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 | 0.0034 |
| 288.15 | 0.1000 | 0.0027 |
| 288.15 | 0.2001 | 0.0024 |
| 288.15 | 0.3000 | 0.0023 |
| 288.15 | 0.3999 | 0.0023 |
| 288.15 | 0.5000 | 0.0023 |
| 288.15 | 0.6001 | 0.0024 |
| 288.15 | 0.6998 | 0.0025 |
| 288.15 | 0.7999 | 0.0027 |
| 288.15 | 0.8997 | 0.0029 |
| 288.15 | 1.0000 | 0.0032 |
| 293.15 | 0.0000 | 0.0029 |
| 293.15 | 0.1000 | 0.0023 |
| 293.15 | 0.2001 | 0.0021 |
| 293.15 | 0.3000 | 0.0020 |
| 293.15 | 0.3999 | 0.0020 |
| 293.15 | 0.5000 | 0.0021 |
| 293.15 | 0.6001 | 0.0021 |
| 293.15 | 0.6998 | 0.0022 |
| 293.15 | 0.7999 | 0.0024 |
| 293.15 | 0.8997 | 0.0026 |
| 293.15 | 1.0000 | 0.0028 |
| 298.15 | 0.0000 | 0.0026 |
| 298.15 | 0.1000 | 0.0021 |
| 298.15 | 0.2001 | 0.0019 |
| 298.15 | 0.3000 | 0.0018 |
| 298.15 | 0.3999 | 0.0018 |
| 298.15 | 0.5000 | 0.0019 |
| 298.15 | 0.6001 | 0.0019 |
| 298.15 | 0.6998 | 0.0020 |
| 298.15 | 0.7999 | 0.0021 |
| 298.15 | 0.8997 | 0.0023 |
| 298.15 | 1.0000 | 0.0025 |
| 303.15 | 0.0000 | 0.0023 |
| 303.15 | 0.1000 | 0.0018 |
| 303.15 | 0.2001 | 0.0017 |
| 303.15 | 0.3000 | 0.0016 |
| 303.15 | 0.3999 | 0.0016 |
| 303.15 | 0.5000 | 0.0017 |
| 303.15 | 0.6001 | 0.0017 |
| 303.15 | 0.6998 | 0.0018 |
| 303.15 | 0.7999 | 0.0019 |
| 303.15 | 0.8997 | 0.0021 |
| 303.15 | 1.0000 | 0.0022 |
| 308.15 | 0.0000 | 0.0020 |
| 308.15 | 0.1000 | 0.0016 |
| 308.15 | 0.2001 | 0.0015 |
| 308.15 | 0.3000 | 0.0015 |
| 308.15 | 0.3999 | 0.0015 |
| 308.15 | 0.5000 | 0.0015 |
| 308.15 | 0.6001 | 0.0016 |
| 308.15 | 0.6998 | 0.0016 |
| 308.15 | 0.7999 | 0.0017 |
| 308.15 | 0.8997 | 0.0019 |
| 308.15 | 1.0000 | 0.0020 |
| 313.15 | 0.0000 | 0.0018 |
| 313.15 | 0.1000 | 0.0015 |
| 313.15 | 0.2001 | 0.0014 |
| 313.15 | 0.3000 | 0.0014 |
| 313.15 | 0.3999 | 0.0014 |
| 313.15 | 0.5000 | 0.0014 |
| 313.15 | 0.6001 | 0.0014 |
| 313.15 | 0.6998 | 0.0015 |
| 313.15 | 0.7999 | 0.0016 |
| 313.15 | 0.8997 | 0.0017 |
| 313.15 | 1.0000 | 0.0018 |
| 318.15 | 0.0000 | 0.0016 |
| 318.15 | 0.1000 | 0.0013 |
| 318.15 | 0.2001 | 0.0012 |
| 318.15 | 0.3000 | 0.0012 |
| 318.15 | 0.3999 | 0.0012 |
| 318.15 | 0.5000 | 0.0013 |
| 318.15 | 0.6001 | 0.0013 |
| 318.15 | 0.6998 | 0.0014 |
