- InChI
- InChI=1S/C7H8O/c1-8-7-5-3-2-4-6-7/h2-6H,1H3
- InChI Key
- RDOXTESZEPMUJZ-UHFFFAOYSA-N
- Formula
- C7H8O
- SMILES
- COc1ccccc1
- Molecular Weight1
- 108.14
- CAS
- 100-66-3
- Other Names
-
- Anisol
- Anizol
- Benzene, methoxy-
- Ether, methyl phenyl-
- Methoxybenzene
- Methyl phenyl ether
- NSC 7920
- Phenoxymethane
- Phenyl methyl ether
- UN 2222
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- 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.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 839.60 | kJ/mol | NIST |
| BasG | 807.20 | kJ/mol | NIST |
| ΔcH°liquid | [-3783.12; -3778.00] | kJ/mol |
|
| ΔcH°liquid | -3783.12 | kJ/mol | NIST |
| ΔcH°liquid | -3778.00 ± 0.80 | kJ/mol | NIST |
| ΔcH°liquid | -3779.50 | kJ/mol | NIST |
| Cp,liquid | 191.54 | J/mol×K | Thermod... |
| ΔfG° | 15.47 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-76.69; -67.90] | kJ/mol |
|
| ΔfH°gas | -67.90 ± 1.20 | kJ/mol | NIST |
| ΔfH°gas | -76.69 ± 0.92 | kJ/mol | NIST |
| ΔfH°gas | -70.70 | kJ/mol | NIST |
| ΔfH°gas | -75.10 | kJ/mol | NIST |
| ΔfH°liquid | [-120.00; -114.80] | kJ/mol |
|
| ΔfH°liquid | -114.80 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -120.00 ± 0.80 | kJ/mol | NIST |
| ΔfH°liquid | -118.40 | kJ/mol | NIST |
| ΔfusH° | 9.12 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [38.00; 46.91] | kJ/mol |
|
| ΔvapH° | 46.91 | kJ/mol | NIST |
| ΔvapH° | 44.30 | kJ/mol | NIST |
| ΔvapH° | 46.60 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 45.30 | kJ/mol | NIST |
| ΔvapH° | 46.90 | kJ/mol | NIST |
| ΔvapH° | 46.84 ± 0.22 | kJ/mol | NIST |
| ΔvapH° | 46.90 | kJ/mol | NIST |
| ΔvapH° | 46.80 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 38.00 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 43.30 | kJ/mol | NIST |
| ΔvapH° | 38.20 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 39.40 | kJ/mol | NIST |
| ΔvapH° | 39.40 | kJ/mol | NIST |
| IE | [8.10; 8.80] | eV |
|
| IE | 8.20 ± 0.05 | eV | NIST |
| IE | 8.25 ± 0.03 | eV | NIST |
| IE | 8.10 | eV | NIST |
| IE | 8.24 | eV | NIST |
| IE | 8.60 | eV | NIST |
| IE | 8.20 ± 0.02 | eV | NIST |
| IE | 8.37 | eV | NIST |
| IE | 8.30 ± 0.10 | eV | NIST |
| IE | 8.20 | eV | NIST |
| IE | 8.18 | eV | NIST |
| IE | Outlier 8.80 ± 0.10 | eV | NIST |
| IE | 8.40 ± 0.10 | eV | NIST |
| IE | 8.21 | eV | NIST |
| IE | 8.60 | eV | NIST |
| IE | 8.22 ± 0.02 | eV | NIST |
| IE | 8.20 ± 0.02 | eV | NIST |
| IE | 8.39 | eV | NIST |
| IE | 8.45 | eV | NIST |
| IE | 8.42 | eV | NIST |
| IE | 8.25 | eV | NIST |
| IE | 8.39 | eV | NIST |
| IE | 8.46 | eV | NIST |
| IE | 8.42 | eV | NIST |
| log10WS | [-1.85; -1.85] |
|
|
| log10WS | -1.85 | Aq. Sol... | |
| log10WS | -1.85 | Estimat... | |
| logPoct/wat | 1.695 | Crippen Calculated Property | |
| McVol | 91.600 | ml/mol | McGowan Calculated Property |
| Pc | [4174.59; 4250.00] | kPa |
|
| Pc | 4222.00 ± 20.00 | kPa | NIST |
| Pc | 4250.00 ± 100.00 | kPa | NIST |
| Pc | 4179.66 ± 202.65 | kPa | NIST |
| Pc | 4180.00 ± 60.79 | kPa | NIST |
| Pc | 4174.59 ± 101.32 | kPa | NIST |
| Pc | 4184.72 ± 101.32 | kPa | NIST |
