Datasets
-
Mass fraction (4)
-
η - Viscosity, Pa*s (2)
-
Interfacial tension, N/m (2)
-
ρl - Mass density, kg/m3 (2)
Mass fraction of Water (3)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
Fixed |
Measured |
Solvent: Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mass fraction of Water (3) - Liquid mixture 1 |
0.1014 |
298.15 |
0.0021 |
0.2025 |
298.15 |
0.0047 |
0.3334 |
298.15 |
0.0093 |
0.4037 |
298.15 |
0.0125 |
0.5039 |
298.15 |
0.0189 |
0.6535 |
298.15 |
0.0284 |
0.8025 |
298.15 |
0.0464 |
0.1014 |
313.15 |
0.0024 |
0.2025 |
313.15 |
0.0054 |
0.3334 |
313.15 |
0.0103 |
0.4037 |
313.15 |
0.0140 |
0.5039 |
313.15 |
0.0199 |
0.6535 |
313.15 |
0.0309 |
0.8025 |
313.15 |
0.0487 |
Temperature, K x Mass fraction
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Mass fraction of Water (3) - Liquid mixture 1 |
Mass fraction of Ethylbenzene (2) - Liquid mixture 1 |
Mass fraction of Water (3) - Liquid mixture 2 |
Mass fraction of Ethylbenzene (2) - Liquid mixture 2 |
298.20 |
0.9734 |
0.0000 |
0.0536 |
0.0000 |
298.20 |
0.9919 |
0.0003 |
0.0045 |
0.8440 |
298.20 |
0.9996 |
0.0004 |
0.0025 |
0.9975 |
308.20 |
0.9742 |
0.0000 |
0.0613 |
0.0000 |
308.20 |
0.9771 |
0.0001 |
0.0426 |
0.1202 |
308.20 |
0.9799 |
0.0001 |
0.0370 |
0.2194 |
308.20 |
0.9816 |
0.0001 |
0.0277 |
0.3122 |
308.20 |
0.9826 |
0.0001 |
0.0177 |
0.4091 |
308.20 |
0.9851 |
0.0002 |
0.0162 |
0.5103 |
308.20 |
0.9869 |
0.0002 |
0.0066 |
0.6082 |
308.20 |
0.9885 |
0.0003 |
0.0058 |
0.7012 |
298.20 |
0.9765 |
0.0001 |
0.0396 |
0.1212 |
308.20 |
0.9902 |
0.0003 |
0.0057 |
0.8068 |
308.20 |
0.9913 |
0.0004 |
0.0032 |
0.8471 |
308.20 |
0.9995 |
0.0005 |
0.0021 |
0.9979 |
318.20 |
0.9756 |
0.0000 |
0.0681 |
0.0000 |
318.20 |
0.9810 |
0.0001 |
0.0487 |
0.1169 |
318.20 |
0.9820 |
0.0001 |
0.0404 |
0.2071 |
318.20 |
0.9835 |
0.0001 |
0.0322 |
0.3056 |
318.20 |
0.9856 |
0.0001 |
0.0262 |
0.4016 |
318.20 |
0.9877 |
0.0003 |
0.0191 |
0.5048 |
318.20 |
0.9887 |
0.0003 |
0.0129 |
0.6075 |
298.20 |
0.9800 |
0.0001 |
0.0313 |
0.2142 |
318.20 |
0.9900 |
0.0003 |
0.0082 |
0.7094 |
318.20 |
0.9914 |
0.0003 |
0.0053 |
0.7904 |
318.20 |
0.9930 |
0.0004 |
0.0045 |
0.8412 |
318.20 |
0.9995 |
0.0005 |
0.0006 |
0.9994 |
328.20 |
0.9761 |
0.0000 |
0.0676 |
0.0000 |
328.20 |
0.9794 |
0.0001 |
0.0524 |
0.1199 |
328.20 |
0.9822 |
0.0001 |
0.0432 |
0.2051 |
328.20 |
0.9835 |
0.0001 |
