- InChI
- InChI=1S/C5H6S/c1-5-2-3-6-4-5/h2-4H,1H3
- InChI Key
- QENGPZGAWFQWCZ-UHFFFAOYSA-N
- Formula
- C5H6S
- SMILES
- Cc1ccsc1
- Molecular Weight1
- 98.17
- CAS
- 616-44-4
- Other Names
-
- .beta.-methylthiophene
- 3-Methyl thiophene
- 3-Thiotolene
- 3-methylthiophene
- Methyl-3-thiophene
- «beta»-Methylthiophene
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (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 a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- 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.
- Ip : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2430 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ΔcH°liquid | -3470.40 ± 0.71 | kJ/mol | NIST |
| ΔfH°gas | 82.59 ± 0.92 | kJ/mol | NIST |
| ΔfH°liquid | 43.05 ± 0.88 | kJ/mol | NIST |
| ΔvapH° | [39.46; 39.50] | kJ/mol |
|
| ΔvapH° | 39.46 | kJ/mol | NIST |
| ΔvapH° | 39.50 | kJ/mol | NIST |
| ΔvapH° | 39.50 | kJ/mol | NIST |
| ΔvapH° | 39.50 | kJ/mol | NIST |
| IE | [8.40; 8.84] | eV |
|
| IE | 8.84 | eV | NIST |
| IE | 8.72 | eV | NIST |
| IE | 8.40 | eV | NIST |
| IE | 8.70 | eV | NIST |
| log10WS | -2.39 | Aq. Solubility Prediction | |
| logPoct/wat | 2.057 | Crippen Calculated Property | |
| McVol | 78.200 | ml/mol | McGowan Calculated Property |
| Pc | [4787.61; 4788.00] | kPa |
|
| Pc | 4787.61 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4788.00 | kPa | KDB |
| Inp | [755.00; 811.00] |
|
|
| Inp | 776.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 755.00 | NIST | |
| Inp | 763.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 805.00 | NIST | |
| Inp | 774.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 779.00 | NIST | |
| Inp | 760.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 779.00 | NIST | |
| Inp | Outlier 811.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 757.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 767.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 772.00 | NIST | |
| Inp | 759.00 | NIST | |
| Inp | 773.00 | NIST | |
| Inp | 776.00 | NIST | |
| Inp | 782.00 | NIST | |
| Ip | [1078.00; 1136.00] |
|
|
| Ip | 1136.00 | NIST | |
| Ip | 1106.00 | NIST | |
| Ip | 1115.00 | NIST | |
| Ip | Outlier 1078.00 | NIST | |
| Ip | 1099.00 | NIST | |
| Ip | 1114.00 | NIST | |
| Ip | 1124.00 | NIST | |
| Ip | 1121.00 | NIST | |
| Ip | 1117.00 | NIST | |
| Ip | 1130.00 | NIST | |
| Ip | 1120.00 | NIST | |
| Ip | 1101.00 | NIST | |
| Ip | 1127.00 | NIST | |
| Ip | 1110.00 | NIST | |
| Ip | 1127.00 | NIST | |
| Ip | 1130.00 | NIST | |
| Ip | 1123.00 | NIST | |
| Ip | 1120.00 | NIST | |
| Ip | 1123.00 | NIST | |
| Ip | 1127.00 | NIST | |
| Ip | 1123.00 | NIST | |
| Ip | 1127.00 | NIST | |
| Ip | 1120.00 | NIST | |
| Ip | 1120.00 | NIST | |
| Ip | 1101.00 | NIST | |
| Ip | 1123.00 | NIST | |
| Ip | 1127.00 | NIST | |
| Ip | 1115.00 | NIST | |
| Ip | 1121.00 | NIST | |
| Ip | 1136.00 | NIST | |
| Tboil | [388.35; 388.60] | K |
|
| Tboil | 388.35 | K | Isobaric vapor-liquid equilibrium for four binary systems of 3-methylthiophene |