| ρc | 316.84 ± 9.95 | kg/m3 | NIST |
| Inp | [880.00; 956.00] |
|
|
| Inp | 891.69 | NIST | |
| Inp | 893.73 | NIST | |
| Inp | 895.86 | NIST | |
| Inp | 897.86 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 902.32 | NIST | |
| Inp | 904.91 | NIST | |
| Inp | 907.48 | NIST | |
| Inp | 909.99 | NIST | |
| Inp | 912.78 | NIST | |
| Inp | 889.68 | NIST | |
| Inp | 909.00 | NIST | |
| Inp | 901.90 | NIST | |
| Inp | 903.80 | NIST | |
| Inp | 908.80 | NIST | |
| Inp | 898.10 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 910.10 | NIST | |
| Inp | 909.40 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | Outlier 880.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | Outlier 940.00 | NIST | |
| Inp | 913.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 923.60 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 898.40 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 900.30 | NIST | |
| Inp | 893.90 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | Outlier 956.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 900.00 | NIST | |
| I | [1306.00; 1398.00] |
|
|
| I | 1340.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1373.00 | NIST | |
| I | 1331.00 | NIST | |
| I | 1368.60 | NIST | |
| I | 1368.60 | NIST | |
| I | Outlier 1394.00 | NIST | |
| I | Outlier 1398.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1355.40 | NIST | |
| I | 1345.60 | NIST | |
| I | 1356.80 | NIST | |
| I | 1353.80 | NIST | |
| I | 1348.20 | NIST | |
| I | 1351.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1350.90 | NIST | |
| I | 1349.00 | NIST | |
| I | 1342.00 | NIST | |
| I | 1344.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1355.00 | NIST | |
| I | 1355.00 | NIST | |
| I | 1355.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1327.00 | NIST | |
| I | 1327.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1327.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1327.00 | NIST | |
| I | Outlier 1306.00 | NIST | |
| I | 1340.00 | NIST | |
| I | 1327.00 | NIST | |
| I | 1330.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1340.00 | NIST | |
| I | 1368.60 | NIST | |
| Tboil | [426.56; 426.77] | K |
|
| Tboil | 426.56 | K | Isobari... |
| Tboil | 426.69 | K | Isobari... |
| Tboil | 426.77 | K | Vapor-L... |
| Tc | 619.41 | K | Joback Calculated Property |
| Tfus | [235.20; 236.03] | K |
|
| Tfus | 236.03 | K | Aq. Sol... |
| Tfus | 235.20 | K | The sol... |
| Vc | 0.338 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [162.46; 195.94] | J/mol×K | [388.15; 498.15] |
|
| Cp,gas | 162.46 | J/mol×K | 388.15 | NIST |
| Cp,gas | 168.82 | J/mol×K | 408.15 | NIST |
| Cp,gas | 176.98 | J/mol×K | 433.15 | NIST |
| Cp,gas | 183.05 | J/mol×K | 453.15 | NIST |
| Cp,gas | 188.99 | J/mol×K | 473.15 | NIST |
| Cp,gas | 195.94 | J/mol×K | 498.15 | NIST |
| Cp,liquid | [191.20; 208.80] | J/mol×K | [297.20; 304.80] |
|
| Cp,liquid | 191.20 | J/mol×K | 297.20 | NIST |
| Cp,liquid | 199.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 208.80 | J/mol×K | 304.80 | NIST |
| η | [0.0009310; 0.0011880] | Pa×s | [288.15; 303.15] |
