- 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
- Molecular Weight1
- 174.19
- CAS
- 627-93-0
- Other Names
-
- 1,6-Dimethylhexanedioate
- 1,6-hexanedioic acid, dimethyl ester
- Adipic acid, dimethyl ester
- Dimethyl adipate
- Dimethyl ester of hexanedioic acid
- Dimethyl hexanedioate
- Hexanedioic acid, methyl ester
- Methyl adipate
- dimethyl 1,6-hexanedioate
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- D*i : Self diffusion coefficient (m2/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -4286.20 ± 3.20 | kJ/mol | NIST |
| ΔcH°solid | -4266.00 | kJ/mol | NIST |
| ΔfG° | -451.36 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -698.05 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -862.80 ± 3.20 | kJ/mol | NIST |
| ΔfusH° | 22.05 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [67.10; 73.40] | kJ/mol |
|
| ΔvapH° | 67.10 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 69.00 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 73.40 | kJ/mol | NIST |
| log10WS | -0.90 | Crippen Calculated Property | |
| logPoct/wat | 0.893 | Crippen Calculated Property | |
| McVol | 138.460 | ml/mol | McGowan Calculated Property |
| Pc | 2500.00 | kPa | Vapor P... |
| Inp | [210.93; 1256.00] |
|
|
| Inp | 1243.00 | NIST | |
| Inp | 1242.00 | NIST | |
| Inp | 1241.00 | NIST | |
| Inp | 1207.00 | NIST | |
| Inp | 1205.00 | NIST | |
| Inp | 1204.00 | NIST | |
| Inp | 1202.00 | NIST | |
| Inp | 1234.00 | NIST | |
| Inp | 1223.00 | NIST | |
| Inp | 1208.20 | NIST | |
| Inp | 1246.00 | NIST | |
| Inp | 1206.00 | NIST | |
| Inp | 1235.00 | NIST | |
| Inp | 1256.00 | NIST | |
| Inp | 1243.00 | NIST | |
| Inp | 1205.00 | NIST | |
| Inp | 1213.00 | NIST | |
| Inp | 1246.70 | NIST | |
| Inp | 1213.00 | NIST | |
| Inp | 1212.00 | NIST | |
| Inp | 1211.00 | NIST | |
| Inp | 1215.00 | NIST | |
| Inp | 1206.00 | NIST | |
| Inp | 1206.00 | NIST | |
| Inp | 1206.00 | NIST | |
| Inp | 1212.00 | NIST | |
| Inp | 1223.00 | NIST | |
| Inp | 1213.00 | NIST | |
| Inp | Outlier 211.70 | NIST | |
| Inp | Outlier 210.93 | NIST | |
| Inp | 1213.00 | NIST | |
| Inp | 1243.00 | NIST | |
| Inp | 1204.00 | NIST | |
| Inp | 1206.00 | NIST | |
| I | [1777.00; 1819.00] |
|
|
| I | 1777.00 | NIST | |
| I | 1809.00 | NIST | |
| I | 1817.00 | NIST | |
| I | 1819.00 | NIST | |
| I | 1804.00 | NIST | |
| I | 1779.00 | NIST | |
| I | 1817.00 | NIST | |
| I | 1779.00 | NIST | |
| Tboil | [498.20; 508.00] | K |
|
| Tboil | 498.20 | K | Liquid ... |
| Tboil | 508.00 ± 4.00 | K | NIST |
| Tc | 718.73 | K | Joback Calculated Property |
| Tfus | [283.50; 283.50] | K |
|
| Tfus | 283.50 ± 0.60 | K | NIST |
| Tfus | 283.50 ± 1.00 | K | NIST |