0.0302 |
0.3125 |
328.20 |
0.9864 |
0.0001 |
0.0226 |
0.4104 |
328.20 |
0.9867 |
0.0002 |
0.0181 |
0.4983 |
298.20 |
0.9809 |
0.0002 |
0.0241 |
0.3118 |
328.20 |
0.9885 |
0.0002 |
0.0140 |
0.5888 |
328.20 |
0.9900 |
0.0003 |
0.0097 |
0.6932 |
328.20 |
0.9912 |
0.0003 |
0.0064 |
0.7947 |
328.20 |
0.9918 |
0.0003 |
0.0046 |
0.8172 |
328.20 |
0.9994 |
0.0006 |
0.0004 |
0.9996 |
298.20 |
0.9849 |
0.0002 |
0.0196 |
0.4111 |
298.20 |
0.9862 |
0.0003 |
0.0175 |
0.5321 |
298.20 |
0.9875 |
0.0003 |
0.0097 |
0.5994 |
298.20 |
0.9886 |
0.0003 |
0.0092 |
0.7005 |
298.20 |
0.9915 |
0.0003 |
0.0084 |
0.7999 |
Mass fraction of Water (3)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
Fixed |
Measured |
Solvent: Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mass fraction of Water (3) - Liquid mixture 1 |
0.1014 |
298.15 |
0.0021 |
0.2025 |
298.15 |
0.0047 |
0.3334 |
298.15 |
0.0093 |
0.4037 |
298.15 |
0.0125 |
0.5039 |
298.15 |
0.0189 |
0.6535 |
298.15 |
0.0284 |
0.8025 |
298.15 |
0.0464 |
0.1014 |
313.15 |
0.0024 |
0.2025 |
313.15 |
0.0054 |
0.3334 |
313.15 |
0.0103 |
0.4037 |
313.15 |
0.0140 |
0.5039 |
313.15 |
0.0199 |
0.6535 |
313.15 |
0.0309 |
0.8025 |
313.15 |
0.0487 |
Temperature, K x Mass fraction
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
Fixed |
Measured |
Temperature, K - Liquid mixture 2 |
Mass fraction of Water (3) - Liquid mixture 1 |
Mass fraction of Ethylbenzene (2) - Liquid mixture 1 |
Mass fraction of Water (3) - Liquid mixture 2 |
Mass fraction of Ethylbenzene (2) - Liquid mixture 2 |
298.20 |
0.9734 |
0.0000 |
0.0536 |
0.0000 |
298.20 |
0.9919 |
0.0003 |
0.0045 |
0.8440 |
298.20 |
0.9996 |
0.0004 |
0.0025 |
0.9975 |
308.20 |
0.9742 |
0.0000 |
0.0613 |
0.0000 |
308.20 |
0.9771 |
0.0001 |
0.0426 |
0.1202 |
308.20 |
0.9799 |
0.0001 |
0.0370 |
0.2194 |
308.20 |
0.9816 |
0.0001 |
0.0277 |
0.3122 |
308.20 |
0.9826 |
0.0001 |
0.0177 |
0.4091 |
308.20 |
0.9851 |
0.0002 |
0.0162 |
0.5103 |
308.20 |
0.9869 |
0.0002 |
0.0066 |
0.6082 |
308.20 |
0.9885 |
0.0003 |
0.0058 |
0.7012 |
298.20 |
0.9765 |
0.0001 |
0.0396 |
0.1212 |
308.20 |
0.9902 |
0.0003 |
0.0057 |
0.8068 |
308.20 |
0.9913 |
0.0004 |
0.0032 |
0.8471 |
308.20 |
0.9995 |
0.0005 |
0.0021 |
0.9979 |
318.20 |
0.9756 |
0.0000 |
0.0681 |
0.0000 |
318.20 |
0.9810 |
0.0001 |
0.0487 |
0.1169 |
318.20 |
0.9820 |
0.0001 |
0.0404 |
0.2071 |
318.20 |
0.9835 |
0.0001 |