|
| η | 0.0011880 | Pa×s | 288.15 | Viscosi... |
| η | 0.0010840 | Pa×s | 293.15 | Viscosi... |
| η | 0.0010170 | Pa×s | 298.15 | Viscosi... |
| η | 0.0009310 | Pa×s | 303.15 | Viscosi... |
| ΔfusH | [11.66; 17.03] | kJ/mol | [236.00; 293.20] |
|
| ΔfusH | 12.89 | kJ/mol | 236.00 | NIST |
| ΔfusH | 11.66 | kJ/mol | 237.00 | NIST |
| ΔfusH | 17.03 | kJ/mol | 293.20 | NIST |
| ΔvapH | [38.90; 42.90] | kJ/mol | [359.50; 427.00] |
|
| ΔvapH | 39.00 | kJ/mol | 359.50 | NIST |
| ΔvapH | 42.90 ± 0.10 | kJ/mol | 367.00 | NIST |
| ΔvapH | 42.00 ± 0.10 | kJ/mol | 382.00 | NIST |
| ΔvapH | 40.50 ± 0.10 | kJ/mol | 402.00 | NIST |
| ΔvapH | 41.80 | kJ/mol | 405.50 | NIST |
| ΔvapH | 41.90 | kJ/mol | 409.50 | NIST |
| ΔvapH | 41.90 | kJ/mol | 409.50 | NIST |
| ΔvapH | 38.97 | kJ/mol | 426.80 | NIST |
| ΔvapH | 38.90 ± 0.10 | kJ/mol | 427.00 | NIST |
| Pvap | [0.12; 96.15] | kPa | [278.30; 424.79] |
|
| Pvap | 0.12 | kPa | 278.30 | Thermod... |
| Pvap | 0.15 | kPa | 281.30 | Thermod... |
| Pvap | 0.19 | kPa | 284.30 | Thermod... |
| Pvap | 0.23 | kPa | 287.30 | Thermod... |
| Pvap | 0.29 | kPa | 290.30 | Thermod... |
| Pvap | 0.35 | kPa | 293.30 | Thermod... |
| Pvap | 0.41 | kPa | 296.30 | Thermod... |
| Pvap | 0.50 | kPa | 298.60 | Thermod... |
| Pvap | 0.50 | kPa | 298.60 | Thermod... |
| Pvap | 0.52 | kPa | 299.30 | Thermod... |
| Pvap | 0.61 | kPa | 302.20 | Thermod... |
| Pvap | 0.67 | kPa | 303.60 | Thermod... |
| Pvap | 0.67 | kPa | 303.60 | Thermod... |
| Pvap | 0.77 | kPa | 306.20 | Thermod... |
| Pvap | 0.89 | kPa | 308.60 | Thermod... |
| Pvap | 0.89 | kPa | 308.60 | Thermod... |
| Pvap | 0.93 | kPa | 309.20 | Thermod... |
| Pvap | 1.11 | kPa | 312.30 | Thermod... |
| Pvap | 1.40 | kPa | 313.20 | Isother... |
| Pvap | 1.18 | kPa | 313.60 | Thermod... |
| Pvap | 1.18 | kPa | 313.60 | Thermod... |
| Pvap | 1.54 | kPa | 318.60 | Thermod... |
| Pvap | 1.54 | kPa | 318.60 | Thermod... |
| Pvap | 2.00 | kPa | 323.60 | Thermod... |
| Pvap | 93.13 | kPa | 423.38 | Refract... |
| Pvap | 96.15 | kPa | 424.55 | Vapor L... |
| Pvap | 96.15 | kPa | 424.61 | Vapor L... |
| Pvap | 96.15 | kPa | 424.79 | Vapor L... |
| n0 | [1.50341; 1.52560] | [288.15; 318.15] |
|
|
| n0 | 1.52560 | 288.15 | Excess ... | |
| n0 | 1.51710 | 293.13 | Isobari... | |
| n0 | 1.51770 | 293.15 | Densiti... | |
| n0 | 1.51610 | 293.15 | Physica... | |
| n0 | 1.51690 | 293.15 | Excess ... | |
| n0 | 1.51710 | 293.15 | Isobari... | |
| n0 | 1.51720 | 293.15 | Excess ... | |
| n0 | 1.51495 | 298.15 | Densiti... | |
| n0 | 1.51360 | 298.15 | Excess ... | |
| n0 | 1.51410 | 298.15 | Physica... | |
| n0 | 1.51410 | 298.15 | Excess ... | |
| n0 | 1.51530 | 298.15 | Enthalp... | |
| n0 | 1.51370 | 298.15 | Thermod... | |
| n0 | 1.51480 | 298.15 | Density... | |
| n0 | 1.51554 | 298.15 | Isobari... | |
| n0 | 1.51420 | 298.15 | (Vapor ... | |
| n0 | 1.51460 | 298.15 | Volumet... | |
| n0 | 1.51420 | 298.15 | (Vapor ... | |
| n0 | 1.51191 | 303.15 | Volumet... | |
| n0 | 1.51290 | 303.15 | Physica... | |
| n0 | 1.51395 | 303.15 | Densiti... | |