| 318.15 | 0.7999 | 0.0015 |
| 318.15 | 0.8997 | 0.0016 |
| 318.15 | 1.0000 | 0.0017 |
| 323.15 | 0.0000 | 0.0014 |
| 323.15 | 0.1000 | 0.0012 |
| 323.15 | 0.2001 | 0.0011 |
| 323.15 | 0.3000 | 0.0011 |
| 323.15 | 0.3999 | 0.0011 |
| 323.15 | 0.5000 | 0.0012 |
| 323.15 | 0.6001 | 0.0012 |
| 323.15 | 0.6998 | 0.0013 |
| 323.15 | 0.7999 | 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 | 0.0034 |
| 288.15 | 0.1000 | 0.0027 |
| 288.15 | 0.2001 | 0.0024 |
| 288.15 | 0.3000 | 0.0023 |
| 288.15 | 0.3999 | 0.0023 |
| 288.15 | 0.5000 | 0.0023 |
| 288.15 | 0.6001 | 0.0024 |
| 288.15 | 0.6998 | 0.0025 |
| 288.15 | 0.7999 | 0.0027 |
| 288.15 | 0.8997 | 0.0029 |
| 288.15 | 1.0000 | 0.0032 |
| 293.15 | 0.0000 | 0.0029 |
| 293.15 | 0.1000 | 0.0023 |
| 293.15 | 0.2001 | 0.0021 |
| 293.15 | 0.3000 | 0.0020 |
| 293.15 | 0.3999 | 0.0020 |
| 293.15 | 0.5000 | 0.0021 |
| 293.15 | 0.6001 | 0.0021 |
| 293.15 | 0.6998 | 0.0022 |
| 293.15 | 0.7999 | 0.0024 |
| 293.15 | 0.8997 | 0.0026 |
| 293.15 | 1.0000 | 0.0028 |
| 298.15 | 0.0000 | 0.0026 |
| 298.15 | 0.1000 | 0.0021 |
| 298.15 | 0.2001 | 0.0019 |
| 298.15 | 0.3000 | 0.0018 |
| 298.15 | 0.3999 | 0.0018 |
| 298.15 | 0.5000 | 0.0019 |
| 298.15 | 0.6001 | 0.0019 |
| 298.15 | 0.6998 | 0.0020 |
| 298.15 | 0.7999 | 0.0021 |
| 298.15 | 0.8997 | 0.0023 |
| 298.15 | 1.0000 | 0.0025 |
| 303.15 | 0.0000 | 0.0023 |
| 303.15 | 0.1000 | 0.0018 |
| 303.15 | 0.2001 | 0.0017 |
| 303.15 | 0.3000 | 0.0016 |
| 303.15 | 0.3999 | 0.0016 |
| 303.15 | 0.5000 | 0.0017 |
| 303.15 | 0.6001 | 0.0017 |
| 303.15 | 0.6998 | 0.0018 |
| 303.15 | 0.7999 | 0.0019 |
| 303.15 | 0.8997 | 0.0021 |
| 303.15 | 1.0000 | 0.0022 |
| 308.15 | 0.0000 | 0.0020 |
| 308.15 | 0.1000 | 0.0016 |
| 308.15 | 0.2001 | 0.0015 |
| 308.15 | 0.3000 | 0.0015 |
| 308.15 | 0.3999 | 0.0015 |
| 308.15 | 0.5000 | 0.0015 |
| 308.15 | 0.6001 | 0.0016 |
| 308.15 | 0.6998 | 0.0016 |
| 308.15 | 0.7999 | 0.0017 |
| 308.15 | 0.8997 | 0.0019 |
| 308.15 | 1.0000 | 0.0020 |
| 313.15 | 0.0000 | 0.0018 |
| 313.15 | 0.1000 | 0.0015 |
| 313.15 | 0.2001 | 0.0014 |
| 313.15 | 0.3000 | 0.0014 |
| 313.15 | 0.3999 | 0.0014 |
| 313.15 | 0.5000 | 0.0014 |
| 313.15 | 0.6001 | 0.0014 |
| 313.15 | 0.6998 | 0.0015 |