| Tboil | 388.35 | K | Isobaric vapor-liquid equilibrium for systems containing sulfur compounds |
| Tboil | 388.60 | K | KDB |
| Tboil | 388.60 | K | NIST |
| Tboil | 388.60 | K | NIST |
| Tboil | 388.60 ± 0.30 | K | NIST |
| Tc | [607.30; 610.80] | K |
|
| Tc | 607.30 | K | DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development |
| Tc | 610.80 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 610.80 | K | KDB |
| Tc | 610.80 | K | NIST |
| Tfus | [204.15; 204.21] | K |
|
| Tfus | 204.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 204.20 | K | KDB |
| Tfus | 204.21 ± 0.06 | K | NIST |
| Ttriple | [204.18; 204.20] | K |
|
| Ttriple | 204.20 | K | Staveley, Lobo and Calado (1981), triple points Compiled value |
| Ttriple | 204.18 | K | KDB |
| Ttriple | 204.19 ± 0.02 | K | NIST |
| Ttriple | 204.19 ± 0.02 | K | NIST |
| Vc | [0.275; 0.275] | m3/kmol |
|
| Vc | 0.275 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.275 | m3/kmol | KDB |
| Zc | 0.2590810 | KDB |
Cheméo can also estimate Standard Gibbs free energy of formation for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [10.54; 10.54] | kJ/mol | [204.20; 204.20] |
|
| ΔfusH | 10.54 | kJ/mol | 204.20 | NIST |
| ΔfusH | 10.54 | kJ/mol | 204.20 | NIST |
| ΔvapH | [34.24; 39.50] | kJ/mol | [329.00; 388.60] |
|
| ΔvapH | 39.50 | kJ/mol | 329.00 | NIST |
| ΔvapH | 39.50 | kJ/mol | 329.00 | NIST |
| ΔvapH | 37.40 | kJ/mol | 353.00 | NIST |
| ΔvapH | 37.30 | kJ/mol | 360.50 | NIST |
| ΔvapH | 36.80 | kJ/mol | 362.00 | NIST |
| ΔvapH | 37.50 | kJ/mol | 363.00 | NIST |
| ΔvapH | 34.25 | kJ/mol | 388.60 | KDB |
| ΔvapH | 34.24 | kJ/mol | 388.60 | NIST |
| n0 | [1.51720; 1.51720] | [298.15; 298.15] |
|
|
| n0 | 1.51720 | 298.15 | Phase equilibria on four binary systems containing 3-methylthiophene | |
| n0 | 1.51720 | 298.15 | Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons | |
| ρl | 1020.89 | kg/m3 | 293.10 | KDB |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 387.20 | K | 98.40 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 1031.82 |
| 288.15 | 100.00 | 1026.57 |
| 293.15 | 100.00 | 1021.31 |
| 298.15 | 100.00 | 1016.0 |
| 303.15 | 100.00 | 1010.72 |
| 308.15 | 100.00 | 1005.4 |
| 313.15 | 100.00 | 1000.05 |
| 318.15 | 100.00 | 994.7 |
| 323.15 | 100.00 | 989.3 |
| 328.15 | 100.00 | 983.88 |
| 333.15 | 100.00 | 978.47 |
| 338.15 | 100.00 | 972.98 |
| 283.15 | 2000.00 | 1033.26 |
| 288.15 | 2000.00 | 1028.05 |
| 293.15 | 2000.00 | 1022.81 |
| 298.15 | 2000.00 | 1017.57 |
| 303.15 | 2000.00 | 1012.32 |
| 308.15 | 2000.00 | 1007.04 |
| 313.15 | 2000.00 | 1001.76 |
| 318.15 | 2000.00 | 996.44 |
| 323.15 | 2000.00 | 991.1 |
| 328.15 | 2000.00 | 985.74 |
| 333.15 | 2000.00 | 980.39 |
| 338.15 | 2000.00 | 974.96 |
| 283.15 | 5000.00 | 1035.47 |
| 288.15 | 5000.00 | 1030.34 |
| 293.15 | 5000.00 | 1025.16 |
| 298.15 | 5000.00 | 1019.98 |
| 303.15 | 5000.00 | 1014.81 |
| 308.15 | 5000.00 | 1009.61 |
| 313.15 | 5000.00 | 1004.39 |
| 318.15 | 5000.00 | 999.15 |
| 323.15 | 5000.00 | 993.9 |
| 328.15 | 5000.00 | 988.63 |
| 333.15 | 5000.00 | 983.35 |
| 338.15 | 5000.00 | 978.01 |