| n0 | 1.51120 | 303.15 | Excess ... | |
| n0 | 1.51130 | 303.15 | Thermod... | |
| n0 | 1.51240 | 303.15 | Density... | |
| n0 | 1.51240 | 303.15 | Densiti... | |
| n0 | 1.51170 | 303.15 | Excess ... | |
| n0 | 1.50950 | 308.15 | Enthalp... | |
| n0 | 1.50880 | 308.15 | Excess ... | |
| n0 | 1.50920 | 308.15 | Density... | |
| n0 | 1.50880 | 308.15 | Thermod... | |
| n0 | 1.51095 | 308.15 | Densiti... | |
| n0 | 1.50865 | 308.15 | Volumet... | |
| n0 | 1.50604 | 313.15 | Volumet... | |
| n0 | 1.50341 | 318.15 | Volumet... | |
| ρl | [965.73; 1003.30] | kg/m3 | [283.15; 323.15] |
|
| ρl | 1003.30 | kg/m3 | 283.15 | The den... |
| ρl | 996.56 | kg/m3 | 288.15 | Solid-l... |
| ρl | 998.62 | kg/m3 | 288.15 | The den... |
| ρl | 991.95 | kg/m3 | 293.15 | Solid-l... |
| ρl | 994.01 | kg/m3 | 293.15 | The den... |
| ρl | 989.09 | kg/m3 | 298.15 | Solid-l... |
| ρl | 989.42 | kg/m3 | 298.15 | Solid-l... |
| ρl | 989.32 | kg/m3 | 298.15 | The phy... |
| ρl | 989.32 | kg/m3 | 298.15 | The den... |
| ρl | 989.42 | kg/m3 | 298.15 | Ternary... |
| ρl | 988.90 | kg/m3 | 298.15 | Intermo... |
| ρl | 993.60 | kg/m3 | 298.15 | Densiti... |
| ρl | 989.13 | kg/m3 | 298.15 | Liquid-... |
| ρl | 989.13 | kg/m3 | 298.15 | Binary ... |
| ρl | 989.42 | kg/m3 | 298.15 | Liquid ... |
| ρl | 989.40 | kg/m3 | 303.15 | Densiti... |
| ρl | 983.04 | kg/m3 | 303.15 | Solid-l... |
| ρl | 984.59 | kg/m3 | 303.15 | The den... |
| ρl | 984.40 | kg/m3 | 303.15 | Density... |
| ρl | 979.80 | kg/m3 | 308.15 | Density... |
| ρl | 979.50 | kg/m3 | 308.15 | Intermo... |
| ρl | 984.60 | kg/m3 | 308.15 | Densiti... |
| ρl | 978.34 | kg/m3 | 308.15 | Solid-l... |
| ρl | 980.04 | kg/m3 | 308.15 | The phy... |
| ρl | 975.25 | kg/m3 | 313.15 | The phy... |
| ρl | 975.00 | kg/m3 | 313.15 | Density... |
| ρl | 973.62 | kg/m3 | 313.15 | Solid-l... |
| ρl | 980.00 | kg/m3 | 313.15 | Densiti... |
| ρl | 969.99 | kg/m3 | 318.15 | Solid-l... |
| ρl | 970.52 | kg/m3 | 318.15 | The phy... |
| ρl | 970.50 | kg/m3 | 318.15 | Intermo... |
| ρl | 965.73 | kg/m3 | 323.15 | The phy... |
| ΔfusS | 58.10 | J/mol×K | 293.20 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 989.2 |
| 298.15 | 10000.00 | 995.6 |
| 298.15 | 15000.00 | 998.5 |
| 298.15 | 20000.00 | 1001.4 |
| 298.15 | 25000.00 | 1004.1 |
| 298.15 | 30000.00 | 1006.9 |
| 298.15 | 35000.00 | 1009.7 |
| 298.15 | 40000.00 | 1012.5 |
| 298.15 | 45000.00 | 1015.2 |
| 298.15 | 50000.00 | 1017.5 |
| 318.15 | 100.00 | 969.9 |
| 318.15 | 10000.00 | 977.3 |
| 318.15 | 15000.00 | 980.4 |
| 318.15 | 20000.00 | 983.6 |
| 318.15 | 25000.00 | 986.9 |
| 318.15 | 30000.00 | 989.8 |
| 318.15 | 35000.00 | 992.9 |
| 318.15 | 40000.00 | 995.7 |
| 318.15 | 45000.00 | 998.6 |
| 318.15 | 50000.00 | 1001.5 |
| 348.15 | 100.00 | 941.3 |
| 348.15 | 10000.00 | 949.8 |
| 348.15 | 15000.00 | 953.5 |
| 348.15 | 20000.00 | 957.3 |
| 348.15 | 25000.00 | 961.1 |
| 348.15 | 30000.00 | 964.5 |
| 348.15 | 35000.00 | 967.9 |
| 348.15 | 40000.00 | 971.0 |
| 348.15 | 45000.00 | 974.5 |
| 348.15 | 50000.00 | 977.8 |
| Reference | ||
Similar Compounds
Find more compounds similar to Anisole.