0.0322 |
0.3056 |
318.20 |
0.9856 |
0.0001 |
0.0262 |
0.4016 |
318.20 |
0.9877 |
0.0003 |
0.0191 |
0.5048 |
318.20 |
0.9887 |
0.0003 |
0.0129 |
0.6075 |
298.20 |
0.9800 |
0.0001 |
0.0313 |
0.2142 |
318.20 |
0.9900 |
0.0003 |
0.0082 |
0.7094 |
318.20 |
0.9914 |
0.0003 |
0.0053 |
0.7904 |
318.20 |
0.9930 |
0.0004 |
0.0045 |
0.8412 |
318.20 |
0.9995 |
0.0005 |
0.0006 |
0.9994 |
328.20 |
0.9761 |
0.0000 |
0.0676 |
0.0000 |
328.20 |
0.9794 |
0.0001 |
0.0524 |
0.1199 |
328.20 |
0.9822 |
0.0001 |
0.0432 |
0.2051 |
328.20 |
0.9835 |
0.0001 |
0.0302 |
0.3125 |
328.20 |
0.9864 |
0.0001 |
0.0226 |
0.4104 |
328.20 |
0.9867 |
0.0002 |
0.0181 |
0.4983 |
298.20 |
0.9809 |
0.0002 |
0.0241 |
0.3118 |
328.20 |
0.9885 |
0.0002 |
0.0140 |
0.5888 |
328.20 |
0.9900 |
0.0003 |
0.0097 |
0.6932 |
328.20 |
0.9912 |
0.0003 |
0.0064 |
0.7947 |
328.20 |
0.9918 |
0.0003 |
0.0046 |
0.8172 |
328.20 |
0.9994 |
0.0006 |
0.0004 |
0.9996 |
298.20 |
0.9849 |
0.0002 |
0.0196 |
0.4111 |
298.20 |
0.9862 |
0.0003 |
0.0175 |
0.5321 |
298.20 |
0.9875 |
0.0003 |
0.0097 |
0.5994 |
298.20 |
0.9886 |
0.0003 |
0.0092 |
0.7005 |
298.20 |
0.9915 |
0.0003 |
0.0084 |
0.7999 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid |
Mole fraction of Ethylbenzene (2) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
1.0000 |
298.15 |
0.0006 |
0.0000 |
0.9967 |
298.15 |
0.0006 |
0.1001 |
0.8874 |
298.15 |
0.0007 |
0.1969 |
0.7755 |
298.15 |
0.0008 |
0.3151 |
0.6299 |
298.15 |
0.0012 |
0.3742 |
0.5527 |
298.15 |
0.0013 |
0.4399 |
0.4513 |
298.15 |
0.0017 |
0.5496 |
0.2914 |
298.15 |
0.0026 |
0.6072 |
0.1495 |
298.15 |
0.0041 |
0.6557 |
0.0000 |
298.15 |
0.0076 |
1.0000 |
0.0000 |
298.15 |
0.0087 |
0.0000 |
1.0000 |
303.15 |
0.0006 |
0.0000 |
0.9967 |
303.15 |
0.0006 |
0.1001 |
0.8874 |
303.15 |
0.0007 |
0.1969 |
0.7755 |
303.15 |
0.0008 |
0.3151 |
0.6299 |
303.15 |
0.0011 |
0.3742 |
0.5527 |
303.15 |
0.0012 |
0.4399 |
0.4513 |
303.15 |
0.0015 |
0.5496 |
0.2914 |
303.15 |
0.0022 |
0.6072 |
0.1495 |
303.15 |
0.0035 |
0.6557 |
0.0000 |
303.15 |
0.0061 |
1.0000 |
0.0000 |
303.15 |
0.0070 |
0.0000 |
1.0000 |
308.15 |
0.0006 |
0.0000 |
0.9967 |
308.15 |
0.0005 |
0.1001 |
0.8874 |
308.15 |
0.0006 |
0.1969 |
0.7755 |
308.15 |
0.0007 |
0.3151 |
0.6299 |
308.15 |
0.0010 |
0.3742 |
0.5527 |
308.15 |
0.0011 |
0.4399 |
0.4513 |
308.15 |
0.0014 |
0.5496 |
0.2914 |
308.15 |
0.0020 |
0.6072 |
