrium temperature, K
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Mass fraction of Ammonium sulfate (1) - Liquid |
Solid-liquid equilibrium temperature, K - Liquid |
0.0000 |
272.60 |
0.1000 |
265.20 |
0.2000 |
262.60 |
Sources
-
Phase equilibrium of the quaternary system K2SO4-MgSO4-(NH4)2SO4-H2O at 25 C
-
The effect of temperature on polyethylene glycol (4000 or 8000)e(sodium or ammonium) sulfate Aqueous Two Phase Systems
-
Measuring and modeling aqueous electrolyte/amino-acid solutions with ePC-SAFT
-
Thermodynamic equilibrium of the polyethylene glycol 2000 and sulphate salts solutions
-
Solid-liquid phase equilibria of quaternary system NH4(+)//C1(-) , SO4(2-), H2PO4(-)-H2O and its subsystems NH4(+)//C1(-), SO4(2-)-H2O, NH4(+)//C1(-), H2PO4 (-)-H2O at 313.15 K
-
Phase diagrams of the quaternary system K+, NH4+//Cl-, SO4(2-)-H2O at 273.15 K and their application
-
Solubility Investigations in the MgSO4 Al2(SO4)3 (NH4)2SO4 H2O Quaternary System at 40 and 80 deg C
-
Phase Equilibria in the Aqueous Ternary System (NH4)2SO4 + Na2SO4 + H2O at T = (303.15 and 313.15) K and p = 0.1 MPa
-
Phase Equilibrium of the MgSO4-(NH4)2SO4-H2O Ternary System: Effects of Sulfuric Acid and Iron Sulfate and Its Application in Mineral Carbonation of Serpentine
-
Phase Diagrams of (NH4)2SO4-Al2(SO4)3-H2O Ternary System: Effect of Sulfuric Acid and Its Application in Recovery of Aluminum from Coal Fly Ash
-
Water in Solutions of Chaotropic and Kosmotropic Salts: A Differential Scanning Calorimetry Investigation
-
Densities of Univalent Cation Sulfates in Ethanol + Water Solutions
-
Thermal Conductivity and Density of (NH4)2SO4 + H2O, NH4NO3 + H2O, and (NH4)2SO4 + NH4NO3 + H2O Solutions at T = (278.15 to 333.15) K
-
Viscosities of Ammonium Sulfate, Potassium Sulfate, and Aluminum Sulfate in Water and Water + N,N-Dimethylformamide Mixtures at Different Temperatures
-
Physicochemical Properties of Aqueous Hydroxylamine Sulfate and Aqueous (Hydroxylamine Sulfate + Ammonium Sulfate) Solutions at Different Temperatures
-
Refractive Indices of Sodium, Potassium, and Ammonium Sulfates in Ethanol-Water Solutions