| 283.15 | 7000.00 | 1036.93 |
| 288.15 | 7000.00 | 1031.84 |
| 293.15 | 7000.00 | 1026.7 |
| 298.15 | 7000.00 | 1021.56 |
| 303.15 | 7000.00 | 1016.43 |
| 308.15 | 7000.00 | 1011.27 |
| 313.15 | 7000.00 | 1006.11 |
| 318.15 | 7000.00 | 1000.93 |
| 323.15 | 7000.00 | 995.72 |
| 328.15 | 7000.00 | 990.51 |
| 333.15 | 7000.00 | 985.3 |
| 338.15 | 7000.00 | 980.02 |
| 283.15 | 10000.00 | 1039.07 |
| 288.15 | 10000.00 | 1034.03 |
| 293.15 | 10000.00 | 1028.95 |
| 298.15 | 10000.00 | 1023.89 |
| 303.15 | 10000.00 | 1018.83 |
| 308.15 | 10000.00 | 1013.72 |
| 313.15 | 10000.00 | 1008.64 |
| 318.15 | 10000.00 | 1003.52 |
| 323.15 | 10000.00 | 998.41 |
| 328.15 | 10000.00 | 993.26 |
| 333.15 | 10000.00 | 988.13 |
| 338.15 | 10000.00 | 982.95 |
| 283.15 | 15000.00 | 1042.56 |
| 288.15 | 15000.00 | 1037.61 |
| 293.15 | 15000.00 | 1032.61 |
| 298.15 | 15000.00 | 1027.64 |
| 303.15 | 15000.00 | 1022.7 |
| 308.15 | 15000.00 | 1017.69 |
| 313.15 | 15000.00 | 1012.71 |
| 318.15 | 15000.00 | 1007.7 |
| 323.15 | 15000.00 | 1002.71 |
| 328.15 | 15000.00 | 997.7 |
| 333.15 | 15000.00 | 992.67 |
| 338.15 | 15000.00 | 987.63 |
| 283.15 | 20000.00 | 1045.93 |
| 288.15 | 20000.00 | 1041.07 |
| 293.15 | 20000.00 | 1036.16 |
| 298.15 | 20000.00 | 1031.29 |
| 303.15 | 20000.00 | 1026.42 |
| 308.15 | 20000.00 | 1021.53 |
| 313.15 | 20000.00 | 1016.63 |
| 318.15 | 20000.00 | 1011.74 |
| 323.15 | 20000.00 | 1006.85 |
| 328.15 | 20000.00 | 1001.93 |
| 333.15 | 20000.00 | 997.03 |
| 338.15 | 20000.00 | 992.12 |
| 283.15 | 25000.00 | 1049.2 |
| 288.15 | 25000.00 | 1044.41 |
| 293.15 | 25000.00 | 1039.6 |
| 298.15 | 25000.00 | 1034.81 |
| 303.15 | 25000.00 | 1030.01 |
| 308.15 | 25000.00 | 1025.22 |
| 313.15 | 25000.00 | 1020.43 |
| 318.15 | 25000.00 | 1015.6 |
| 323.15 | 25000.00 | 1010.83 |
| 328.15 | 25000.00 | 1006.0 |
| 333.15 | 25000.00 | 1001.22 |
| 338.15 | 25000.00 | 996.41 |
| 283.15 | 30000.00 | 1052.37 |
| 288.15 | 30000.00 | 1047.65 |
| 293.15 | 30000.00 | 1042.92 |
| 298.15 | 30000.00 | 1038.2 |
| 303.15 | 30000.00 | 1033.5 |
| 308.15 | 30000.00 | 1028.73 |
| 313.15 | 30000.00 | 1024.08 |
| 318.15 | 30000.00 | 1019.35 |
| 323.15 | 30000.00 | 1014.66 |
| 328.15 | 30000.00 | 1009.94 |
| 333.15 | 30000.00 | 1005.22 |
| 338.15 | 30000.00 | 1000.53 |
| 283.15 | 35000.00 | 1055.46 |
| 288.15 | 35000.00 | 1050.8 |
| 293.15 | 35000.00 | 1046.15 |
| 298.15 | 35000.00 | 1041.52 |
| 303.15 | 35000.00 | 1036.87 |
| 308.15 | 35000.00 | 1032.24 |
| 313.15 | 35000.00 | 1027.61 |
| 318.15 | 35000.00 | 1022.99 |
| 323.15 | 35000.00 | 1018.35 |
| 328.15 | 35000.00 | 1013.73 |
| 333.15 | 35000.00 | 1009.12 |
| 338.15 | 35000.00 | 1004.49 |
| 283.15 | 40000.00 | 1058.46 |
| 288.15 | 40000.00 | 1053.86 |
| 293.15 | 40000.00 | 1049.27 |
| 298.15 | 40000.00 | 1044.71 |
| 303.15 | 40000.00 | 1040.16 |
| 308.15 | 40000.00 | 1035.59 |
| 313.15 | 40000.00 | 1031.05 |
| 318.15 | 40000.00 | 1026.48 |
| 323.15 | 40000.00 | 1021.93 |
| 328.15 | 40000.00 | 1017.38 |
| 333.15 | 40000.00 | 1012.87 |
| 338.15 | 40000.00 | 1008.33 |
| 283.15 | 45000.00 | 1061.37 |