| 313.15 | 0.7999 | 0.0016 |
| 313.15 | 0.8997 | 0.0017 |
| 313.15 | 1.0000 | 0.0018 |
| 318.15 | 0.0000 | 0.0016 |
| 318.15 | 0.1000 | 0.0013 |
| 318.15 | 0.2001 | 0.0012 |
| 318.15 | 0.3000 | 0.0012 |
| 318.15 | 0.3999 | 0.0012 |
| 318.15 | 0.5000 | 0.0013 |
| 318.15 | 0.6001 | 0.0013 |
| 318.15 | 0.6998 | 0.0014 |
| 318.15 | 0.7999 | 0.0015 |
| 318.15 | 0.8997 | 0.0016 |
| 318.15 | 1.0000 | 0.0017 |
| 323.15 | 0.0000 | 0.0014 |
| 323.15 | 0.1000 | 0.0012 |
| 323.15 | 0.2001 | 0.0011 |
| 323.15 | 0.3000 | 0.0011 |
| 323.15 | 0.3999 | 0.0011 |
| 323.15 | 0.5000 | 0.0012 |
| 323.15 | 0.6001 | 0.0012 |
| 323.15 | 0.6998 | 0.0013 |
| 323.15 | 0.7999 | 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 | 1.4012 |
| 288.15 | 0.1000 | 1.4042 |
| 288.15 | 0.2001 | 1.4069 |
| 288.15 | 0.3000 | 1.4094 |
| 288.15 | 0.3999 | 1.4116 |
| 288.15 | 0.5000 | 1.4137 |
| 288.15 | 0.6001 | 1.4156 |
| 288.15 | 0.6998 | 1.4173 |
| 288.15 | 0.7999 | 1.419 |
| 288.15 | 0.8997 | 1.4204 |
| 288.15 | 1.0000 | 1.4217 |
| 293.15 | 0.0000 | 1.3992 |
| 293.15 | 0.1000 | 1.4021 |
| 293.15 | 0.2001 | 1.4048 |
| 293.15 | 0.3000 | 1.4072 |
| 293.15 | 0.3999 | 1.4094 |
| 293.15 | 0.5000 | 1.4115 |
| 293.15 | 0.6001 | 1.4134 |
| 293.15 | 0.6998 | 1.4151 |
| 293.15 | 0.7999 | 1.4168 |
| 293.15 | 0.8997 | 1.4182 |
| 293.15 | 1.0000 | 1.4195 |
| 298.15 | 0.0000 | 1.3972 |
| 298.15 | 0.1000 | 1.4 |
| 298.15 | 0.2001 | 1.4027 |
| 298.15 | 0.3000 | 1.405 |
| 298.15 | 0.3999 | 1.4073 |
| 298.15 | 0.5000 | 1.4093 |
| 298.15 | 0.6001 | 1.4112 |
| 298.15 | 0.6998 | 1.4129 |
| 298.15 | 0.7999 | 1.4146 |
| 298.15 | 0.8997 | 1.416 |
| 298.15 | 1.0000 | 1.4173 |
| 303.15 | 0.0000 | 1.3951 |
| 303.15 | 0.1000 | 1.3979 |
| 303.15 | 0.2001 | 1.4005 |
| 303.15 | 0.3000 | 1.4029 |
| 303.15 | 0.3999 | 1.4051 |
| 303.15 | 0.5000 | 1.4071 |
| 303.15 | 0.6001 | 1.409 |
| 303.15 | 0.6998 | 1.4107 |
| 303.15 | 0.7999 | 1.4123 |
| 303.15 | 0.8997 | 1.4138 |
| 303.15 | 1.0000 | 1.4151 |
| 308.15 | 0.0000 | 1.393 |
| 308.15 | 0.1000 | 1.3958 |
| 308.15 | 0.2001 | 1.3983 |
| 308.15 | 0.3000 | 1.4007 |
| 308.15 | 0.3999 | 1.4029 |
| 308.15 | 0.5000 | 1.4049 |
| 308.15 | 0.6001 | 1.4068 |
| 308.15 | 0.6998 | 1.4085 |
