Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0025 |
| 288.15 | 0.1000 | 0.0021 |
| 288.15 | 0.2000 | 0.0020 |
| 288.15 | 0.2999 | 0.0020 |
| 288.15 | 0.3998 | 0.0021 |
| 288.15 | 0.4999 | 0.0022 |
| 288.15 | 0.6001 | 0.0023 |
| 288.15 | 0.7001 | 0.0025 |
| 288.15 | 0.8002 | 0.0027 |
| 288.15 | 0.8997 | 0.0029 |
| 288.15 | 1.0000 | 0.0032 |
| 293.15 | 0.0000 | 0.0022 |
| 293.15 | 0.1000 | 0.0019 |
| 293.15 | 0.2000 | 0.0018 |
| 293.15 | 0.2999 | 0.0018 |
| 293.15 | 0.3998 | 0.0019 |
| 293.15 | 0.4999 | 0.0020 |
| 293.15 | 0.6001 | 0.0021 |
| 293.15 | 0.7001 | 0.0022 |
| 293.15 | 0.8002 | 0.0024 |
| 293.15 | 0.8997 | 0.0026 |
| 293.15 | 1.0000 | 0.0028 |
| 298.15 | 0.0000 | 0.0020 |
| 298.15 | 0.1000 | 0.0017 |
| 298.15 | 0.2000 | 0.0016 |
| 298.15 | 0.2999 | 0.0016 |
| 298.15 | 0.3998 | 0.0017 |
| 298.15 | 0.4999 | 0.0018 |
| 298.15 | 0.6001 | 0.0019 |
| 298.15 | 0.7001 | 0.0020 |
| 298.15 | 0.8002 | 0.0021 |
| 298.15 | 0.8997 | 0.0023 |
| 298.15 | 1.0000 | 0.0025 |
| 303.15 | 0.0000 | 0.0017 |
| 303.15 | 0.1000 | 0.0015 |
| 303.15 | 0.2000 | 0.0015 |
| 303.15 | 0.2999 | 0.0015 |
| 303.15 | 0.3998 | 0.0015 |
| 303.15 | 0.4999 | 0.0016 |
| 303.15 | 0.6001 | 0.0017 |
| 303.15 | 0.7001 | 0.0018 |
| 303.15 | 0.8002 | 0.0019 |
| 303.15 | 0.8997 | 0.0021 |
| 303.15 | 1.0000 | 0.0022 |
| 308.15 | 0.0000 | 0.0015 |
| 308.15 | 0.1000 | 0.0014 |
| 308.15 | 0.2000 | 0.0013 |
| 308.15 | 0.2999 | 0.0013 |
| 308.15 | 0.3998 | 0.0014 |
| 308.15 | 0.4999 | 0.0014 |
| 308.15 | 0.6001 | 0.0015 |
| 308.15 | 0.7001 | 0.0016 |
| 308.15 | 0.8002 | 0.0017 |
| 308.15 | 0.8997 | 0.0019 |
| 308.15 | 1.0000 | 0.0020 |
| 313.15 | 0.0000 | 0.0014 |
| 313.15 | 0.1000 | 0.0012 |
| 313.15 | 0.2000 | 0.0012 |
| 313.15 | 0.2999 | 0.0012 |
| 313.15 | 0.3998 | 0.0013 |
| 313.15 | 0.4999 | 0.0013 |
| 313.15 | 0.6001 | 0.0014 |
| 313.15 | 0.7001 | 0.0015 |
| 313.15 | 0.8002 | 0.0016 |
| 313.15 | 0.8997 | 0.0017 |
| 313.15 | 1.0000 | 0.0018 |
| 318.15 | 0.0000 | 0.0012 |
| 318.15 | 0.1000 | 0.0011 |
| 318.15 | 0.2000 | 0.0011 |
| 318.15 | 0.2999 | 0.0011 |
| 318.15 | 0.3998 | 0.0011 |
| 318.15 | 0.4999 | 0.0012 |
| 318.15 | 0.6001 | 0.0013 |
| 318.15 | 0.7001 | 0.0014 |
| 318.15 | 0.8002 | 0.0014 |
| 318.15 | 0.8997 | 0.0015 |