| 288.15 | 45000.00 | 1056.84 |
| 293.15 | 45000.00 | 1052.31 |
| 298.15 | 45000.00 | 1047.82 |
| 303.15 | 45000.00 | 1043.34 |
| 308.15 | 45000.00 | 1038.84 |
| 313.15 | 45000.00 | 1034.35 |
| 318.15 | 45000.00 | 1029.86 |
| 323.15 | 45000.00 | 1025.4 |
| 328.15 | 45000.00 | 1020.94 |
| 333.15 | 45000.00 | 1016.49 |
| 338.15 | 45000.00 | 1012.04 |
| 283.15 | 50000.00 | 1064.22 |
| 288.15 | 50000.00 | 1059.74 |
| 293.15 | 50000.00 | 1055.28 |
| 298.15 | 50000.00 | 1050.84 |
| 303.15 | 50000.00 | 1046.42 |
| 308.15 | 50000.00 | 1041.98 |
| 313.15 | 50000.00 | 1037.58 |
| 318.15 | 50000.00 | 1033.15 |
| 323.15 | 50000.00 | 1028.76 |
| 328.15 | 50000.00 | 1024.36 |
| 333.15 | 50000.00 | 1020.0 |
| 338.15 | 50000.00 | 1015.62 |
| 283.15 | 55000.00 | 1066.97 |
| 288.15 | 55000.00 | 1062.56 |
| 293.15 | 55000.00 | 1058.15 |
| 298.15 | 55000.00 | 1053.78 |
| 303.15 | 55000.00 | 1049.41 |
| 308.15 | 55000.00 | 1045.05 |
| 313.15 | 55000.00 | 1040.71 |
| 318.15 | 55000.00 | 1036.33 |
| 323.15 | 55000.00 | 1032.03 |
| 328.15 | 55000.00 | 1027.68 |
| 333.15 | 55000.00 | 1023.38 |
| 338.15 | 55000.00 | 1019.08 |
| 283.15 | 60000.00 | 1069.67 |
| 288.15 | 60000.00 | 1065.32 |
| 293.15 | 60000.00 | 1060.96 |
| 298.15 | 60000.00 | 1056.65 |
| 303.15 | 60000.00 | 1052.33 |
| 308.15 | 60000.00 | 1048.03 |
| 313.15 | 60000.00 | 1043.73 |
| 318.15 | 60000.00 | 1039.44 |
| 323.15 | 60000.00 | 1035.18 |
| 328.15 | 60000.00 | 1030.89 |
| 333.15 | 60000.00 | 1026.67 |
| 338.15 | 60000.00 | 1022.44 |
| 283.15 | 65000.00 | 1072.32 |
| 288.15 | 65000.00 | 1068.01 |
| 293.15 | 65000.00 | 1063.7 |
| 298.15 | 65000.00 | 1059.43 |
| 303.15 | 65000.00 | 1055.16 |
| 308.15 | 65000.00 | 1050.91 |
| 313.15 | 65000.00 | 1046.69 |
| 318.15 | 65000.00 | 1042.45 |
| 323.15 | 65000.00 | 1038.24 |
| 328.15 | 65000.00 | 1034.03 |
| 333.15 | 65000.00 | 1029.88 |
| 338.15 | 65000.00 | 1025.7 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [282.44; 414.79] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.45884e+01 | |||
| Coefficient B | -3.49514e+03 | |||
| Coefficient C | -3.80360e+01 | |||
| Temperature range, min. | 282.44 | |||
| Temperature range, max. | 414.79 | |||
| Pvap | 1.33 | kPa | 282.44 | Calculated Property |
| Pvap | 3.00 | kPa | 297.15 | Calculated Property |
| Pvap | 6.20 | kPa | 311.85 | Calculated Property |
| Pvap | 11.87 | kPa | 326.56 | Calculated Property |
| Pvap | 21.37 | kPa | 341.26 | Calculated Property |
| Pvap | 36.42 | kPa | 355.97 | Calculated Property |
| Pvap | 59.21 | kPa | 370.67 | Calculated Property |
| Pvap | 92.38 | kPa | 385.38 | Calculated Property |
| Pvap | 139.02 | kPa | 400.08 | Calculated Property |
| Pvap | 202.63 | kPa | 414.79 | Calculated Property |
| Pvap | [1.34; 4952.72] | kPa | [284.15; 615.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.19136e+01 | |||
| Coefficient B | -6.97496e+03 | |||
| Coefficient C | -8.40512e+00 | |||
| Coefficient D | 5.04996e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 284.15 | |||
| Temperature range, max. | 615.00 | |||