| 308.15 | 0.7999 | 1.4101 |
| 308.15 | 0.8997 | 1.4116 |
| 308.15 | 1.0000 | 1.4129 |
| 313.15 | 0.0000 | 1.391 |
| 313.15 | 0.1000 | 1.3936 |
| 313.15 | 0.2001 | 1.3962 |
| 313.15 | 0.3000 | 1.3985 |
| 313.15 | 0.3999 | 1.4007 |
| 313.15 | 0.5000 | 1.4027 |
| 313.15 | 0.6001 | 1.4046 |
| 313.15 | 0.6998 | 1.4063 |
| 313.15 | 0.7999 | 1.4079 |
| 313.15 | 0.8997 | 1.4094 |
| 313.15 | 1.0000 | 1.4108 |
| 318.15 | 0.0000 | 1.3889 |
| 318.15 | 0.1000 | 1.3915 |
| 318.15 | 0.2001 | 1.394 |
| 318.15 | 0.3000 | 1.3963 |
| 318.15 | 0.3999 | 1.3985 |
| 318.15 | 0.5000 | 1.4005 |
| 318.15 | 0.6001 | 1.4024 |
| 318.15 | 0.6998 | 1.4041 |
| 318.15 | 0.7999 | 1.4058 |
| 318.15 | 0.8997 | 1.4073 |
| 318.15 | 1.0000 | 1.4088 |
| 323.15 | 0.0000 | 1.3867 |
| 323.15 | 0.1000 | 1.3894 |
| 323.15 | 0.2001 | 1.3918 |
| 323.15 | 0.3000 | 1.3942 |
| 323.15 | 0.3999 | 1.3963 |
| 323.15 | 0.5000 | 1.3983 |
| 323.15 | 0.6001 | 1.4002 |
| 323.15 | 0.6998 | 1.402 |
| 323.15 | 0.7999 | 1.4036 |
| 323.15 | 0.8997 | 1.4052 |
| 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 | 1.4012 |
| 288.15 | 0.1000 | 1.4042 |
| 288.15 | 0.2001 | 1.4069 |
| 288.15 | 0.3000 | 1.4094 |
| 288.15 | 0.3999 | 1.4116 |
| 288.15 | 0.5000 | 1.4137 |
| 288.15 | 0.6001 | 1.4156 |
| 288.15 | 0.6998 | 1.4173 |
| 288.15 | 0.7999 | 1.419 |
| 288.15 | 0.8997 | 1.4204 |
| 288.15 | 1.0000 | 1.4217 |
| 293.15 | 0.0000 | 1.3992 |
| 293.15 | 0.1000 | 1.4021 |
| 293.15 | 0.2001 | 1.4048 |
| 293.15 | 0.3000 | 1.4072 |
| 293.15 | 0.3999 | 1.4094 |
| 293.15 | 0.5000 | 1.4115 |
| 293.15 | 0.6001 | 1.4134 |
| 293.15 | 0.6998 | 1.4151 |
| 293.15 | 0.7999 | 1.4168 |
| 293.15 | 0.8997 | 1.4182 |
| 293.15 | 1.0000 | 1.4195 |
| 298.15 | 0.0000 | 1.3972 |
| 298.15 | 0.1000 | 1.4 |
| 298.15 | 0.2001 | 1.4027 |
| 298.15 | 0.3000 | 1.405 |
| 298.15 | 0.3999 | 1.4073 |
| 298.15 | 0.5000 | 1.4093 |
| 298.15 | 0.6001 | 1.4112 |
| 298.15 | 0.6998 | 1.4129 |
| 298.15 | 0.7999 | 1.4146 |
| 298.15 | 0.8997 | 1.416 |
| 298.15 | 1.0000 | 1.4173 |
| 303.15 | 0.0000 | 1.3951 |
| 303.15 | 0.1000 | 1.3979 |
| 303.15 | 0.2001 | 1.4005 |
| 303.15 | 0.3000 | 1.4029 |
| 303.15 | 0.3999 | 1.4051 |
| 303.15 | 0.5000 | 1.4071 |