| 318.15 | 1.0000 | 0.0017 |
| 323.15 | 0.0000 | 0.0011 |
| 323.15 | 0.1000 | 0.0010 |
| 323.15 | 0.2000 | 0.0010 |
| 323.15 | 0.2999 | 0.0010 |
| 323.15 | 0.3998 | 0.0011 |
| 323.15 | 0.4999 | 0.0011 |
| 323.15 | 0.6001 | 0.0012 |
| 323.15 | 0.7001 | 0.0013 |
| 323.15 | 0.8002 | 0.0013 |
| 323.15 | 0.8997 | 0.0014 |
| 323.15 | 1.0000 | 0.0015 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0025 |
| 288.15 | 0.1000 | 0.0021 |
| 288.15 | 0.2000 | 0.0020 |
| 288.15 | 0.2999 | 0.0020 |
| 288.15 | 0.3998 | 0.0021 |
| 288.15 | 0.4999 | 0.0022 |
| 288.15 | 0.6001 | 0.0023 |
| 288.15 | 0.7001 | 0.0025 |
| 288.15 | 0.8002 | 0.0027 |
| 288.15 | 0.8997 | 0.0029 |
| 288.15 | 1.0000 | 0.0032 |
| 293.15 | 0.0000 | 0.0022 |
| 293.15 | 0.1000 | 0.0019 |
| 293.15 | 0.2000 | 0.0018 |
| 293.15 | 0.2999 | 0.0018 |
| 293.15 | 0.3998 | 0.0019 |
| 293.15 | 0.4999 | 0.0020 |
| 293.15 | 0.6001 | 0.0021 |
| 293.15 | 0.7001 | 0.0022 |
| 293.15 | 0.8002 | 0.0024 |
| 293.15 | 0.8997 | 0.0026 |
| 293.15 | 1.0000 | 0.0028 |
| 298.15 | 0.0000 | 0.0020 |
| 298.15 | 0.1000 | 0.0017 |
| 298.15 | 0.2000 | 0.0016 |
| 298.15 | 0.2999 | 0.0016 |
| 298.15 | 0.3998 | 0.0017 |
| 298.15 | 0.4999 | 0.0018 |
| 298.15 | 0.6001 | 0.0019 |
| 298.15 | 0.7001 | 0.0020 |
| 298.15 | 0.8002 | 0.0021 |
| 298.15 | 0.8997 | 0.0023 |
| 298.15 | 1.0000 | 0.0025 |
| 303.15 | 0.0000 | 0.0017 |
| 303.15 | 0.1000 | 0.0015 |
| 303.15 | 0.2000 | 0.0015 |
| 303.15 | 0.2999 | 0.0015 |
| 303.15 | 0.3998 | 0.0015 |
| 303.15 | 0.4999 | 0.0016 |
| 303.15 | 0.6001 | 0.0017 |
| 303.15 | 0.7001 | 0.0018 |
| 303.15 | 0.8002 | 0.0019 |
| 303.15 | 0.8997 | 0.0021 |
| 303.15 | 1.0000 | 0.0022 |
| 308.15 | 0.0000 | 0.0015 |
| 308.15 | 0.1000 | 0.0014 |
| 308.15 | 0.2000 | 0.0013 |
| 308.15 | 0.2999 | 0.0013 |
| 308.15 | 0.3998 | 0.0014 |
| 308.15 | 0.4999 | 0.0014 |
| 308.15 | 0.6001 | 0.0015 |
| 308.15 | 0.7001 | 0.0016 |
| 308.15 | 0.8002 | 0.0017 |
| 308.15 | 0.8997 | 0.0019 |
| 308.15 | 1.0000 | 0.0020 |
| 313.15 | 0.0000 | 0.0014 |
| 313.15 | 0.1000 | 0.0012 |
| 313.15 | 0.2000 | 0.0012 |
| 313.15 | 0.2999 | 0.0012 |
| 313.15 | 0.3998 | 0.0013 |
| 313.15 | 0.4999 | 0.0013 |
| 313.15 | 0.6001 | 0.0014 |
| 313.15 | 0.7001 | 0.0015 |
