- Name
- 1-Butanol
- InChI
- InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
- InChI Key
- LRHPLDYGYMQRHN-UHFFFAOYSA-N
- Formula
- C4H10O
- SMILES
- CCCCO
- Mol. Weight (g/mol)
- 74.12
- CAS
- 71-36-3
- Name
- Hexanedioic acid, dimethyl ester
- InChI
- InChI=1S/C8H14O4/c1-11-7(9)5-3-4-6-8(10)12-2/h3-6H2,1-2H3
- InChI Key
- UDSFAEKRVUSQDD-UHFFFAOYSA-N
- Formula
- C8H14O4
- SMILES
- COC(=O)CCCCC(=O)OC
- Mol. Weight (g/mol)
- 174.19
- CAS
- 627-93-0
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Datasets
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Hexanedioic acid, dimethyl ester (2) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0034 |
| 288.15 | 0.0999 | 0.0026 |
| 288.15 | 0.2004 | 0.0024 |
| 288.15 | 0.2999 | 0.0024 |
| 288.15 | 0.4003 | 0.0024 |
| 288.15 | 0.4999 | 0.0025 |
| 288.15 | 0.6007 | 0.0027 |
| 288.15 | 0.6996 | 0.0029 |
| 288.15 | 0.7994 | 0.0031 |
| 288.15 | 0.8991 | 0.0034 |
| 288.15 | 1.0000 | 0.0038 |
| 293.15 | 0.0000 | 0.0029 |
| 293.15 | 0.0999 | 0.0023 |
| 293.15 | 0.2004 | 0.0021 |
| 293.15 | 0.2999 | 0.0021 |
| 293.15 | 0.4003 | 0.0021 |
| 293.15 | 0.4999 | 0.0022 |
| 293.15 | 0.6007 | 0.0024 |
| 293.15 | 0.6996 | 0.0026 |
| 293.15 | 0.7994 | 0.0027 |
| 293.15 | 0.8991 | 0.0030 |
| 293.15 | 1.0000 | 0.0033 |
| 298.15 | 0.0000 | 0.0026 |
| 298.15 | 0.0999 | 0.0021 |
| 298.15 | 0.2004 | 0.0019 |
| 298.15 | 0.2999 | 0.0019 |
| 298.15 | 0.4003 | 0.0019 |
| 298.15 | 0.4999 | 0.0020 |
| 298.15 | 0.6007 | 0.0021 |
| 298.15 | 0.6996 | 0.0023 |
| 298.15 | 0.7994 | 0.0024 |
| 298.15 | 0.8991 | 0.0026 |
| 298.15 | 1.0000 | 0.0029 |
| 303.15 | 0.0000 | 0.0023 |
| 303.15 | 0.0999 | 0.0018 |
| 303.15 | 0.2004 | 0.0017 |
| 303.15 | 0.2999 | 0.0017 |
| 303.15 | 0.4003 | 0.0017 |
| 303.15 | 0.4999 | 0.0018 |
| 303.15 | 0.6007 | 0.0019 |
| 303.15 | 0.6996 | 0.0021 |
| 303.15 | 0.7994 | 0.0022 |
| 303.15 | 0.8991 | 0.0024 |
| 303.15 | 1.0000 | 0.0026 |
| 308.15 | 0.0000 | 0.0020 |
| 308.15 | 0.0999 | 0.0016 |
| 308.15 | 0.2004 | 0.0015 |
| 308.15 | 0.2999 | 0.0015 |
| 308.15 | 0.4003 | 0.0016 |
| 308.15 | 0.4999 | 0.0016 |
| 308.15 | 0.6007 | 0.0017 |
| 308.15 | 0.6996 | 0.0019 |
| 308.15 | 0.7994 | 0.0020 |
| 308.15 | 0.8991 | 0.0021 |
| 308.15 | 1.0000 | 0.0023 |
| 313.15 | 0.0000 | 0.0018 |
| 313.15 | 0.0999 | 0.0015 |
| 313.15 | 0.2004 | 0.0014 |
| 313.15 | 0.2999 | 0.0014 |
| 313.15 | 0.4003 | 0.0014 |
| 313.15 | 0.4999 | 0.0015 |
| 313.15 | 0.6007 | 0.0016 |