| 303.15 | 0.6001 | 1.409 |
| 303.15 | 0.6998 | 1.4107 |
| 303.15 | 0.7999 | 1.4123 |
| 303.15 | 0.8997 | 1.4138 |
| 303.15 | 1.0000 | 1.4151 |
| 308.15 | 0.0000 | 1.393 |
| 308.15 | 0.1000 | 1.3958 |
| 308.15 | 0.2001 | 1.3983 |
| 308.15 | 0.3000 | 1.4007 |
| 308.15 | 0.3999 | 1.4029 |
| 308.15 | 0.5000 | 1.4049 |
| 308.15 | 0.6001 | 1.4068 |
| 308.15 | 0.6998 | 1.4085 |
| 308.15 | 0.7999 | 1.4101 |
| 308.15 | 0.8997 | 1.4116 |
| 308.15 | 1.0000 | 1.4129 |
| 313.15 | 0.0000 | 1.391 |
| 313.15 | 0.1000 | 1.3936 |
| 313.15 | 0.2001 | 1.3962 |
| 313.15 | 0.3000 | 1.3985 |
| 313.15 | 0.3999 | 1.4007 |
| 313.15 | 0.5000 | 1.4027 |
| 313.15 | 0.6001 | 1.4046 |
| 313.15 | 0.6998 | 1.4063 |
| 313.15 | 0.7999 | 1.4079 |
| 313.15 | 0.8997 | 1.4094 |
| 313.15 | 1.0000 | 1.4108 |
| 318.15 | 0.0000 | 1.3889 |
| 318.15 | 0.1000 | 1.3915 |
| 318.15 | 0.2001 | 1.394 |
| 318.15 | 0.3000 | 1.3963 |
| 318.15 | 0.3999 | 1.3985 |
| 318.15 | 0.5000 | 1.4005 |
| 318.15 | 0.6001 | 1.4024 |
| 318.15 | 0.6998 | 1.4041 |
| 318.15 | 0.7999 | 1.4058 |
| 318.15 | 0.8997 | 1.4073 |
| 318.15 | 1.0000 | 1.4088 |
| 323.15 | 0.0000 | 1.3867 |
| 323.15 | 0.1000 | 1.3894 |
| 323.15 | 0.2001 | 1.3918 |
| 323.15 | 0.3000 | 1.3942 |
| 323.15 | 0.3999 | 1.3963 |
| 323.15 | 0.5000 | 1.3983 |
| 323.15 | 0.6001 | 1.4002 |
| 323.15 | 0.6998 | 1.402 |
| 323.15 | 0.7999 | 1.4036 |
| 323.15 | 0.8997 | 1.4052 |
| 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 | 813.46 |
| 288.15 | 0.1000 | 851.32 |
| 288.15 | 0.2001 | 884.48 |
| 288.15 | 0.3000 | 913.45 |
| 288.15 | 0.3999 | 938.87 |
| 288.15 | 0.5000 | 961.37 |
| 288.15 | 0.6001 | 981.44 |
| 288.15 | 0.6998 | 999.46 |
| 288.15 | 0.7999 | 1015.94 |
| 288.15 | 0.8997 | 1031.0 |
| 288.15 | 1.0000 | 1044.83 |
| 293.15 | 0.0000 | 809.66 |
| 293.15 | 0.1000 | 847.26 |
| 293.15 | 0.2001 | 880.14 |
| 293.15 | 0.3000 | 908.86 |
| 293.15 | 0.3999 | 934.12 |
| 293.15 | 0.5000 | 956.51 |
| 293.15 | 0.6001 | 976.5 |
| 293.15 | 0.6998 | 994.45 |
| 293.15 | 0.7999 | 1010.87 |
| 293.15 | 0.8997 | 1025.85 |
| 293.15 | 1.0000 | 1039.63 |
| 298.15 | 0.0000 | 805.84 |
| 298.15 | 0.1000 | 843.14 |
| 298.15 | 0.2001 | 875.78 |
| 298.15 | 0.3000 | 904.32 |