| 313.15 | 0.8002 | 0.0016 |
| 313.15 | 0.8997 | 0.0017 |
| 313.15 | 1.0000 | 0.0018 |
| 318.15 | 0.0000 | 0.0012 |
| 318.15 | 0.1000 | 0.0011 |
| 318.15 | 0.2000 | 0.0011 |
| 318.15 | 0.2999 | 0.0011 |
| 318.15 | 0.3998 | 0.0011 |
| 318.15 | 0.4999 | 0.0012 |
| 318.15 | 0.6001 | 0.0013 |
| 318.15 | 0.7001 | 0.0014 |
| 318.15 | 0.8002 | 0.0014 |
| 318.15 | 0.8997 | 0.0015 |
| 318.15 | 1.0000 | 0.0017 |
| 323.15 | 0.0000 | 0.0011 |
| 323.15 | 0.1000 | 0.0010 |
| 323.15 | 0.2000 | 0.0010 |
| 323.15 | 0.2999 | 0.0010 |
| 323.15 | 0.3998 | 0.0011 |
| 323.15 | 0.4999 | 0.0011 |
| 323.15 | 0.6001 | 0.0012 |
| 323.15 | 0.7001 | 0.0013 |
| 323.15 | 0.8002 | 0.0013 |
| 323.15 | 0.8997 | 0.0014 |
| 323.15 | 1.0000 | 0.0015 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.3875 |
| 288.15 | 0.1000 | 1.394 |
| 288.15 | 0.2000 | 1.3993 |
| 288.15 | 0.2999 | 1.4037 |
| 288.15 | 0.3998 | 1.4075 |
| 288.15 | 0.4999 | 1.4107 |
| 288.15 | 0.6001 | 1.4135 |
| 288.15 | 0.7001 | 1.416 |
| 288.15 | 0.8002 | 1.4182 |
| 288.15 | 0.8997 | 1.4201 |
| 288.15 | 1.0000 | 1.4217 |
| 293.15 | 0.0000 | 1.3854 |
| 293.15 | 0.1000 | 1.3918 |
| 293.15 | 0.2000 | 1.3971 |
| 293.15 | 0.2999 | 1.4016 |
| 293.15 | 0.3998 | 1.4053 |
| 293.15 | 0.4999 | 1.4085 |
| 293.15 | 0.6001 | 1.4113 |
| 293.15 | 0.7001 | 1.4138 |
| 293.15 | 0.8002 | 1.416 |
| 293.15 | 0.8997 | 1.4179 |
| 293.15 | 1.0000 | 1.4195 |
| 298.15 | 0.0000 | 1.3834 |
| 298.15 | 0.1000 | 1.3897 |
| 298.15 | 0.2000 | 1.395 |
| 298.15 | 0.2999 | 1.3994 |
| 298.15 | 0.3998 | 1.4031 |
| 298.15 | 0.4999 | 1.4063 |
| 298.15 | 0.6001 | 1.4091 |
| 298.15 | 0.7001 | 1.4116 |
| 298.15 | 0.8002 | 1.4138 |
| 298.15 | 0.8997 | 1.4157 |
| 298.15 | 1.0000 | 1.4173 |
| 303.15 | 0.0000 | 1.3814 |
| 303.15 | 0.1000 | 1.3876 |
| 303.15 | 0.2000 | 1.3928 |
| 303.15 | 0.2999 | 1.3972 |
| 303.15 | 0.3998 | 1.4009 |
| 303.15 | 0.4999 | 1.4041 |
| 303.15 | 0.6001 | 1.4069 |
| 303.15 | 0.7001 | 1.4094 |
| 303.15 | 0.8002 | 1.4116 |
| 303.15 | 0.8997 | 1.4135 |
| 303.15 | 1.0000 | 1.4151 |
| 308.15 | 0.0000 | 1.3792 |
| 308.15 | 0.1000 | 1.3854 |
| 308.15 | 0.2000 | 1.3906 |
| 308.15 | 0.2999 | 1.3949 |
| 308.15 | 0.3998 | 1.3986 |
| 308.15 | 0.4999 | 1.4018 |
| 308.15 | 0.6001 | 1.4047 |