| Vc | 0.531 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [322.22; 384.50] | J/mol×K | [535.02; 718.73] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 320 330 340 350 360 370 380 390 550 600 650 700 | ||||
| Cp,gas | 322.22 | J/mol×K | 535.02 | Joback Calculated Property |
| Cp,gas | 333.68 | J/mol×K | 565.64 | Joback Calculated Property |
| Cp,gas | 344.72 | J/mol×K | 596.26 | Joback Calculated Property |
| Cp,gas | 355.33 | J/mol×K | 626.88 | Joback Calculated Property |
| Cp,gas | 365.50 | J/mol×K | 657.50 | Joback Calculated Property |
| Cp,gas | 375.23 | J/mol×K | 688.12 | Joback Calculated Property |
| Cp,gas | 384.50 | J/mol×K | 718.73 | Joback Calculated Property |
| η | [0.0009200; 0.0043900] | Pa×s | [283.15; 373.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 4.50e-3 300 320 340 360 | ||||
| η | 0.0043900 | Pa×s | 283.15 | Influen... |
| η | 0.0038200 | Pa×s | 288.15 | Influen... |
| η | 0.0033600 | Pa×s | 293.15 | Influen... |
| η | 0.0029800 | Pa×s | 298.15 | Influen... |
| η | 0.0026700 | Pa×s | 303.15 | Influen... |
| η | 0.0024000 | Pa×s | 308.15 | Influen... |
| η | 0.0021800 | Pa×s | 313.15 | Influen... |
| η | 0.0019900 | Pa×s | 318.15 | Influen... |
| η | 0.0018200 | Pa×s | 323.15 | Influen... |
| η | 0.0016800 | Pa×s | 328.15 | Influen... |
| η | 0.0015500 | Pa×s | 333.15 | Influen... |
| η | 0.0014400 | Pa×s | 338.15 | Influen... |
| η | 0.0013400 | Pa×s | 343.15 | Influen... |
| η | 0.0012500 | Pa×s | 348.15 | Influen... |
| η | 0.0011700 | Pa×s | 353.15 | Influen... |
| η | 0.0011000 | Pa×s | 358.15 | Influen... |
| η | 0.0010300 | Pa×s | 363.15 | Influen... |
| η | 0.0009700 | Pa×s | 368.15 | Influen... |
| η | 0.0009200 | Pa×s | 373.15 | Influen... |
| ΔvapH | [58.80; 74.60] | kJ/mol | [398.00; 441.00] |
|
| ΔvapH | 74.60 | kJ/mol | 398.00 | NIST |
| ΔvapH | 58.80 | kJ/mol | 441.00 | NIST |
| Pvap | [2.53e-03; 216.30] | kPa | [293.20; 531.44] |
|
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 400 500 | ||||
| Pvap | 2.53e-03 | kPa | 293.20 | Thermod... |
| Pvap | 3.36e-03 | kPa | 296.20 | Thermod... |
| Pvap | 4.43e-03 | kPa | 299.20 | Thermod... |
| Pvap | 5.86e-03 | kPa | 302.20 | Thermod... |
| Pvap | 7.40e-03 | kPa | 305.20 | Thermod... |
| Pvap | 9.91e-03 | kPa | 308.20 | Thermod... |
| Pvap | 0.01 | kPa | 310.20 | Thermod... |
| Pvap | 0.01 | kPa | 313.30 | Thermod... |
| Pvap | 0.02 | kPa | 316.20 | Thermod... |
| Pvap | 0.02 | kPa | 319.30 | Thermod... |
| Pvap | 0.03 | kPa | 322.20 | Thermod... |
| Pvap | 0.04 | kPa | 325.30 | Thermod... |
| Pvap | 0.05 | kPa | 328.20 | Thermod... |
| Pvap | 0.06 | kPa | 331.20 | Thermod... |
| Pvap | 0.07 | kPa | 334.20 | Thermod... |
| Pvap | 0.51 | kPa | 353.15 | Vapor-L... |