0.1495 |
308.15 |
0.0030 |
0.6557 |
0.0000 |
308.15 |
0.0051 |
1.0000 |
0.0000 |
308.15 |
0.0057 |
0.0000 |
1.0000 |
313.15 |
0.0005 |
0.0000 |
0.9967 |
313.15 |
0.0005 |
0.1001 |
0.8874 |
313.15 |
0.0006 |
0.1969 |
0.7755 |
313.15 |
0.0007 |
0.3151 |
0.6299 |
313.15 |
0.0009 |
0.3742 |
0.5527 |
313.15 |
0.0010 |
0.4399 |
0.4513 |
313.15 |
0.0013 |
0.5496 |
0.2914 |
313.15 |
0.0018 |
0.6072 |
0.1495 |
313.15 |
0.0026 |
0.6557 |
0.0000 |
313.15 |
0.0042 |
1.0000 |
0.0000 |
313.15 |
0.0047 |
Viscosity, Pa*s
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid |
Mole fraction of Ethylbenzene (2) - Liquid |
Temperature, K - Liquid |
Viscosity, Pa*s - Liquid |
0.0000 |
1.0000 |
298.15 |
0.0006 |
0.0000 |
0.9967 |
298.15 |
0.0006 |
0.1001 |
0.8874 |
298.15 |
0.0007 |
0.1969 |
0.7755 |
298.15 |
0.0008 |
0.3151 |
0.6299 |
298.15 |
0.0012 |
0.3742 |
0.5527 |
298.15 |
0.0013 |
0.4399 |
0.4513 |
298.15 |
0.0017 |
0.5496 |
0.2914 |
298.15 |
0.0026 |
0.6072 |
0.1495 |
298.15 |
0.0041 |
0.6557 |
0.0000 |
298.15 |
0.0076 |
1.0000 |
0.0000 |
298.15 |
0.0087 |
0.0000 |
1.0000 |
303.15 |
0.0006 |
0.0000 |
0.9967 |
303.15 |
0.0006 |
0.1001 |
0.8874 |
303.15 |
0.0007 |
0.1969 |
0.7755 |
303.15 |
0.0008 |
0.3151 |
0.6299 |
303.15 |
0.0011 |
0.3742 |
0.5527 |
303.15 |
0.0012 |
0.4399 |
0.4513 |
303.15 |
0.0015 |
0.5496 |
0.2914 |
303.15 |
0.0022 |
0.6072 |
0.1495 |
303.15 |
0.0035 |
0.6557 |
0.0000 |
303.15 |
0.0061 |
1.0000 |
0.0000 |
303.15 |
0.0070 |
0.0000 |
1.0000 |
308.15 |
0.0006 |
0.0000 |
0.9967 |
308.15 |
0.0005 |
0.1001 |
0.8874 |
308.15 |
0.0006 |
0.1969 |
0.7755 |
308.15 |
0.0007 |
0.3151 |
0.6299 |
308.15 |
0.0010 |
0.3742 |
0.5527 |
308.15 |
0.0011 |
0.4399 |
0.4513 |
308.15 |
0.0014 |
0.5496 |
0.2914 |
308.15 |
0.0020 |
0.6072 |
0.1495 |
308.15 |
0.0030 |
0.6557 |
0.0000 |
308.15 |
0.0051 |
1.0000 |
0.0000 |
308.15 |
0.0057 |
0.0000 |
1.0000 |
313.15 |
0.0005 |
0.0000 |
0.9967 |
313.15 |
0.0005 |
0.1001 |
0.8874 |
313.15 |
0.0006 |
0.1969 |
0.7755 |
313.15 |
0.0007 |
0.3151 |
0.6299 |
313.15 |
0.0009 |
0.3742 |
0.5527 |
313.15 |
0.0010 |
0.4399 |
0.4513 |
313.15 |
0.0013 |
0.5496 |
0.2914 |
313.15 |
0.0018 |
0.6072 |
0.1495 |
313.15 |
0.0026 |
0.6557 |
0.0000 |
313.15 |
0.0042 |
1.0000 |
0.0000 |
313.15 |
0.0047 |
Interfacial tension, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid mixture 1 |