| 308.15 | 0.7001 | 1.4072 |
| 308.15 | 0.8002 | 1.4094 |
| 308.15 | 0.8997 | 1.4113 |
| 308.15 | 1.0000 | 1.4129 |
| 313.15 | 0.0000 | 1.377 |
| 313.15 | 0.1000 | 1.3831 |
| 313.15 | 0.2000 | 1.3883 |
| 313.15 | 0.2999 | 1.3927 |
| 313.15 | 0.3998 | 1.3964 |
| 313.15 | 0.4999 | 1.3996 |
| 313.15 | 0.6001 | 1.4025 |
| 313.15 | 0.7001 | 1.4049 |
| 313.15 | 0.8002 | 1.4072 |
| 313.15 | 0.8997 | 1.4091 |
| 313.15 | 1.0000 | 1.4108 |
| 318.15 | 0.0000 | 1.3748 |
| 318.15 | 0.1000 | 1.3809 |
| 318.15 | 0.2000 | 1.3861 |
| 318.15 | 0.2999 | 1.3905 |
| 318.15 | 0.3998 | 1.3942 |
| 318.15 | 0.4999 | 1.3974 |
| 318.15 | 0.6001 | 1.4002 |
| 318.15 | 0.7001 | 1.4027 |
| 318.15 | 0.8002 | 1.4049 |
| 318.15 | 0.8997 | 1.4069 |
| 318.15 | 1.0000 | 1.4088 |
| 323.15 | 0.0000 | 1.3726 |
| 323.15 | 0.1000 | 1.3787 |
| 323.15 | 0.2000 | 1.3839 |
| 323.15 | 0.2999 | 1.3882 |
| 323.15 | 0.3998 | 1.392 |
| 323.15 | 0.4999 | 1.3952 |
| 323.15 | 0.6001 | 1.398 |
| 323.15 | 0.7001 | 1.4005 |
| 323.15 | 0.8002 | 1.4027 |
| 323.15 | 0.8997 | 1.4048 |
| 323.15 | 1.0000 | 1.4067 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.3875 |
| 288.15 | 0.1000 | 1.394 |
| 288.15 | 0.2000 | 1.3993 |
| 288.15 | 0.2999 | 1.4037 |
| 288.15 | 0.3998 | 1.4075 |
| 288.15 | 0.4999 | 1.4107 |
| 288.15 | 0.6001 | 1.4135 |
| 288.15 | 0.7001 | 1.416 |
| 288.15 | 0.8002 | 1.4182 |
| 288.15 | 0.8997 | 1.4201 |
| 288.15 | 1.0000 | 1.4217 |
| 293.15 | 0.0000 | 1.3854 |
| 293.15 | 0.1000 | 1.3918 |
| 293.15 | 0.2000 | 1.3971 |
| 293.15 | 0.2999 | 1.4016 |
| 293.15 | 0.3998 | 1.4053 |
| 293.15 | 0.4999 | 1.4085 |
| 293.15 | 0.6001 | 1.4113 |
| 293.15 | 0.7001 | 1.4138 |
| 293.15 | 0.8002 | 1.416 |
| 293.15 | 0.8997 | 1.4179 |
| 293.15 | 1.0000 | 1.4195 |
| 298.15 | 0.0000 | 1.3834 |
| 298.15 | 0.1000 | 1.3897 |
| 298.15 | 0.2000 | 1.395 |
| 298.15 | 0.2999 | 1.3994 |
| 298.15 | 0.3998 | 1.4031 |
| 298.15 | 0.4999 | 1.4063 |
| 298.15 | 0.6001 | 1.4091 |
| 298.15 | 0.7001 | 1.4116 |
| 298.15 | 0.8002 | 1.4138 |
| 298.15 | 0.8997 | 1.4157 |
| 298.15 | 1.0000 | 1.4173 |
| 303.15 | 0.0000 | 1.3814 |
| 303.15 | 0.1000 | 1.3876 |
| 303.15 | 0.2000 | 1.3928 |
| 303.15 | 0.2999 | 1.3972 |
| 303.15 | 0.3998 | 1.4009 |
| 303.15 | 0.4999 | 1.4041 |