| Pvap | 1.26 | kPa | 373.15 | Vapor-L... |
| Pvap | 1.92 | kPa | 383.15 | Vapor-L... |
| Pvap | 2.00 | kPa | 390.98 | Isobari... |
| Pvap | 4.33 | kPa | 403.15 | Vapor-L... |
| Pvap | 5.20 | kPa | 410.82 | Isobari... |
| Pvap | 5.93 | kPa | 413.15 | Vapor-L... |
| Pvap | 8.30 | kPa | 422.47 | Isobari... |
| Pvap | 8.37 | kPa | 423.15 | Vapor-L... |
| Pvap | 7.79 | kPa | 424.91 | Isobari... |
| Pvap | 10.00 | kPa | 431.20 | Isobari... |
| Pvap | 12.30 | kPa | 433.15 | Vapor-L... |
| Pvap | 14.56 | kPa | 441.21 | Isobari... |
| Pvap | 16.66 | kPa | 443.15 | Vapor-L... |
| Pvap | 20.00 | kPa | 450.08 | Isobari... |
| Pvap | 28.55 | kPa | 460.47 | Isobari... |
| Pvap | 44.63 | kPa | 474.33 | Isobari... |
| Pvap | 54.37 | kPa | 480.72 | Isobari... |
| Pvap | 68.77 | kPa | 488.62 | Isobari... |
| Pvap | 85.45 | kPa | 496.14 | Isobari... |
| Pvap | 99.00 | kPa | 501.00 | Isobari... |
| Pvap | 108.77 | kPa | 504.86 | Isobari... |
| Pvap | 131.95 | kPa | 512.00 | Isobari... |
| Pvap | 157.68 | kPa | 518.78 | Isobari... |
| Pvap | 179.21 | kPa | 523.92 | Isobari... |
| Pvap | 216.30 | kPa | 531.44 | Isobari... |
| n0 | [1.41614; 1.43050] | [288.15; 323.15] |
|
|
|
T(K) Refractive Index 1.42 1.42 1.42 1.42 1.42 1.43 1.43 1.43 290 300 310 320 | ||||
| n0 | 1.43050 | 288.15 | Experim... | |
| n0 | 1.42825 | 293.15 | Phase e... | |
| n0 | 1.42825 | 293.15 | (Liquid... | |
| n0 | 1.42825 | 293.15 | (Liquid... | |
| n0 | 1.42842 | 293.15 | Experim... | |
| n0 | 1.42825 | 293.20 | Liquid-... | |
| n0 | 1.42636 | 298.15 | Experim... | |
| n0 | 1.42429 | 303.15 | Experim... | |
| n0 | 1.42222 | 308.15 | Experim... | |
| n0 | 1.42017 | 313.15 | Experim... | |
| n0 | 1.41819 | 318.15 | Experim... | |
| n0 | 1.41614 | 323.15 | Experim... | |
| ρl | [1032.62; 1066.79] | kg/m3 | [288.15; 323.15] |
|
|
T(K) Liquid Density (kg/m3) 1030 1040 1050 1060 1070 290 300 310 320 | ||||
| ρl | 1066.79 | kg/m3 | 288.15 | Experim... |
| ρl | 1061.92 | kg/m3 | 293.15 | Experim... |
| ρl | 1061.93 | kg/m3 | 293.15 | Thermod... |
| ρl | 1061.93 | kg/m3 | 293.15 | Densiti... |
| ρl | 1057.05 | kg/m3 | 298.15 | Experim... |
| ρl | 1052.18 | kg/m3 | 303.15 | Experim... |
| ρl | 1047.30 | kg/m3 | 308.15 | Experim... |
| ρl | 1042.41 | kg/m3 | 313.15 | Experim... |
| ρl | 1037.52 | kg/m3 | 318.15 | Experim... |
| ρl | 1032.62 | kg/m3 | 323.15 | Experim... |
| D*i | [0.00; 0.00] | m2/s | [293.43; 338.47] |
|
|
T(K) Self diffusion coefficient (m2/s) 3.00e-10 4.00e-10 5.00e-10 6.00e-10 7.00e-10 8.00e-10 9.00e-10 1.00e-9 300 310 320 330 | ||||
| D*i | 0.00 | m2/s | 293.43 | Self-di... |
| D*i | 0.00 | m2/s | 302.44 | Self-di... |
| D*i | 0.00 | m2/s | 311.45 | Self-di... |