| 313.15 | 0.6996 | 0.0017 |
| 313.15 | 0.7994 | 0.0018 |
| 313.15 | 0.8991 | 0.0019 |
| 313.15 | 1.0000 | 0.0021 |
| 318.15 | 0.0000 | 0.0016 |
| 318.15 | 0.0999 | 0.0013 |
| 318.15 | 0.2004 | 0.0013 |
| 318.15 | 0.2999 | 0.0013 |
| 318.15 | 0.4003 | 0.0013 |
| 318.15 | 0.4999 | 0.0014 |
| 318.15 | 0.6007 | 0.0014 |
| 318.15 | 0.6996 | 0.0016 |
| 318.15 | 0.7994 | 0.0016 |
| 318.15 | 0.8991 | 0.0018 |
| 318.15 | 1.0000 | 0.0019 |
| 323.15 | 0.0000 | 0.0014 |
| 323.15 | 0.0999 | 0.0012 |
| 323.15 | 0.2004 | 0.0012 |
| 323.15 | 0.2999 | 0.0012 |
| 323.15 | 0.4003 | 0.0012 |
| 323.15 | 0.4999 | 0.0013 |
| 323.15 | 0.6007 | 0.0013 |
| 323.15 | 0.6996 | 0.0015 |
| 323.15 | 0.7994 | 0.0015 |
| 323.15 | 0.8991 | 0.0016 |
| 323.15 | 1.0000 | 0.0018 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Hexanedioic acid, dimethyl ester (2) - Liquid | Viscosity, Pa*s - Liquid |
| 288.15 | 0.0000 | 0.0034 |
| 288.15 | 0.0999 | 0.0026 |
| 288.15 | 0.2004 | 0.0024 |
| 288.15 | 0.2999 | 0.0024 |
| 288.15 | 0.4003 | 0.0024 |
| 288.15 | 0.4999 | 0.0025 |
| 288.15 | 0.6007 | 0.0027 |
| 288.15 | 0.6996 | 0.0029 |
| 288.15 | 0.7994 | 0.0031 |
| 288.15 | 0.8991 | 0.0034 |
| 288.15 | 1.0000 | 0.0038 |
| 293.15 | 0.0000 | 0.0029 |
| 293.15 | 0.0999 | 0.0023 |
| 293.15 | 0.2004 | 0.0021 |
| 293.15 | 0.2999 | 0.0021 |
| 293.15 | 0.4003 | 0.0021 |
| 293.15 | 0.4999 | 0.0022 |
| 293.15 | 0.6007 | 0.0024 |
| 293.15 | 0.6996 | 0.0026 |
| 293.15 | 0.7994 | 0.0027 |
| 293.15 | 0.8991 | 0.0030 |
| 293.15 | 1.0000 | 0.0033 |
| 298.15 | 0.0000 | 0.0026 |
| 298.15 | 0.0999 | 0.0021 |
| 298.15 | 0.2004 | 0.0019 |
| 298.15 | 0.2999 | 0.0019 |
| 298.15 | 0.4003 | 0.0019 |
| 298.15 | 0.4999 | 0.0020 |
| 298.15 | 0.6007 | 0.0021 |
| 298.15 | 0.6996 | 0.0023 |
| 298.15 | 0.7994 | 0.0024 |
| 298.15 | 0.8991 | 0.0026 |
| 298.15 | 1.0000 | 0.0029 |
| 303.15 | 0.0000 | 0.0023 |
| 303.15 | 0.0999 | 0.0018 |
| 303.15 | 0.2004 | 0.0017 |
| 303.15 | 0.2999 | 0.0017 |
| 303.15 | 0.4003 | 0.0017 |
| 303.15 | 0.4999 | 0.0018 |
| 303.15 | 0.6007 | 0.0019 |
| 303.15 | 0.6996 | 0.0021 |
| 303.15 | 0.7994 | 0.0022 |
| 303.15 | 0.8991 | 0.0024 |
| 303.15 | 1.0000 | 0.0026 |
| 308.15 | 0.0000 | 0.0020 |
| 308.15 | 0.0999 | 0.0016 |
| 308.15 | 0.2004 | 0.0015 |
| 308.15 | 0.2999 | 0.0015 |
| 308.15 | 0.4003 | 0.0016 |
| 308.15 | 0.4999 | 0.0016 |
| 308.15 | 0.6007 | 0.0017 |
| 308.15 | 0.6996 | 0.0019 |
| 308.15 | 0.7994 | 0.0020 |