| 303.15 | 0.6001 | 1.4069 |
| 303.15 | 0.7001 | 1.4094 |
| 303.15 | 0.8002 | 1.4116 |
| 303.15 | 0.8997 | 1.4135 |
| 303.15 | 1.0000 | 1.4151 |
| 308.15 | 0.0000 | 1.3792 |
| 308.15 | 0.1000 | 1.3854 |
| 308.15 | 0.2000 | 1.3906 |
| 308.15 | 0.2999 | 1.3949 |
| 308.15 | 0.3998 | 1.3986 |
| 308.15 | 0.4999 | 1.4018 |
| 308.15 | 0.6001 | 1.4047 |
| 308.15 | 0.7001 | 1.4072 |
| 308.15 | 0.8002 | 1.4094 |
| 308.15 | 0.8997 | 1.4113 |
| 308.15 | 1.0000 | 1.4129 |
| 313.15 | 0.0000 | 1.377 |
| 313.15 | 0.1000 | 1.3831 |
| 313.15 | 0.2000 | 1.3883 |
| 313.15 | 0.2999 | 1.3927 |
| 313.15 | 0.3998 | 1.3964 |
| 313.15 | 0.4999 | 1.3996 |
| 313.15 | 0.6001 | 1.4025 |
| 313.15 | 0.7001 | 1.4049 |
| 313.15 | 0.8002 | 1.4072 |
| 313.15 | 0.8997 | 1.4091 |
| 313.15 | 1.0000 | 1.4108 |
| 318.15 | 0.0000 | 1.3748 |
| 318.15 | 0.1000 | 1.3809 |
| 318.15 | 0.2000 | 1.3861 |
| 318.15 | 0.2999 | 1.3905 |
| 318.15 | 0.3998 | 1.3942 |
| 318.15 | 0.4999 | 1.3974 |
| 318.15 | 0.6001 | 1.4002 |
| 318.15 | 0.7001 | 1.4027 |
| 318.15 | 0.8002 | 1.4049 |
| 318.15 | 0.8997 | 1.4069 |
| 318.15 | 1.0000 | 1.4088 |
| 323.15 | 0.0000 | 1.3726 |
| 323.15 | 0.1000 | 1.3787 |
| 323.15 | 0.2000 | 1.3839 |
| 323.15 | 0.2999 | 1.3882 |
| 323.15 | 0.3998 | 1.392 |
| 323.15 | 0.4999 | 1.3952 |
| 323.15 | 0.6001 | 1.398 |
| 323.15 | 0.7001 | 1.4005 |
| 323.15 | 0.8002 | 1.4027 |
| 323.15 | 0.8997 | 1.4048 |
| 323.15 | 1.0000 | 1.4067 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 807.75 |
| 288.15 | 0.1000 | 854.4 |
| 288.15 | 0.2000 | 891.88 |
| 288.15 | 0.2999 | 922.67 |
| 288.15 | 0.3998 | 948.47 |
| 288.15 | 0.4999 | 970.46 |
| 288.15 | 0.6001 | 989.43 |
| 288.15 | 0.7001 | 1005.92 |
| 288.15 | 0.8002 | 1020.45 |
| 288.15 | 0.8997 | 1033.27 |
| 288.15 | 1.0000 | 1044.83 |
| 293.15 | 0.0000 | 803.77 |
| 293.15 | 0.1000 | 850.08 |
| 293.15 | 0.2000 | 887.33 |
| 293.15 | 0.2999 | 917.95 |
| 293.15 | 0.3998 | 943.61 |
| 293.15 | 0.4999 | 965.5 |
| 293.15 | 0.6001 | 984.4 |
| 293.15 | 0.7001 | 1000.83 |
| 293.15 | 0.8002 | 1015.31 |
| 293.15 | 0.8997 | 1028.1 |
| 293.15 | 1.0000 | 1039.63 |
| 298.15 | 0.0000 | 799.76 |
| 298.15 | 0.1000 | 845.75 |
| 298.15 | 0.2000 | 882.77 |
| 298.15 | 0.2999 | 913.21 |
| 298.15 | 0.3998 | 938.75 |