Mole fraction of Ethylbenzene (2) - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
298.15 |
0.0000 |
0.9967 |
0.0346 |
298.15 |
0.0503 |
0.9426 |
0.0224 |
298.15 |
0.1001 |
0.8874 |
0.0167 |
298.15 |
0.1969 |
0.7755 |
0.0138 |
298.15 |
0.3151 |
0.6299 |
0.0117 |
298.15 |
0.3742 |
0.5527 |
0.0106 |
298.15 |
0.4399 |
0.4513 |
0.0098 |
313.15 |
0.0000 |
0.9967 |
0.0307 |
313.15 |
0.0503 |
0.9426 |
0.0197 |
313.15 |
0.1001 |
0.8874 |
0.0161 |
313.15 |
0.1969 |
0.7755 |
0.0134 |
313.15 |
0.3151 |
0.6299 |
0.0114 |
313.15 |
0.3742 |
0.5527 |
0.0104 |
313.15 |
0.4399 |
0.4513 |
0.0092 |
Interfacial tension, N/m
[ref]
Fixed |
Measured |
Temperature, K - Liquid mixture 1 |
Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid mixture 1 |
Mole fraction of Ethylbenzene (2) - Liquid mixture 1 |
Interfacial tension, N/m - Liquid mixture 1 |
298.15 |
0.0000 |
0.9967 |
0.0346 |
298.15 |
0.0503 |
0.9426 |
0.0224 |
298.15 |
0.1001 |
0.8874 |
0.0167 |
298.15 |
0.1969 |
0.7755 |
0.0138 |
298.15 |
0.3151 |
0.6299 |
0.0117 |
298.15 |
0.3742 |
0.5527 |
0.0106 |
298.15 |
0.4399 |
0.4513 |
0.0098 |
313.15 |
0.0000 |
0.9967 |
0.0307 |
313.15 |
0.0503 |
0.9426 |
0.0197 |
313.15 |
0.1001 |
0.8874 |
0.0161 |
313.15 |
0.1969 |
0.7755 |
0.0134 |
313.15 |
0.3151 |
0.6299 |
0.0114 |
313.15 |
0.3742 |
0.5527 |
0.0104 |
313.15 |
0.4399 |
0.4513 |
0.0092 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid |
Mole fraction of Ethylbenzene (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
1.0000 |
862.5 |
298.15 |
0.0000 |
0.9967 |
863.3 |
298.15 |
0.1001 |
0.8874 |
875.8 |
298.15 |
0.1969 |
0.7755 |
890.4 |
298.15 |
0.3151 |
0.6299 |
910.4 |
298.15 |
0.3742 |
0.5527 |
919.9 |
298.15 |
0.4399 |
0.4513 |
936.7 |
298.15 |
0.5496 |
0.2914 |
958.1 |
298.15 |
0.6072 |
0.1495 |
981.0 |
298.15 |
0.6557 |
0.0000 |
1009.5 |
298.15 |
1.0000 |
0.0000 |
1009.0 |
303.15 |
0.0000 |
1.0000 |
858.1 |
303.15 |
0.0000 |
0.9967 |
858.9 |
303.15 |
0.1001 |
0.8874 |
871.4 |
303.15 |
0.1969 |
0.7755 |
886.0 |
303.15 |
0.3151 |
0.6299 |
906.0 |
303.15 |
0.3742 |
0.5527 |
915.6 |
303.15 |
0.4399 |
0.4513 |
932.4 |
303.15 |
0.5496 |
0.2914 |
953.9 |
303.15 |
0.6072 |
0.1495 |
976.8 |
303.15 |
0.6557 |
0.0000 |
1005.4 |
303.15 |
1.0000 |
0.0000 |
1004.9 |
308.15 |
0.0000 |
1.0000 |
853.7 |
308.15 |
0.0000 |
0.9967 |
854.5 |
308.15 |
0.1001 |
0.8874 |
867.0 |
308.15 |
0.1969 |
0.7755 |
881.5 |
308.15 |
0.3151 |