Mixtures
- 1,2-Ethanediol + Anisole
- Formamide, N,N-dimethyl- + Anisole
- Toluene + Anisole
- Benzene, n-butyl- + Anisole
- Phenol, 2-methoxy- + Anisole
- Carbonic acid, dimethyl ester + Anisole + Water
- Anisole + Methyl Alcohol + Water
- Anisole + Methyl Alcohol
- Carbonic acid, dimethyl ester + Anisole
- Anisole + Water
- Anisole + Phenol
- n-Hexane + Anisole
- Anisole + Heptane
- Octane + Anisole
- Anisole + Nonane
- Decane + Anisole
- Dodecane + Anisole
- Anisole + Cyclohexane, methyl-
- Benzene + Anisole
- Anisole + o-Xylene
Find more mixtures with Anisole.
Sources
- Crippen Method
- Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
- (Vapor + liquid) equilibrium of binary mixtures formed by N,N-dimethyl formamide with some compounds at 95.1 kPa
- Ternary liquid-liquid equilibrium: Nitric acid - water - anisole/4-methyl anisole
- Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
- Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
- Ternary liquid-liquid equilibria and binary excess and deviation properties at constant temperature for mixtures of dimethyl carbonate, anisole, methanol, phenol and water
- The solid-liquid equilitbrium, excess molar volume and refractive deviation properties of binary systems containing dimethyl carbonate, anisole and phenol
- Determination and correlation of solubility of 2,2',4,4',6,6 '-hexanitro-1,1'-biphenyl and 2,2',2" ,4,4',4" ,6,6',6" -Nonanitro-1,1 ':3',1"-terphenyl in six pure solvents
- Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
- Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
- Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
- Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
- Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
- (Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
- Volumetric and ultrasonic behaviour of binary mixtures of 1-nonanol with o-cresol, m-cresol, p-cresol and anisole at T = (293.15 and 313.15) K
- PVT properties for binary ionic liquids of 1-methyl-1-propylpiperidinium bis(trifluoromethylsulfonyl)imide with anisole or acetophenone at pressures up to 50 MPa
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
- P-V-T properties of binary mixtures of the ionic liquid 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide with anisole or acetophenone at elevated pressures
- Intermolecular interactions in mixtures of poly (ethylene glycol) with methoxybenzene and ethoxybenzene: Volumetric and viscometric studies
- The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
- Isobaric (vapour + liquid) equilibria of binary systems containing butyl acetate for the separation of methoxy aromatic compounds (anisole and guaiacol) from biomass fast pyrolysis oil
- The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
- Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
- Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
- Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
- Determination and Correlation of Solubility of 3,4-Dinitro-1H-pyrazole in Different Pure Solvents from 298.15 K to 338.15 K
- Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
- Isobaric Vapor-Liquid Equilibrium Data for Binary Systems of Anisole with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, and Isopropyl Acetate at 93.9 kPa
- Solubility Measurement, Modeling, and Thermodynamic Functions for para-Methoxyphenylacetic Acid in Pure and Mixed Organic and Aqueous Systems
- Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
- Liquid-Liquid Equilibrium for Ternary Systems of Water + 2,2,3,3-Tetrafluoro-1-propanol + Anisole/1-Octanol at 298.2, 308.2, and 318.2 K
- Physicochemical Properties of LiFSI Solutions II: LiFSI with Water, MTBE, and Anisole
- Experimental Determination and Modeling of Liquid-Liquid Equilibrium for Ternary Mixtures of Ethylene Glycol + 1,2-Butanediol + 3-Heptanone or Anisole
- Vapor-Liquid Equilibria of the Binary System 1-Pentanol + Anisole and the Quaternary System Benzene+Cyclohexane+1-Pentanol+Anisole at 101.32 kPa
- Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
- Enthalpies of Mixing, Densities, and Refractive Indices for Binary Mixtures of (Anisole or Phenetole) + Three Aryl Alcohols at 308.15 K and at Atmospheric Pressure
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
- Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
- Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
- Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
- Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
- Liquid Liquid Equilibria for Ternary Mixtures of Methylphenyl Carbonate, Dimethyl Carbonate, Diphenyl Carbonate, Anisole, Methanol, Phenol, and Water at Several Temperatures
- Isobaric Vapor Liquid Equilibria of the Ternary System 1-Pentanol + Nonane Anisole
- Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Anisole
- Joback Method
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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