| 298.15 | 0.4999 | 960.54 |
| 298.15 | 0.6001 | 979.36 |
| 298.15 | 0.7001 | 995.74 |
| 298.15 | 0.8002 | 1010.18 |
| 298.15 | 0.8997 | 1022.93 |
| 298.15 | 1.0000 | 1034.44 |
| 303.15 | 0.0000 | 795.72 |
| 303.15 | 0.1000 | 841.4 |
| 303.15 | 0.2000 | 878.18 |
| 303.15 | 0.2999 | 908.46 |
| 303.15 | 0.3998 | 933.87 |
| 303.15 | 0.4999 | 955.57 |
| 303.15 | 0.6001 | 974.32 |
| 303.15 | 0.7001 | 990.64 |
| 303.15 | 0.8002 | 1005.04 |
| 303.15 | 0.8997 | 1017.76 |
| 303.15 | 1.0000 | 1029.25 |
| 308.15 | 0.0000 | 791.64 |
| 308.15 | 0.1000 | 837.02 |
| 308.15 | 0.2000 | 873.57 |
| 308.15 | 0.2999 | 903.69 |
| 308.15 | 0.3998 | 928.98 |
| 308.15 | 0.4999 | 950.59 |
| 308.15 | 0.6001 | 969.27 |
| 308.15 | 0.7001 | 985.54 |
| 308.15 | 0.8002 | 999.9 |
| 308.15 | 0.8997 | 1012.6 |
| 308.15 | 1.0000 | 1024.08 |
| 313.15 | 0.0000 | 787.52 |
| 313.15 | 0.1000 | 832.6 |
| 313.15 | 0.2000 | 868.94 |
| 313.15 | 0.2999 | 898.89 |
| 313.15 | 0.3998 | 924.07 |
| 313.15 | 0.4999 | 945.59 |
| 313.15 | 0.6001 | 964.21 |
| 313.15 | 0.7001 | 980.44 |
| 313.15 | 0.8002 | 994.77 |
| 313.15 | 0.8997 | 1007.44 |
| 313.15 | 1.0000 | 1018.9 |
| 318.15 | 0.0000 | 783.36 |
| 318.15 | 0.1000 | 828.14 |
| 318.15 | 0.2000 | 864.27 |
| 318.15 | 0.2999 | 894.07 |
| 318.15 | 0.3998 | 919.14 |
| 318.15 | 0.4999 | 940.58 |
| 318.15 | 0.6001 | 959.14 |
| 318.15 | 0.7001 | 975.33 |
| 318.15 | 0.8002 | 989.62 |
| 318.15 | 0.8997 | 1002.28 |
| 318.15 | 1.0000 | 1013.72 |
| 323.15 | 0.0000 | 779.14 |
| 323.15 | 0.1000 | 823.65 |
| 323.15 | 0.2000 | 859.57 |
| 323.15 | 0.2999 | 889.22 |
| 323.15 | 0.3998 | 914.18 |
| 323.15 | 0.4999 | 935.55 |
| 323.15 | 0.6001 | 954.05 |
| 323.15 | 0.7001 | 970.21 |
| 323.15 | 0.8002 | 984.48 |
| 323.15 | 0.8997 | 997.12 |
| 323.15 | 1.0000 | 1008.55 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Butanedioic acid, diethyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 807.75 |
| 288.15 | 0.1000 | 854.4 |
| 288.15 | 0.2000 | 891.88 |
| 288.15 | 0.2999 | 922.67 |
| 288.15 | 0.3998 | 948.47 |
| 288.15 | 0.4999 | 970.46 |
| 288.15 | 0.6001 | 989.43 |
| 288.15 | 0.7001 | 1005.92 |
| 288.15 | 0.8002 | 1020.45 |
| 288.15 | 0.8997 | 1033.27 |
| 288.15 | 1.0000 | 1044.83 |
| 293.15 | 0.0000 | 803.77 |