| 308.15 | 0.8991 | 0.0021 |
| 308.15 | 1.0000 | 0.0023 |
| 313.15 | 0.0000 | 0.0018 |
| 313.15 | 0.0999 | 0.0015 |
| 313.15 | 0.2004 | 0.0014 |
| 313.15 | 0.2999 | 0.0014 |
| 313.15 | 0.4003 | 0.0014 |
| 313.15 | 0.4999 | 0.0015 |
| 313.15 | 0.6007 | 0.0016 |
| 313.15 | 0.6996 | 0.0017 |
| 313.15 | 0.7994 | 0.0018 |
| 313.15 | 0.8991 | 0.0019 |
| 313.15 | 1.0000 | 0.0021 |
| 318.15 | 0.0000 | 0.0016 |
| 318.15 | 0.0999 | 0.0013 |
| 318.15 | 0.2004 | 0.0013 |
| 318.15 | 0.2999 | 0.0013 |
| 318.15 | 0.4003 | 0.0013 |
| 318.15 | 0.4999 | 0.0014 |
| 318.15 | 0.6007 | 0.0014 |
| 318.15 | 0.6996 | 0.0016 |
| 318.15 | 0.7994 | 0.0016 |
| 318.15 | 0.8991 | 0.0018 |
| 318.15 | 1.0000 | 0.0019 |
| 323.15 | 0.0000 | 0.0014 |
| 323.15 | 0.0999 | 0.0012 |
| 323.15 | 0.2004 | 0.0012 |
| 323.15 | 0.2999 | 0.0012 |
| 323.15 | 0.4003 | 0.0012 |
| 323.15 | 0.4999 | 0.0013 |
| 323.15 | 0.6007 | 0.0013 |
| 323.15 | 0.6996 | 0.0015 |
| 323.15 | 0.7994 | 0.0015 |
| 323.15 | 0.8991 | 0.0016 |
| 323.15 | 1.0000 | 0.0018 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Hexanedioic acid, dimethyl ester (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.4014 |
| 288.15 | 0.0999 | 1.4058 |
| 288.15 | 0.2004 | 1.4099 |
| 288.15 | 0.2999 | 1.4134 |
| 288.15 | 0.4003 | 1.4167 |
| 288.15 | 0.4999 | 1.4197 |
| 288.15 | 0.6007 | 1.4222 |
| 288.15 | 0.6996 | 1.4245 |
| 288.15 | 0.7994 | 1.4267 |
| 288.15 | 0.8991 | 1.4287 |
| 288.15 | 1.0000 | 1.4305 |
| 293.15 | 0.0000 | 1.3993 |
| 293.15 | 0.0999 | 1.4038 |
| 293.15 | 0.2004 | 1.4078 |
| 293.15 | 0.2999 | 1.4114 |
| 293.15 | 0.4003 | 1.4146 |
| 293.15 | 0.4999 | 1.4175 |
| 293.15 | 0.6007 | 1.4201 |
| 293.15 | 0.6996 | 1.4224 |
| 293.15 | 0.7994 | 1.4246 |
| 293.15 | 0.8991 | 1.4266 |
| 293.15 | 1.0000 | 1.4284 |
| 298.15 | 0.0000 | 1.3973 |
| 298.15 | 0.0999 | 1.4017 |
| 298.15 | 0.2004 | 1.4057 |
| 298.15 | 0.2999 | 1.4092 |
| 298.15 | 0.4003 | 1.4125 |
| 298.15 | 0.4999 | 1.4154 |
| 298.15 | 0.6007 | 1.418 |
| 298.15 | 0.6996 | 1.4203 |
| 298.15 | 0.7994 | 1.4225 |
| 298.15 | 0.8991 | 1.4245 |
| 298.15 | 1.0000 | 1.4264 |
| 303.15 | 0.0000 | 1.3952 |
| 303.15 | 0.0999 | 1.3996 |
| 303.15 | 0.2004 | 1.4036 |
| 303.15 | 0.2999 | 1.4071 |
| 303.15 | 0.4003 | 1.4103 |
| 303.15 | 0.4999 | 1.4133 |
| 303.15 | 0.6007 | 1.4159 |
| 303.15 | 0.6996 | 1.4182 |
| 303.15 | 0.7994 | 1.4204 |
| 303.15 | 0.8991 | 1.4224 |
| 303.15 | 1.0000 | 1.4243 |