| D*i | 0.00 | m2/s | 320.46 | Self-di... |
| D*i | 0.00 | m2/s | 329.45 | Self-di... |
| D*i | 0.00 | m2/s | 338.47 | Self-di... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 382.70 | K | 1.90 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 293.17 | 100.00 | 0.0033 |
| 293.17 | 1000.00 | 0.0033 |
| 293.15 | 5000.00 | 0.0035 |
| 293.15 | 10000.00 | 0.0036 |
| 293.15 | 15000.00 | 0.0038 |
| 293.15 | 20000.00 | 0.0040 |
| 293.15 | 30000.00 | 0.0043 |
| 293.15 | 40000.00 | 0.0047 |
| 303.17 | 100.00 | 0.0026 |
| 303.17 | 1000.00 | 0.0026 |
| 303.15 | 5000.00 | 0.0027 |
| 303.15 | 10000.00 | 0.0029 |
| 303.16 | 15000.00 | 0.0030 |
| 303.16 | 20000.00 | 0.0031 |
| 303.16 | 30000.00 | 0.0034 |
| 303.16 | 40000.00 | 0.0037 |
| 313.15 | 100.00 | 0.0021 |
| 313.14 | 1000.00 | 0.0022 |
| 313.15 | 5000.00 | 0.0022 |
| 313.15 | 10000.00 | 0.0023 |
| 313.14 | 15000.00 | 0.0024 |
| 313.14 | 20000.00 | 0.0025 |
| 313.14 | 30000.00 | 0.0027 |
| 313.15 | 40000.00 | 0.0030 |
| 323.15 | 100.00 | 0.0018 |
| 323.15 | 1000.00 | 0.0018 |
| 323.15 | 5000.00 | 0.0018 |
| 323.15 | 10000.00 | 0.0019 |
| 323.15 | 15000.00 | 0.0020 |
| 323.15 | 20000.00 | 0.0021 |
| 323.15 | 30000.00 | 0.0023 |
| 323.14 | 40000.00 | 0.0024 |
| 333.15 | 100.00 | 0.0015 |
| 333.15 | 1000.00 | 0.0015 |
| 333.15 | 5000.00 | 0.0016 |
| 333.15 | 10000.00 | 0.0016 |
| 333.15 | 15000.00 | 0.0017 |
| 333.15 | 20000.00 | 0.0018 |
| 333.15 | 30000.00 | 0.0019 |
| 333.14 | 40000.00 | 0.0020 |
| 343.15 | 100.00 | 0.0013 |
| 343.15 | 1000.00 | 0.0013 |
| 343.15 | 5000.00 | 0.0013 |
| 343.15 | 10000.00 | 0.0014 |
| 343.15 | 15000.00 | 0.0015 |
| 343.15 | 20000.00 | 0.0015 |
| 343.15 | 30000.00 | 0.0016 |
| 343.15 | 40000.00 | 0.0018 |
| 353.15 | 100.00 | 0.0011 |
| 353.16 | 1000.00 | 0.0011 |
| 353.15 | 5000.00 | 0.0012 |
| 353.15 | 10000.00 | 0.0012 |
| 353.15 | 15000.00 | 0.0013 |
| 353.15 | 20000.00 | 0.0013 |
| 353.15 | 30000.00 | 0.0014 |
| 353.15 | 40000.00 | 0.0015 |
| 363.15 | 100.00 | 0.0010 |
| 363.15 | 1000.00 | 0.0010 |
| 363.15 | 5000.00 | 0.0010 |
| 363.15 | 10000.00 | 0.0011 |
| 363.13 | 15000.00 | 0.0011 |
| 363.13 | 20000.00 | 0.0012 |
| 363.15 | 30000.00 | 0.0012 |
| 363.15 | 40000.00 | 0.0013 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 1061.2 |
| 293.15 | 4990.00 | 1064.2 |
| 293.15 | 10010.00 | 1067.3 |
| 293.15 | 20020.00 | 1073.2 |
| 293.15 | 25000.00 | 1076.0 |
| 293.15 | 14980.00 | 1070.3 |
| 293.15 | 7490.00 | 1065.8 |
| 293.15 | 5000.00 | 1064.3 |
| 293.15 | 2510.00 | 1062.8 |
| 323.15 | 100.00 | 1031.9 |
| 323.15 | 4990.00 | 1035.5 |
| 323.15 | 10060.00 | 1039.1 |
| 323.15 | 20020.00 | 1045.8 |
| 323.15 | 24990.00 | 1049.0 |
| 323.15 | 15010.00 | 1042.5 |
