- InChI
- InChI=1S/C3H6O2/c1-3(4)5-2/h1-2H3
- InChI Key
- KXKVLQRXCPHEJC-UHFFFAOYSA-N
- Formula
- C3H6O2
- SMILES
- COC(C)=O
- Molecular Weight1
- 74.08
- CAS
- 79-20-9
- Other Names
-
- Acetate de methyle
- CH3COOCH3
- DEVOTON
- Ethyl ester of monoacetic acid
- METHYL ACETIC ESTER
- METHYL ETHANOATE
- Methyl acetate
- Methyl ester of acetic acid
- Methylacetaat
- Methylacetat
- Methyle (acetate de)
- Methylester kiseliny octove
- Metile (acetato di)
- NSC 405071
- Tereton
- UN 1231
- ethanoic acid, methyl ester
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- 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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- 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.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3260 | KDB | |
| PAff | 821.60 | kJ/mol | NIST |
| Tig | 774.82 | K | KDB |
| BasG | 790.70 | kJ/mol | NIST |
| ΔcH°liquid | [-1592.20; -1583.00] | kJ/mol |
|
| ΔcH°liquid | -1583.00 | kJ/mol | NIST |
| ΔcH°liquid | -1592.20 ± 0.67 | kJ/mol | NIST |
| μ | 1.70 | debye | KDB |
| η | [0.0003711; 0.0004000] | Pa×s |
|
| η | 0.0003711 | Pa×s | Densiti... |
| η | 0.0004000 | Pa×s | Densiti... |
| η | 0.0003800 | Pa×s | Densiti... |
| LFL | 3.10 | % in Air | KDB |
| UFL | 16.00 | % in Air | KDB |
| Tflash,cc | 267.59 | K | KDB |
| Tflash,oc | 263.15 | K | KDB |
| ΔfG° | -259.54 | kJ/mol | Joback Calculated Property |
| Rg | 2.8620 | KDB | |
| ΔfH°gas | [-410.00; -409.70] | kJ/mol |
|
| ΔfH°gas | -409.70 | kJ/mol | KDB |
| ΔfH°gas | -410.00 | kJ/mol | NIST |
| ΔfH°liquid | -445.89 | kJ/mol | NIST |
| ΔfusH° | 6.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 31.43 | kJ/mol | Joback Calculated Property |
| IE | [10.20; 11.00] | eV |
|
| IE | 10.25 ± 0.02 | eV | NIST |
| IE | 10.20 | eV | NIST |
| IE | 10.25 | eV | NIST |
| IE | 10.25 ± 0.05 | eV | NIST |
| IE | 10.33 | eV | NIST |
| IE | 10.27 ± 0.02 | eV | NIST |
| IE | 10.50 | eV | NIST |
| IE | 10.25 | eV | NIST |
| IE | Outlier 11.00 | eV | NIST |
| IE | 10.59 | eV | NIST |
| log10WS | [0.46; 0.52] |
|
|
| log10WS | 0.52 | Aq. Sol... | |
| log10WS | 0.46 | Estimat... | |
| logPoct/wat | 0.179 | Crippen Calculated Property | |
| McVol | 60.570 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [4694.00; 5840.00] | kPa |
|
| Pc | 4750.00 | kPa | KDB |
| Pc | 4750.00 ± 4.74 | kPa | NIST |
| Pc | 4694.00 ± 81.06 | kPa | NIST |
| Pc | 4694.30 ± 40.00 | kPa | NIST |
| Pc | 4817.00 ± 101.32 | kPa | NIST |
| Pc | Outlier 5840.00 ± 607.95 | kPa | NIST |
| ρc | [320.02; 325.50] | kg/m3 |
|
| ρc | 325.50 ± 3.70 | kg/m3 | NIST |
| ρc | 320.02 ± 5.93 | kg/m3 | NIST |
| Inp | [501.15; 560.00] |
|
|
| Inp | 501.15 | NIST | |
| Inp | 522.17 | NIST | |
| Inp | 520.60 | NIST | |
| Inp | 521.00 | NIST | |
| Inp | 526.20 | NIST | |
| Inp | 521.30 | NIST | |
| Inp | 515.70 | NIST | |
| Inp | 513.80 | NIST | |
| Inp | 511.50 | NIST | |
| Inp | 529.70 | NIST | |
| Inp | 525.70 | NIST | |
| Inp | 523.70 | NIST | |
| Inp | 530.00 | NIST | |
| Inp | 525.70 | NIST | |
| Inp | 522.40 | NIST | |
| Inp | 505.00 | NIST | |
| Inp | 505.00 | NIST | |
| Inp | 505.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | 505.00 | NIST | |
| Inp | 529.00 | NIST | |
| Inp | Outlier 560.00 | NIST | |
| Inp | 525.90 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | 505.00 | NIST | |
| Inp | 506.00 | NIST | |
| Inp | 510.00 | NIST | |
| Inp | 531.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | 522.00 | NIST | |
| Inp | 531.00 | NIST | |
| Inp | 517.20 | NIST | |
| Inp | 526.30 | NIST | |
| Inp | 506.00 | NIST | |
| Inp | 511.00 | NIST | |
| Inp | 511.00 | NIST | |
| Inp | 521.30 | NIST | |
| Inp | 516.70 | NIST | |
| Inp | 536.00 | NIST | |
| Inp | 515.00 | NIST | |
| Inp | Outlier 559.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 513.00 | NIST | |
| Inp | 513.00 | NIST | |
| Inp | 510.00 | NIST | |
| Inp | 511.00 | NIST | |