| 308.15 | 0.0000 | 1.3932 |
| 308.15 | 0.0999 | 1.3975 |
| 308.15 | 0.2004 | 1.4014 |
| 308.15 | 0.2999 | 1.405 |
| 308.15 | 0.4003 | 1.4082 |
| 308.15 | 0.4999 | 1.4111 |
| 308.15 | 0.6007 | 1.4138 |
| 308.15 | 0.6996 | 1.4161 |
| 308.15 | 0.7994 | 1.4183 |
| 308.15 | 0.8991 | 1.4204 |
| 308.15 | 1.0000 | 1.4222 |
| 313.15 | 0.0000 | 1.3911 |
| 313.15 | 0.0999 | 1.3953 |
| 313.15 | 0.2004 | 1.3993 |
| 313.15 | 0.2999 | 1.4028 |
| 313.15 | 0.4003 | 1.406 |
| 313.15 | 0.4999 | 1.409 |
| 313.15 | 0.6007 | 1.4116 |
| 313.15 | 0.6996 | 1.414 |
| 313.15 | 0.7994 | 1.4162 |
| 313.15 | 0.8991 | 1.4183 |
| 313.15 | 1.0000 | 1.4202 |
| 318.15 | 0.0000 | 1.389 |
| 318.15 | 0.0999 | 1.3932 |
| 318.15 | 0.2004 | 1.3972 |
| 318.15 | 0.2999 | 1.4007 |
| 318.15 | 0.4003 | 1.4039 |
| 318.15 | 0.4999 | 1.4069 |
| 318.15 | 0.6007 | 1.4095 |
| 318.15 | 0.6996 | 1.4119 |
| 318.15 | 0.7994 | 1.4142 |
| 318.15 | 0.8991 | 1.4162 |
| 318.15 | 1.0000 | 1.4182 |
| 323.15 | 0.0000 | 1.3869 |
| 323.15 | 0.0999 | 1.3911 |
| 323.15 | 0.2004 | 1.395 |
| 323.15 | 0.2999 | 1.3986 |
| 323.15 | 0.4003 | 1.4018 |
| 323.15 | 0.4999 | 1.4047 |
| 323.15 | 0.6007 | 1.4074 |
| 323.15 | 0.6996 | 1.4098 |
| 323.15 | 0.7994 | 1.4121 |
| 323.15 | 0.8991 | 1.4142 |
| 323.15 | 1.0000 | 1.4161 |
Refractive index (Na D-line) [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Hexanedioic acid, dimethyl ester (2) - Liquid | Refractive index (Na D-line) - Liquid |
| 288.15 | 0.0000 | 1.4014 |
| 288.15 | 0.0999 | 1.4058 |
| 288.15 | 0.2004 | 1.4099 |
| 288.15 | 0.2999 | 1.4134 |
| 288.15 | 0.4003 | 1.4167 |
| 288.15 | 0.4999 | 1.4197 |
| 288.15 | 0.6007 | 1.4222 |
| 288.15 | 0.6996 | 1.4245 |
| 288.15 | 0.7994 | 1.4267 |
| 288.15 | 0.8991 | 1.4287 |
| 288.15 | 1.0000 | 1.4305 |
| 293.15 | 0.0000 | 1.3993 |
| 293.15 | 0.0999 | 1.4038 |
| 293.15 | 0.2004 | 1.4078 |
| 293.15 | 0.2999 | 1.4114 |
| 293.15 | 0.4003 | 1.4146 |
| 293.15 | 0.4999 | 1.4175 |
| 293.15 | 0.6007 | 1.4201 |
| 293.15 | 0.6996 | 1.4224 |
| 293.15 | 0.7994 | 1.4246 |
| 293.15 | 0.8991 | 1.4266 |
| 293.15 | 1.0000 | 1.4284 |
| 298.15 | 0.0000 | 1.3973 |
| 298.15 | 0.0999 | 1.4017 |
| 298.15 | 0.2004 | 1.4057 |
| 298.15 | 0.2999 | 1.4092 |
| 298.15 | 0.4003 | 1.4125 |
| 298.15 | 0.4999 | 1.4154 |
| 298.15 | 0.6007 | 1.418 |
| 298.15 | 0.6996 | 1.4203 |
| 298.15 | 0.7994 | 1.4225 |
| 298.15 | 0.8991 | 1.4245 |
| 298.15 | 1.0000 | 1.4264 |
| 303.15 | 0.0000 | 1.3952 |