| 293.15 | 0.1000 | 850.08 |
| 293.15 | 0.2000 | 887.33 |
| 293.15 | 0.2999 | 917.95 |
| 293.15 | 0.3998 | 943.61 |
| 293.15 | 0.4999 | 965.5 |
| 293.15 | 0.6001 | 984.4 |
| 293.15 | 0.7001 | 1000.83 |
| 293.15 | 0.8002 | 1015.31 |
| 293.15 | 0.8997 | 1028.1 |
| 293.15 | 1.0000 | 1039.63 |
| 298.15 | 0.0000 | 799.76 |
| 298.15 | 0.1000 | 845.75 |
| 298.15 | 0.2000 | 882.77 |
| 298.15 | 0.2999 | 913.21 |
| 298.15 | 0.3998 | 938.75 |
| 298.15 | 0.4999 | 960.54 |
| 298.15 | 0.6001 | 979.36 |
| 298.15 | 0.7001 | 995.74 |
| 298.15 | 0.8002 | 1010.18 |
| 298.15 | 0.8997 | 1022.93 |
| 298.15 | 1.0000 | 1034.44 |
| 303.15 | 0.0000 | 795.72 |
| 303.15 | 0.1000 | 841.4 |
| 303.15 | 0.2000 | 878.18 |
| 303.15 | 0.2999 | 908.46 |
| 303.15 | 0.3998 | 933.87 |
| 303.15 | 0.4999 | 955.57 |
| 303.15 | 0.6001 | 974.32 |
| 303.15 | 0.7001 | 990.64 |
| 303.15 | 0.8002 | 1005.04 |
| 303.15 | 0.8997 | 1017.76 |
| 303.15 | 1.0000 | 1029.25 |
| 308.15 | 0.0000 | 791.64 |
| 308.15 | 0.1000 | 837.02 |
| 308.15 | 0.2000 | 873.57 |
| 308.15 | 0.2999 | 903.69 |
| 308.15 | 0.3998 | 928.98 |
| 308.15 | 0.4999 | 950.59 |
| 308.15 | 0.6001 | 969.27 |
| 308.15 | 0.7001 | 985.54 |
| 308.15 | 0.8002 | 999.9 |
| 308.15 | 0.8997 | 1012.6 |
| 308.15 | 1.0000 | 1024.08 |
| 313.15 | 0.0000 | 787.52 |
| 313.15 | 0.1000 | 832.6 |
| 313.15 | 0.2000 | 868.94 |
| 313.15 | 0.2999 | 898.89 |
| 313.15 | 0.3998 | 924.07 |
| 313.15 | 0.4999 | 945.59 |
| 313.15 | 0.6001 | 964.21 |
| 313.15 | 0.7001 | 980.44 |
| 313.15 | 0.8002 | 994.77 |
| 313.15 | 0.8997 | 1007.44 |
| 313.15 | 1.0000 | 1018.9 |
| 318.15 | 0.0000 | 783.36 |
| 318.15 | 0.1000 | 828.14 |
| 318.15 | 0.2000 | 864.27 |
| 318.15 | 0.2999 | 894.07 |
| 318.15 | 0.3998 | 919.14 |
| 318.15 | 0.4999 | 940.58 |
| 318.15 | 0.6001 | 959.14 |
| 318.15 | 0.7001 | 975.33 |
| 318.15 | 0.8002 | 989.62 |
| 318.15 | 0.8997 | 1002.28 |
| 318.15 | 1.0000 | 1013.72 |
| 323.15 | 0.0000 | 779.14 |
| 323.15 | 0.1000 | 823.65 |
| 323.15 | 0.2000 | 859.57 |
| 323.15 | 0.2999 | 889.22 |
| 323.15 | 0.3998 | 914.18 |
| 323.15 | 0.4999 | 935.55 |
| 323.15 | 0.6001 | 954.05 |
| 323.15 | 0.7001 | 970.21 |
| 323.15 | 0.8002 | 984.48 |
| 323.15 | 0.8997 | 997.12 |
| 323.15 | 1.0000 | 1008.55 |