| Pvap | 1.34 | kPa | 284.15 | Calculated Property |
| Pvap | 8.95 | kPa | 320.91 | Calculated Property |
| Pvap | 38.08 | kPa | 357.67 | Calculated Property |
| Pvap | 118.46 | kPa | 394.43 | Calculated Property |
| Pvap | 294.84 | kPa | 431.19 | Calculated Property |
| Pvap | 624.18 | kPa | 467.96 | Calculated Property |
| Pvap | 1172.62 | kPa | 504.72 | Calculated Property |
| Pvap | 2015.27 | kPa | 541.48 | Calculated Property |
| Pvap | 3239.61 | kPa | 578.24 | Calculated Property |
| Pvap | 4952.72 | kPa | 615.00 | Calculated Property |
| Pvap | [15.43; 65.44] | kPa | [333.40; 373.50] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.53474e+01 | |||
| Coefficient B | -3.90868e+03 | |||
| Coefficient C | -2.34560e+01 | |||
| Reference | Eon, Pommier, et al., 1971 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 333.40 | |||
| Temperature range, max. | 373.50 | |||
| Pvap | 15.43 | kPa | 333.40 | Calculated Property |
| Pvap | 18.45 | kPa | 337.86 | Calculated Property |
| Pvap | 21.95 | kPa | 342.31 | Calculated Property |
| Pvap | 25.99 | kPa | 346.77 | Calculated Property |
| Pvap | 30.64 | kPa | 351.22 | Calculated Property |
| Pvap | 35.95 | kPa | 355.68 | Calculated Property |
| Pvap | 42.01 | kPa | 360.13 | Calculated Property |
| Pvap | 48.88 | kPa | 364.59 | Calculated Property |
| Pvap | 56.67 | kPa | 369.04 | Calculated Property |
| Pvap | 65.44 | kPa | 373.50 | Calculated Property |
Similar Compounds
Find more compounds similar to Thiophene, 3-methyl-.
Mixtures
- Thiophene, 3-methyl- + Pentane, 2,2,4-trimethyl-
- Thiophene, 3-methyl- + 1-Pentene, 2,4,4-trimethyl-
- Thiophene, 3-methyl- + Cyclohexane
- Thiophene, 3-methyl- + 1-Hexene
- Thiophene, 3-methyl- + Pentane, 2-methyl-
- Thiophene, 3-methyl- + n-Hexane
- Thiophene, 3-methyl- + Cyclopentane, methyl-
- Thiophene, 3-methyl- + Cyclohexane, methyl-
- Thiophene, 3-methyl- + 1-Butene, 2,3-dimethyl-
- Thiophene, 3-methyl- + 1,2-Ethanediol + Tetrahexylammonium bromide
- Thiophene, 3-methyl- + Glycerin + Tetrahexylammonium bromide
- Thiophene, 3-methyl- + Toluene
- Thiophene, 3-methyl- + o-Xylene
- Thiophene, 3-methyl- + 1,2,4-Trimethylbenzene
- Thiophene, 3-methyl- + 2-Butene, 2,3-dimethyl-
- Thiophene, 3-methyl- + Heptane
- Thiophene, 3-methyl- + Butane, 2-methyl-
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
- Crippen Method
- Phase equilibria on four binary systems containing 3-methylthiophene
- Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons
- Phase equilibria on five binary systems containing 1-butanethiol and 3-methylthiophene in hydrocarbons
- Isobaric vapor-liquid equilibrium for four binary systems of 3-methylthiophene
- Isobaric vapor-liquid equilibrium for systems containing sulfur compounds
- Densities at high pressures and derived properties of thiophenes
- Removal of 2- and 3-methylthiophene from their mixtures with n-heptane using tetrahexylammonium bromide-based deep eutectic solvents as extractive desulfurization agents
- DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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