| 298.15 | 0.3999 | 929.42 |
| 298.15 | 0.5000 | 951.69 |
| 298.15 | 0.6001 | 971.57 |
| 298.15 | 0.6998 | 989.44 |
| 298.15 | 0.7999 | 1005.79 |
| 298.15 | 0.8997 | 1020.71 |
| 298.15 | 1.0000 | 1034.44 |
| 303.15 | 0.0000 | 801.99 |
| 303.15 | 0.1000 | 838.99 |
| 303.15 | 0.2001 | 871.41 |
| 303.15 | 0.3000 | 899.78 |
| 303.15 | 0.3999 | 924.74 |
| 303.15 | 0.5000 | 946.87 |
| 303.15 | 0.6001 | 966.65 |
| 303.15 | 0.6998 | 984.43 |
| 303.15 | 0.7999 | 1000.71 |
| 303.15 | 0.8997 | 1015.58 |
| 303.15 | 1.0000 | 1029.25 |
| 308.15 | 0.0000 | 798.12 |
| 308.15 | 0.1000 | 834.83 |
| 308.15 | 0.2001 | 867.03 |
| 308.15 | 0.3000 | 895.21 |
| 308.15 | 0.3999 | 920.02 |
| 308.15 | 0.5000 | 942.04 |
| 308.15 | 0.6001 | 961.72 |
| 308.15 | 0.6998 | 979.42 |
| 308.15 | 0.7999 | 995.63 |
| 308.15 | 0.8997 | 1010.45 |
| 308.15 | 1.0000 | 1024.08 |
| 313.15 | 0.0000 | 794.22 |
| 313.15 | 0.1000 | 830.64 |
| 313.15 | 0.2001 | 862.62 |
| 313.15 | 0.3000 | 890.63 |
| 313.15 | 0.3999 | 915.3 |
| 313.15 | 0.5000 | 937.2 |
| 313.15 | 0.6001 | 956.78 |
| 313.15 | 0.6998 | 974.41 |
| 313.15 | 0.7999 | 990.55 |
| 313.15 | 0.8997 | 1005.31 |
| 313.15 | 1.0000 | 1018.9 |
| 318.15 | 0.0000 | 790.28 |
| 318.15 | 0.1000 | 826.42 |
| 318.15 | 0.2001 | 858.18 |
| 318.15 | 0.3000 | 886.02 |
| 318.15 | 0.3999 | 910.54 |
| 318.15 | 0.5000 | 932.33 |
| 318.15 | 0.6001 | 951.83 |
| 318.15 | 0.6998 | 969.38 |
| 318.15 | 0.7999 | 985.47 |
| 318.15 | 0.8997 | 1000.18 |
| 318.15 | 1.0000 | 1013.72 |
| 323.15 | 0.0000 | 786.29 |
| 323.15 | 0.1000 | 822.17 |
| 323.15 | 0.2001 | 853.72 |
| 323.15 | 0.3000 | 881.38 |
| 323.15 | 0.3999 | 905.78 |
| 323.15 | 0.5000 | 927.46 |
| 323.15 | 0.6001 | 946.87 |
| 323.15 | 0.6998 | 964.35 |
| 323.15 | 0.7999 | 980.38 |
| 323.15 | 0.8997 | 995.05 |
| 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 | 813.46 |
| 288.15 | 0.1000 | 851.32 |
| 288.15 | 0.2001 | 884.48 |
| 288.15 | 0.3000 | 913.45 |
| 288.15 | 0.3999 | 938.87 |
| 288.15 | 0.5000 | 961.37 |
| 288.15 | 0.6001 | 981.44 |
| 288.15 | 0.6998 | 999.46 |
| 288.15 | 0.7999 | 1015.94 |
| 288.15 | 0.8997 | 1031.0 |
| 288.15 | 1.0000 | 1044.83 |
| 293.15 | 0.0000 | 809.66 |
| 293.15 | 0.1000 | 847.26 |