| 323.15 | 7490.00 | 1037.3 |
| 323.15 | 5000.00 | 1035.5 |
| 323.15 | 2540.00 | 1033.7 |
| 358.15 | 100.00 | 997.6 |
| 358.15 | 4980.00 | 1001.9 |
| 358.15 | 9980.00 | 1006.1 |
| 358.15 | 20030.00 | 1014.2 |
| 358.15 | 25000.00 | 1018.0 |
| 358.15 | 15030.00 | 1010.3 |
| 358.15 | 7500.00 | 1004.1 |
| 358.15 | 5020.00 | 1002.0 |
| 358.15 | 2500.00 | 999.8 |
| 303.15 | 100.00 | 1051.5 |
| 303.15 | 5010.00 | 1054.7 |
| 303.15 | 9990.00 | 1057.9 |
| 303.15 | 20000.00 | 1064.0 |
| 303.15 | 25000.00 | 1067.0 |
| 303.15 | 15010.00 | 1061.0 |
| 303.15 | 7510.00 | 1056.3 |
| 303.15 | 5010.00 | 1054.7 |
| 303.15 | 2510.00 | 1053.1 |
| 333.15 | 100.00 | 1022.1 |
| 333.15 | 5010.00 | 1026.0 |
| 333.15 | 10020.00 | 1029.7 |
| 333.15 | 20030.00 | 1036.8 |
| 333.15 | 24920.00 | 1040.1 |
| 333.15 | 15000.00 | 1033.2 |
| 333.15 | 7490.00 | 1027.8 |
| 333.15 | 5040.00 | 1026.0 |
| 333.15 | 2520.00 | 1024.1 |
| 293.15 | 100.00 | 1061.2 |
| 293.15 | 5020.00 | 1064.3 |
| 293.15 | 10020.00 | 1067.3 |
| 293.15 | 20240.00 | 1073.3 |
| 293.15 | 25010.00 | 1076.0 |
| 293.15 | 15030.00 | 1070.3 |
| 293.15 | 7570.00 | 1065.9 |
| 293.15 | 5030.00 | 1064.3 |
| 293.15 | 2540.00 | 1062.8 |
| 313.15 | 100.00 | 1041.8 |
| 313.15 | 5020.00 | 1045.2 |
| 313.15 | 10010.00 | 1048.5 |
| 313.15 | 20020.00 | 1054.9 |
| 313.15 | 25000.00 | 1058.0 |
| 313.15 | 15010.00 | 1051.7 |
| 313.15 | 7520.00 | 1046.8 |
| 313.15 | 5020.00 | 1045.1 |
| 313.15 | 2520.00 | 1043.5 |
| 343.15 | 100.00 | 1012.4 |
| 343.15 | 5010.00 | 1016.3 |
| 343.15 | 9990.00 | 1020.2 |
| 343.15 | 20000.00 | 1027.7 |
| 343.15 | 24990.00 | 1031.2 |
| 343.15 | 15010.00 | 1024.0 |
| 343.15 | 7530.00 | 1018.3 |
| 343.15 | 5000.00 | 1016.3 |
| 343.15 | 2500.00 | 1014.3 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [378.68; 537.32] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.73676e+01 | |||
| Coefficient B | -6.50271e+03 | |||
| Coefficient C | 2.04500e+00 | |||
| Temperature range, min. | 378.68 | |||
| Temperature range, max. | 537.32 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
| Pvap | 1.33 | kPa | 378.68 | Calculated Property |
| Pvap | 2.84 | kPa | 396.31 | Calculated Property |
| Pvap | 5.67 | kPa | 413.93 | Calculated Property |
| Pvap | 10.71 | kPa | 431.56 | Calculated Property |
| Pvap | 19.23 | kPa | 449.19 | Calculated Property |
| Pvap | 33.06 | kPa | 466.81 | Calculated Property |
| Pvap | 54.65 | kPa | 484.44 | Calculated Property |
| Pvap | 87.21 | kPa | 502.07 | Calculated Property |
| Pvap | 134.84 | kPa | 519.69 | Calculated Property |
| Pvap | 202.63 | kPa | 537.32 | Calculated Property |
Similar Compounds
Find more compounds similar to Hexanedioic acid, dimethyl ester.