| 303.15 | 0.0999 | 1.3996 |
| 303.15 | 0.2004 | 1.4036 |
| 303.15 | 0.2999 | 1.4071 |
| 303.15 | 0.4003 | 1.4103 |
| 303.15 | 0.4999 | 1.4133 |
| 303.15 | 0.6007 | 1.4159 |
| 303.15 | 0.6996 | 1.4182 |
| 303.15 | 0.7994 | 1.4204 |
| 303.15 | 0.8991 | 1.4224 |
| 303.15 | 1.0000 | 1.4243 |
| 308.15 | 0.0000 | 1.3932 |
| 308.15 | 0.0999 | 1.3975 |
| 308.15 | 0.2004 | 1.4014 |
| 308.15 | 0.2999 | 1.405 |
| 308.15 | 0.4003 | 1.4082 |
| 308.15 | 0.4999 | 1.4111 |
| 308.15 | 0.6007 | 1.4138 |
| 308.15 | 0.6996 | 1.4161 |
| 308.15 | 0.7994 | 1.4183 |
| 308.15 | 0.8991 | 1.4204 |
| 308.15 | 1.0000 | 1.4222 |
| 313.15 | 0.0000 | 1.3911 |
| 313.15 | 0.0999 | 1.3953 |
| 313.15 | 0.2004 | 1.3993 |
| 313.15 | 0.2999 | 1.4028 |
| 313.15 | 0.4003 | 1.406 |
| 313.15 | 0.4999 | 1.409 |
| 313.15 | 0.6007 | 1.4116 |
| 313.15 | 0.6996 | 1.414 |
| 313.15 | 0.7994 | 1.4162 |
| 313.15 | 0.8991 | 1.4183 |
| 313.15 | 1.0000 | 1.4202 |
| 318.15 | 0.0000 | 1.389 |
| 318.15 | 0.0999 | 1.3932 |
| 318.15 | 0.2004 | 1.3972 |
| 318.15 | 0.2999 | 1.4007 |
| 318.15 | 0.4003 | 1.4039 |
| 318.15 | 0.4999 | 1.4069 |
| 318.15 | 0.6007 | 1.4095 |
| 318.15 | 0.6996 | 1.4119 |
| 318.15 | 0.7994 | 1.4142 |
| 318.15 | 0.8991 | 1.4162 |
| 318.15 | 1.0000 | 1.4182 |
| 323.15 | 0.0000 | 1.3869 |
| 323.15 | 0.0999 | 1.3911 |
| 323.15 | 0.2004 | 1.395 |
| 323.15 | 0.2999 | 1.3986 |
| 323.15 | 0.4003 | 1.4018 |
| 323.15 | 0.4999 | 1.4047 |
| 323.15 | 0.6007 | 1.4074 |
| 323.15 | 0.6996 | 1.4098 |
| 323.15 | 0.7994 | 1.4121 |
| 323.15 | 0.8991 | 1.4142 |
| 323.15 | 1.0000 | 1.4161 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Hexanedioic acid, dimethyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 813.373 |
| 288.15 | 0.0999 | 854.546 |
| 288.15 | 0.2004 | 890.617 |
| 288.15 | 0.2999 | 921.957 |
| 288.15 | 0.4003 | 949.859 |
| 288.15 | 0.4999 | 974.548 |
| 288.15 | 0.6007 | 996.907 |
| 288.15 | 0.6996 | 1016.647 |
| 288.15 | 0.7994 | 1034.835 |
| 288.15 | 0.8991 | 1051.421 |
| 288.15 | 1.0000 | 1066.794 |
| 293.15 | 0.0000 | 809.573 |
| 293.15 | 0.0999 | 850.5 |
| 293.15 | 0.2004 | 886.373 |
| 293.15 | 0.2999 | 917.562 |
| 293.15 | 0.4003 | 945.34 |
| 293.15 | 0.4999 | 969.9 |
| 293.15 | 0.6007 | 992.211 |
| 293.15 | 0.6996 | 1011.892 |
| 293.15 | 0.7994 | 1030.032 |
| 293.15 | 0.8991 | 1046.58 |
| 293.15 | 1.0000 | 1061.928 |
| 298.15 | 0.0000 | 805.762 |
| 298.15 | 0.0999 | 846.433 |
| 298.15 | 0.2004 | 882.112 |