| 293.15 | 0.2001 | 880.14 |
| 293.15 | 0.3000 | 908.86 |
| 293.15 | 0.3999 | 934.12 |
| 293.15 | 0.5000 | 956.51 |
| 293.15 | 0.6001 | 976.5 |
| 293.15 | 0.6998 | 994.45 |
| 293.15 | 0.7999 | 1010.87 |
| 293.15 | 0.8997 | 1025.85 |
| 293.15 | 1.0000 | 1039.63 |
| 298.15 | 0.0000 | 805.84 |
| 298.15 | 0.1000 | 843.14 |
| 298.15 | 0.2001 | 875.78 |
| 298.15 | 0.3000 | 904.32 |
| 298.15 | 0.3999 | 929.42 |
| 298.15 | 0.5000 | 951.69 |
| 298.15 | 0.6001 | 971.57 |
| 298.15 | 0.6998 | 989.44 |
| 298.15 | 0.7999 | 1005.79 |
| 298.15 | 0.8997 | 1020.71 |
| 298.15 | 1.0000 | 1034.44 |
| 303.15 | 0.0000 | 801.99 |
| 303.15 | 0.1000 | 838.99 |
| 303.15 | 0.2001 | 871.41 |
| 303.15 | 0.3000 | 899.78 |
| 303.15 | 0.3999 | 924.74 |
| 303.15 | 0.5000 | 946.87 |
| 303.15 | 0.6001 | 966.65 |
| 303.15 | 0.6998 | 984.43 |
| 303.15 | 0.7999 | 1000.71 |
| 303.15 | 0.8997 | 1015.58 |
| 303.15 | 1.0000 | 1029.25 |
| 308.15 | 0.0000 | 798.12 |
| 308.15 | 0.1000 | 834.83 |
| 308.15 | 0.2001 | 867.03 |
| 308.15 | 0.3000 | 895.21 |
| 308.15 | 0.3999 | 920.02 |
| 308.15 | 0.5000 | 942.04 |
| 308.15 | 0.6001 | 961.72 |
| 308.15 | 0.6998 | 979.42 |
| 308.15 | 0.7999 | 995.63 |
| 308.15 | 0.8997 | 1010.45 |
| 308.15 | 1.0000 | 1024.08 |
| 313.15 | 0.0000 | 794.22 |
| 313.15 | 0.1000 | 830.64 |
| 313.15 | 0.2001 | 862.62 |
| 313.15 | 0.3000 | 890.63 |
| 313.15 | 0.3999 | 915.3 |
| 313.15 | 0.5000 | 937.2 |
| 313.15 | 0.6001 | 956.78 |
| 313.15 | 0.6998 | 974.41 |
| 313.15 | 0.7999 | 990.55 |
| 313.15 | 0.8997 | 1005.31 |
| 313.15 | 1.0000 | 1018.9 |
| 318.15 | 0.0000 | 790.28 |
| 318.15 | 0.1000 | 826.42 |
| 318.15 | 0.2001 | 858.18 |
| 318.15 | 0.3000 | 886.02 |
| 318.15 | 0.3999 | 910.54 |
| 318.15 | 0.5000 | 932.33 |
| 318.15 | 0.6001 | 951.83 |
| 318.15 | 0.6998 | 969.38 |
| 318.15 | 0.7999 | 985.47 |
| 318.15 | 0.8997 | 1000.18 |
| 318.15 | 1.0000 | 1013.72 |
| 323.15 | 0.0000 | 786.29 |
| 323.15 | 0.1000 | 822.17 |
| 323.15 | 0.2001 | 853.72 |
| 323.15 | 0.3000 | 881.38 |
| 323.15 | 0.3999 | 905.78 |
| 323.15 | 0.5000 | 927.46 |
| 323.15 | 0.6001 | 946.87 |
| 323.15 | 0.6998 | 964.35 |
| 323.15 | 0.7999 | 980.38 |
| 323.15 | 0.8997 | 995.05 |
| 323.15 | 1.0000 | 1008.55 |