0.6299 |
901.6 |
308.15 |
0.3742 |
0.5527 |
911.2 |
308.15 |
0.4399 |
0.4513 |
928.1 |
308.15 |
0.5496 |
0.2914 |
949.6 |
308.15 |
0.6072 |
0.1495 |
972.6 |
308.15 |
0.6557 |
0.0000 |
1001.1 |
308.15 |
1.0000 |
0.0000 |
1000.7 |
313.15 |
0.0000 |
1.0000 |
849.3 |
313.15 |
0.0000 |
0.9967 |
849.7 |
313.15 |
0.1001 |
0.8874 |
862.4 |
313.15 |
0.1969 |
0.7755 |
877.1 |
313.15 |
0.3151 |
0.6299 |
897.2 |
313.15 |
0.3742 |
0.5527 |
907.0 |
313.15 |
0.4399 |
0.4513 |
923.8 |
313.15 |
0.5496 |
0.2914 |
945.4 |
313.15 |
0.6072 |
0.1495 |
968.4 |
313.15 |
0.6557 |
0.0000 |
997.13 |
313.15 |
1.0000 |
0.0000 |
996.7 |
Mass density, kg/m3
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Benzenemethanol, «alpha»-methyl- (1) - Liquid |
Mole fraction of Ethylbenzene (2) - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
0.0000 |
1.0000 |
862.5 |
298.15 |
0.0000 |
0.9967 |
863.3 |
298.15 |
0.1001 |
0.8874 |
875.8 |
298.15 |
0.1969 |
0.7755 |
890.4 |
298.15 |
0.3151 |
0.6299 |
910.4 |
298.15 |
0.3742 |
0.5527 |
919.9 |
298.15 |
0.4399 |
0.4513 |
936.7 |
298.15 |
0.5496 |
0.2914 |
958.1 |
298.15 |
0.6072 |
0.1495 |
981.0 |
298.15 |
0.6557 |
0.0000 |
1009.5 |
298.15 |
1.0000 |
0.0000 |
1009.0 |
303.15 |
0.0000 |
1.0000 |
858.1 |
303.15 |
0.0000 |
0.9967 |
858.9 |
303.15 |
0.1001 |
0.8874 |
871.4 |
303.15 |
0.1969 |
0.7755 |
886.0 |
303.15 |
0.3151 |
0.6299 |
906.0 |
303.15 |
0.3742 |
0.5527 |
915.6 |
303.15 |
0.4399 |
0.4513 |
932.4 |
303.15 |
0.5496 |
0.2914 |
953.9 |
303.15 |
0.6072 |
0.1495 |
976.8 |
303.15 |
0.6557 |
0.0000 |
1005.4 |
303.15 |
1.0000 |
0.0000 |
1004.9 |
308.15 |
0.0000 |
1.0000 |
853.7 |
308.15 |
0.0000 |
0.9967 |
854.5 |
308.15 |
0.1001 |
0.8874 |
867.0 |
308.15 |
0.1969 |
0.7755 |
881.5 |
308.15 |
0.3151 |
0.6299 |
901.6 |
308.15 |
0.3742 |
0.5527 |
911.2 |
308.15 |
0.4399 |
0.4513 |
928.1 |
308.15 |
0.5496 |
0.2914 |
949.6 |
308.15 |
0.6072 |
0.1495 |
972.6 |
308.15 |
0.6557 |
0.0000 |
1001.1 |
308.15 |
1.0000 |
0.0000 |
1000.7 |
313.15 |
0.0000 |
1.0000 |
849.3 |
313.15 |
0.0000 |
0.9967 |
849.7 |
313.15 |
0.1001 |
0.8874 |
862.4 |
313.15 |
0.1969 |
0.7755 |
877.1 |
313.15 |
0.3151 |
0.6299 |
897.2 |
313.15 |
0.3742 |
0.5527 |
907.0 |
313.15 |
0.4399 |
0.4513 |
923.8 |
313.15 |
0.5496 |
0.2914 |
945.4 |
313.15 |
0.6072 |
0.1495 |
968.4 |
313.15 |
0.6557 |
0.0000 |
997.13 |
313.15 |
1.0000 |
0.0000 |
996.7 |
Sources