| 298.15 | 0.2999 | 913.148 |
| 298.15 | 0.4003 | 940.805 |
| 298.15 | 0.4999 | 965.3 |
| 298.15 | 0.6007 | 987.507 |
| 298.15 | 0.6996 | 1007.127 |
| 298.15 | 0.7994 | 1025.222 |
| 298.15 | 0.8991 | 1041.739 |
| 298.15 | 1.0000 | 1057.056 |
| 303.15 | 0.0000 | 801.923 |
| 303.15 | 0.0999 | 842.341 |
| 303.15 | 0.2004 | 877.825 |
| 303.15 | 0.2999 | 908.714 |
| 303.15 | 0.4003 | 936.253 |
| 303.15 | 0.4999 | 960.66 |
| 303.15 | 0.6007 | 982.791 |
| 303.15 | 0.6996 | 1002.355 |
| 303.15 | 0.7994 | 1020.409 |
| 303.15 | 0.8991 | 1036.892 |
| 303.15 | 1.0000 | 1052.185 |
| 308.15 | 0.0000 | 798.053 |
| 308.15 | 0.0999 | 838.219 |
| 308.15 | 0.2004 | 873.513 |
| 308.15 | 0.2999 | 904.259 |
| 308.15 | 0.4003 | 931.684 |
| 308.15 | 0.4999 | 955.998 |
| 308.15 | 0.6007 | 978.06 |
| 308.15 | 0.6996 | 997.573 |
| 308.15 | 0.7994 | 1015.587 |
| 308.15 | 0.8991 | 1032.04 |
| 308.15 | 1.0000 | 1047.308 |
| 313.15 | 0.0000 | 794.147 |
| 313.15 | 0.0999 | 834.066 |
| 313.15 | 0.2004 | 869.172 |
| 313.15 | 0.2999 | 899.775 |
| 313.15 | 0.4003 | 927.091 |
| 313.15 | 0.4999 | 951.32 |
| 313.15 | 0.6007 | 973.316 |
| 313.15 | 0.6996 | 992.781 |
| 313.15 | 0.7994 | 1010.757 |
| 313.15 | 0.8991 | 1027.183 |
| 313.15 | 1.0000 | 1042.427 |
| 318.15 | 0.0000 | 790.231 |
| 318.15 | 0.0999 | 829.874 |
| 318.15 | 0.2004 | 864.799 |
| 318.15 | 0.2999 | 895.264 |
| 318.15 | 0.4003 | 922.473 |
| 318.15 | 0.4999 | 946.622 |
| 318.15 | 0.6007 | 968.555 |
| 318.15 | 0.6996 | 987.974 |
| 318.15 | 0.7994 | 1005.915 |
| 318.15 | 0.8991 | 1022.314 |
| 318.15 | 1.0000 | 1037.539 |
| 323.15 | 0.0000 | 786.238 |
| 323.15 | 0.0999 | 825.64 |
| 323.15 | 0.2004 | 860.391 |
| 323.15 | 0.2999 | 890.725 |
| 323.15 | 0.4003 | 917.832 |
| 323.15 | 0.4999 | 941.902 |
| 323.15 | 0.6007 | 963.778 |
| 323.15 | 0.6996 | 983.155 |
| 323.15 | 0.7994 | 1001.064 |
| 323.15 | 0.8991 | 1017.438 |
| 323.15 | 1.0000 | 1032.645 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Hexanedioic acid, dimethyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 813.373 |
| 288.15 | 0.0999 | 854.546 |
| 288.15 | 0.2004 | 890.617 |
| 288.15 | 0.2999 | 921.957 |
| 288.15 | 0.4003 | 949.859 |
| 288.15 | 0.4999 | 974.548 |
| 288.15 | 0.6007 | 996.907 |
| 288.15 | 0.6996 | 1016.647 |
| 288.15 | 0.7994 | 1034.835 |
| 288.15 | 0.8991 | 1051.421 |
| 288.15 | 1.0000 | 1066.794 |
| 293.15 | 0.0000 | 809.573 |
| 293.15 | 0.0999 | 850.5 |
| 293.15 | 0.2004 | 886.373 |
