- InChI
- InChI=1S/C8H10O/c1-7-3-5-8(9-2)6-4-7/h3-6H,1-2H3
- InChI Key
- CHLICZRVGGXEOD-UHFFFAOYSA-N
- Formula
- C8H10O
- SMILES
- COc1ccc(C)cc1
- Molecular Weight1
- 122.16
- CAS
- 104-93-8
- Other Names
-
- 1-Methyl-4-methoxybenzene
- 1-methoxy-4-methylbenzene
- 4-Methyl-1-methoxybenzene
- 4-Methylmethoxybenzene
- 4-Methylphenol methyl ether
- 4-methoxymethylbenzene
- 4-methoxytoluene
- 4-methylanisole
- Methyl 4-methylphenyl ether
- Methyl p-cresyl ether
- NSC 6254
- anisole, p-methyl-
- methyl 4-tolyl ether
- methyl p-methylphenyl ether
- methyl p-tolyl ether
- p-Cresyl methyl ether
- p-Methylanisol
- p-cresol methyl ether
- p-methoxytoluene
- p-methylanisole
- p-tolyl methyl ether
- para-Methyl anisol
- para-Methyl anisole
- toluene, 4-methoxy-
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (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).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- 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 | 841.00 ± 8.00 | kJ/mol | NIST |
| BasG | 809.00 ± 8.00 | kJ/mol | NIST |
| ΔfG° | 14.26 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -115.61 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 11.32 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 38.75 | kJ/mol | Joback Calculated Property |
| IE | [7.83; 8.30] | eV |
|
| IE | 7.90 ± 0.05 | eV | NIST |
| IE | 7.90 ± 0.03 | eV | NIST |
| IE | 7.85 | eV | NIST |
| IE | 7.91 | eV | NIST |
| IE | 7.83 | eV | NIST |
| IE | 8.30 ± 0.10 | eV | NIST |
| IE | 8.00 ± 0.15 | eV | NIST |
| IE | 8.14 ± 0.01 | eV | NIST |
| IE | 8.18 | eV | NIST |
| IE | 8.17 | eV | NIST |
| IE | 8.16 | eV | NIST |
| log10WS | -2.07 | Crippen Calculated Property | |
| logPoct/wat | 2.004 | Crippen Calculated Property | |
| McVol | 105.690 | ml/mol | McGowan Calculated Property |
| Pc | 3513.74 | kPa | Joback Calculated Property |
| Inp | [986.60; 1036.00] |
|
|
| Inp | 986.60 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1029.50 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 999.20 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1016.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1001.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 986.60 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 999.20 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1029.50 | NIST | |
| I | [1409.00; 1461.10] |
|
|
| I | 1461.00 | NIST | |
| I | 1461.10 | NIST | |
| I | 1446.00 | NIST | |
| I | 1434.00 | NIST | |
| I | 1430.00 | NIST | |
| I | 1446.00 | NIST | |
| I | 1441.00 | NIST | |
| I | 1409.00 | NIST | |
| I | 1432.00 | NIST | |
| I | 1415.00 | NIST | |
| I | 1432.00 | NIST | |
| I | 1430.00 | NIST | |
| Tboil | [443.75; 450.90] | K |
|
| Tboil | 447.20 | K | NIST |
| Tboil | 450.90 ± 3.00 | K | NIST |
| Tboil | 449.90 ± 0.50 | K | NIST |
| Tboil | 449.70 ± 0.20 | K | NIST |
| Tboil | 443.75 ± 0.50 | K | NIST |
| Tc | 666.00 ± 1.00 | K | NIST |
| Tfus | [241.10; 241.96] | K |
|
| Tfus | 241.10 ± 0.30 | K | NIST |
| Tfus | 241.96 ± 0.30 | K | NIST |
| Vc | 0.394 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [199.01; 262.44] | J/mol×K | [436.52; 646.36] |
|
| Cp,gas | 199.01 | J/mol×K | 436.52 | Joback Calculated Property |
| Cp,gas | 210.91 | J/mol×K | 471.49 | Joback Calculated Property |
| Cp,gas | 222.27 | J/mol×K | 506.47 | Joback Calculated Property |
| Cp,gas | 233.10 | J/mol×K | 541.44 | Joback Calculated Property |
| Cp,gas | 243.40 | J/mol×K | 576.41 | Joback Calculated Property |
| Cp,gas | 253.17 | J/mol×K | 611.38 | Joback Calculated Property |
| Cp,gas | 262.44 | J/mol×K | 646.36 | Joback Calculated Property |
| η | [0.0001977; 0.0017292] | Pa×s | [241.09; 436.52] |
|
| η | 0.0017292 | Pa×s | 241.09 | Joback Calculated Property |
| η | 0.0009715 | Pa×s | 273.66 | Joback Calculated Property |
| η | 0.0006170 | Pa×s | 306.23 | Joback Calculated Property |
| η | 0.0004276 | Pa×s | 338.81 | Joback Calculated Property |
| η | 0.0003160 | Pa×s | 371.38 | Joback Calculated Property |
| η | 0.0002453 | Pa×s | 403.95 | Joback Calculated Property |
| η | 0.0001977 | Pa×s | 436.52 | Joback Calculated Property |
| Pvap | [0.03; 0.34] | kPa | [275.20; 308.00] |
|
| Pvap | 0.03 | kPa | 275.20 | Benchma... |
| Pvap | 0.03 | kPa | 276.40 | Benchma... |
| Pvap | 0.03 | kPa | 277.20 | Benchma... |
| Pvap | 0.04 | kPa | 278.80 | Benchma... |
| Pvap | 0.05 | kPa | 281.70 | Benchma... |
| Pvap | 0.06 | kPa | 284.80 | Benchma... |
| Pvap | 0.08 | kPa | 287.50 | Benchma... |
| Pvap | 0.09 | kPa | 289.20 | Benchma... |
| Pvap | 0.10 | kPa | 290.40 | Benchma... |
| Pvap | 0.10 | kPa | 291.20 | Benchma... |
| Pvap | 0.10 | kPa | 291.30 | Benchma... |
| Pvap | 0.13 | kPa | 294.20 | Benchma... |
| Pvap | 0.14 | kPa | 296.20 | Benchma... |
| Pvap | 0.16 | kPa | 297.10 | Benchma... |
| Pvap | 0.18 | kPa | 299.20 | Benchma... |
| Pvap | 0.19 | kPa | 300.10 | Benchma... |
| Pvap | 0.20 | kPa | 300.10 | Benchma... |
| Pvap | 0.21 | kPa | 301.10 | Benchma... |
| Pvap | 0.25 | kPa | 303.10 | Benchma... |
| Pvap | 0.28 | kPa | 305.00 | Benchma... |
| Pvap | 0.34 | kPa | 308.00 | Benchma... |
Similar Compounds
Find more compounds similar to Benzene, 1-methoxy-4-methyl-.
Mixtures
Sources
- Crippen Method
- Crippen Method
- Ternary liquid-liquid equilibrium: Nitric acid - water - anisole/4-methyl anisole
- Benchmark thermodynamic properties of methylanisoles: Experimental and theoretical study
- Joback Method
- McGowan Method
- NIST Webbook
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