Mixtures
- Hexanedioic acid, dimethyl ester + Water
- Acetic acid + Hexanedioic acid, dimethyl ester + Water
- Pentanoic acid, 4-oxo- + Hexanedioic acid, dimethyl ester + Water
- Pentanedioic acid, dimethyl ester + Hexanedioic acid, dimethyl ester
- Butanoic acid + Hexanedioic acid, dimethyl ester + Water
- Hexanedioic acid, dimethyl ester + Propanoic acid + Water
- Hexanedioic acid, dimethyl ester + Butanedioic acid, dimethyl ester
- 1-Butanol + Hexanedioic acid, dimethyl ester
- 2-Butanone + Hexanedioic acid, dimethyl ester
- Hexanedioic acid, dimethyl ester + 1,6-Hexanediol
- 1-Butanol + Hexanedioic acid, dimethyl ester + Tetrahydrofuran
- 2-Butanone + 1-Butanol + Hexanedioic acid, dimethyl ester
- Hexanedioic acid, dimethyl ester + Methyl Alcohol
- Formic acid + Hexanedioic acid, dimethyl ester + Water
- Choline chloride + 1,2-Ethanediol + Hexanedioic acid, dimethyl ester
- Hexanedioic acid + Hexanedioic acid, dimethyl ester + Methyl Alcohol
- Hexanedioic acid, dimethyl ester + Methyl Alcohol + Pentanedioic acid
- Butanedioic acid + Hexanedioic acid, dimethyl ester + Methyl Alcohol
- Hexanedioic acid + Hexanedioic acid, dimethyl ester
- Hexanedioic acid, dimethyl ester + Pentanedioic acid
Find more mixtures with Hexanedioic acid, dimethyl ester.
Sources
- Crippen Method
- Crippen Method
- Viscosity Measurements of Dialkyl Adipates in the Temperature Range of (283 to 363) K and up to 40 MPa
- Liquid liquid equilibria of the ternary system water + acetic acid + dimethyl adipate
- Liquid liquid equilibria of aqueous mixtures containing selected dibasic esters and/or methanol
- Phase equilibria of (water + levulinic acid + dibasic esters) ternary systems
- Viscosity and density measurements of compressed liquid dimethyl adipate using oscillating body techniques
- (Liquid + liquid) equilibria of the (water + carboxylic acid + dibasic esters mixture (DBE-2)) ternary systems
- Self-diffusivity measurements of dimethyl, diethyl, dipropyl, dibutyl, Bis(2-ethylhexyl) adipates from (293 - 339) K by a PGSE-NMR spin-echo technique
- (Liquid + liquid) equilibria of (water + butyric acid + dibasic esters) ternary systems
- (Liquid + liquid) equilibria of (water + propionic acid + dibasic esters) ternary systems
- Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
- 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
- Experimental Investigation of Interactions and Thermodynamic Properties of Poly(ethylene glycol) 200/400 + Dimethyl Adipate/Dimethyl Phthalate Binary Mixtures
- Thermophysical Properties and Solubility of Different Sugar-Derived Molecules in Deep Eutectic Solvents
- Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid, and Succinic Acid in Dimethyl Adipate + Methanol Mixtures
- Isobaric Vapor-Liquid Equilibrium for the Binary System of Dimethyl Adipate and 1,6-Hexanediol at 10, 20, and 99 kPa
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 7. Activity Coefficients of Aliphatic and Aromatic Esters and Benzylamine in 1-Methyl-3-ethylimidazolium Bis(trifluoromethylsulfonyl) Imide Using the Transpiration Method
- Vapor Pressures, Enthalpies of Vaporization, and Critical Parameters of a Series of Linear Aliphatic Dimethyl Esters of Dicarboxylic Acids
- Influence of the Molecular Structure on the Volumetric Properties and Viscosities of Dialkyl Adipates (Dimethyl, Diethyl, and Diisobutyl Adipates)
- Thermodynamic and Spectroscopic Study of the Ternary System Dimethyladipate + Tetrahydrofuran +1-Butanol at T = (288.15 to 323.15) K
- Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
- Vapor-Liquid Equilibrium of Mixtures Containing Adipic Acid, Glutaric Acid, Dimethyl Adipate, Dimethyl Glutarate, Methanol, and Water
- Liquid-Liquid Equilibria for Ternary Systems of Water + Formic Acid + Dibasic Esters
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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