| 293.15 | 0.2999 | 917.562 |
| 293.15 | 0.4003 | 945.34 |
| 293.15 | 0.4999 | 969.9 |
| 293.15 | 0.6007 | 992.211 |
| 293.15 | 0.6996 | 1011.892 |
| 293.15 | 0.7994 | 1030.032 |
| 293.15 | 0.8991 | 1046.58 |
| 293.15 | 1.0000 | 1061.928 |
| 298.15 | 0.0000 | 805.762 |
| 298.15 | 0.0999 | 846.433 |
| 298.15 | 0.2004 | 882.112 |
| 298.15 | 0.2999 | 913.148 |
| 298.15 | 0.4003 | 940.805 |
| 298.15 | 0.4999 | 965.3 |
| 298.15 | 0.6007 | 987.507 |
| 298.15 | 0.6996 | 1007.127 |
| 298.15 | 0.7994 | 1025.222 |
| 298.15 | 0.8991 | 1041.739 |
| 298.15 | 1.0000 | 1057.056 |
| 303.15 | 0.0000 | 801.923 |
| 303.15 | 0.0999 | 842.341 |
| 303.15 | 0.2004 | 877.825 |
| 303.15 | 0.2999 | 908.714 |
| 303.15 | 0.4003 | 936.253 |
| 303.15 | 0.4999 | 960.66 |
| 303.15 | 0.6007 | 982.791 |
| 303.15 | 0.6996 | 1002.355 |
| 303.15 | 0.7994 | 1020.409 |
| 303.15 | 0.8991 | 1036.892 |
| 303.15 | 1.0000 | 1052.185 |
| 308.15 | 0.0000 | 798.053 |
| 308.15 | 0.0999 | 838.219 |
| 308.15 | 0.2004 | 873.513 |
| 308.15 | 0.2999 | 904.259 |
| 308.15 | 0.4003 | 931.684 |
| 308.15 | 0.4999 | 955.998 |
| 308.15 | 0.6007 | 978.06 |
| 308.15 | 0.6996 | 997.573 |
| 308.15 | 0.7994 | 1015.587 |
| 308.15 | 0.8991 | 1032.04 |
| 308.15 | 1.0000 | 1047.308 |
| 313.15 | 0.0000 | 794.147 |
| 313.15 | 0.0999 | 834.066 |
| 313.15 | 0.2004 | 869.172 |
| 313.15 | 0.2999 | 899.775 |
| 313.15 | 0.4003 | 927.091 |
| 313.15 | 0.4999 | 951.32 |
| 313.15 | 0.6007 | 973.316 |
| 313.15 | 0.6996 | 992.781 |
| 313.15 | 0.7994 | 1010.757 |
| 313.15 | 0.8991 | 1027.183 |
| 313.15 | 1.0000 | 1042.427 |
| 318.15 | 0.0000 | 790.231 |
| 318.15 | 0.0999 | 829.874 |
| 318.15 | 0.2004 | 864.799 |
| 318.15 | 0.2999 | 895.264 |
| 318.15 | 0.4003 | 922.473 |
| 318.15 | 0.4999 | 946.622 |
| 318.15 | 0.6007 | 968.555 |
| 318.15 | 0.6996 | 987.974 |
| 318.15 | 0.7994 | 1005.915 |
| 318.15 | 0.8991 | 1022.314 |
| 318.15 | 1.0000 | 1037.539 |
| 323.15 | 0.0000 | 786.238 |
| 323.15 | 0.0999 | 825.64 |
| 323.15 | 0.2004 | 860.391 |
| 323.15 | 0.2999 | 890.725 |
| 323.15 | 0.4003 | 917.832 |
| 323.15 | 0.4999 | 941.902 |
| 323.15 | 0.6007 | 963.778 |
| 323.15 | 0.6996 | 983.155 |
| 323.15 | 0.7994 | 1001.064 |
| 323.15 | 0.8991 | 1017.438 |
| 323.15 | 1.0000 | 1032.645 |
Sources
- Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
- Thermodynamic and Spectroscopic Study of the Ternary System Dimethyladipate + Tetrahydrofuran +1-Butanol at T = (288.15 to 323.15) K