| Inp | 507.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 515.00 | NIST | |
| Inp | 524.00 | NIST | |
| Inp | 515.30 | NIST | |
| Inp | 525.00 | NIST | |
| Inp | 511.00 | NIST | |
| Inp | 515.00 | NIST | |
| Inp | 513.00 | NIST | |
| Inp | 519.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | 531.00 | NIST | |
| Inp | 528.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | 525.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | Outlier 559.00 | NIST | |
| Inp | 523.00 | NIST | |
| Inp | 513.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | 530.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 510.00 | NIST | |
| Inp | 507.00 | NIST | |
| Inp | 512.00 | NIST | |
| Inp | 513.00 | NIST | |
| Inp | 524.00 | NIST | |
| Inp | 508.00 | NIST | |
| Inp | 508.00 | NIST | |
| Inp | 519.00 | NIST | |
| Inp | 513.00 | NIST | |
| I | [782.00; 877.00] |
|
|
| I | 844.00 | NIST | |
| I | Outlier 877.00 | NIST | |
| I | 823.00 | NIST | |
| I | 839.00 | NIST | |
| I | 850.00 | NIST | |
| I | 836.00 | NIST | |
| I | 832.00 | NIST | |
| I | 810.00 | NIST | |
| I | 827.00 | NIST | |
| I | 828.00 | NIST | |
| I | 798.00 | NIST | |
| I | 839.00 | NIST | |
| I | 826.00 | NIST | |
| I | Outlier 864.00 | NIST | |
| I | 832.80 | NIST | |
| I | 801.00 | NIST | |
| I | 834.00 | NIST | |
| I | 825.00 | NIST | |
| I | 829.00 | NIST | |
| I | 827.00 | NIST | |
| I | 817.00 | NIST | |
| I | 825.00 | NIST | |
| I | 828.00 | NIST | |
| I | 825.00 | NIST | |
| I | 848.00 | NIST | |
| I | 818.00 | NIST | |
| I | 843.00 | NIST | |
| I | 828.00 | NIST | |
| I | 813.00 | NIST | |
| I | 832.00 | NIST | |
| I | 828.00 | NIST | |
| I | 826.00 | NIST | |
| I | Outlier 782.00 | NIST | |
| I | 856.00 | NIST | |
| I | 822.00 | NIST | |
| I | Outlier 782.00 | NIST | |
| I | Outlier 782.00 | NIST | |
| I | 825.00 | NIST | |
| I | 827.00 | NIST | |
| I | 837.00 | NIST | |
| I | 845.00 | NIST | |
| I | 825.00 | NIST | |
| I | 825.00 | NIST | |
| I | 828.00 | NIST | |
| I | Outlier 784.00 | NIST | |
| I | 834.00 | NIST | |
| I | 854.00 | NIST | |
| I | 826.00 | NIST | |
| I | 827.00 | NIST | |
| I | 813.00 | NIST | |
| I | 834.00 | NIST | |
| I | 804.00 | NIST | |
| I | 834.00 | NIST | |
| I | 834.00 | NIST | |
| I | 813.00 | NIST | |
| I | 834.00 | NIST | |
| I | 841.00 | NIST | |
| I | 841.00 | NIST | |
| I | 827.00 | NIST | |
| I | 796.00 | NIST | |
| Tboil | [329.85; 330.95] | K |
|
| Tboil | 330.02 | K | KDB |
| Tboil | 330.04 | K | Volumet... |
| Tboil | 330.05 | K | Multiph... |
| Tboil | Outlier 330.95 | K | Isobari... |
| Tboil | 330.40 | K | Isobari... |
| Tboil | 330.02 | K | Experim... |
| Tboil | 330.05 | K | Isobari... |
| Tboil | 330.20 | K | Isobari... |
| Tboil | 329.85 | K | Isobari... |
| Tboil | 329.97 | K | Vapor-L... |
| Tboil | 329.95 | K | Experim... |
| Tc | 506.55 | K | KDB |
| Tfus | [175.00; 175.15] | K |
|
| Tfus | 175.00 | K | KDB |
| Tfus | 175.15 ± 0.30 | K | NIST |
| Tfus | 175.10 ± 0.20 | K | NIST |
| Ttriple | 174.90 ± 0.01 | K | NIST |
| Vc | 0.228 | m3/kmol | KDB |
| Zc | 0.2571400 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [92.58; 114.63] | J/mol×K | [335.00; 450.00] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 95 100 105 110 115 350 400 450 | ||||
| Cp,gas | 92.58 | J/mol×K | 335.00 | NIST |
| Cp,gas | 95.46 | J/mol×K | 350.00 | NIST |
| Cp,gas | 100.39 | J/mol×K | 375.00 | NIST |
| Cp,gas | 105.31 | J/mol×K | 400.00 | NIST |
| Cp,gas | 109.98 | J/mol×K | 425.00 | NIST |
| Cp,gas | 114.63 | J/mol×K | 450.00 | NIST |
| Cp,liquid | [123.70; 141.34] | J/mol×K | [288.58; 298.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 125 130 135 140 290 295 | ||||
| Cp,liquid | 140.20 | J/mol×K | 288.58 | NIST |
| Cp,liquid | 123.70 | J/mol×K | 297.00 | NIST |
| Cp,liquid | 141.34 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 140.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 140.56 | J/mol×K | 298.15 | NIST |
| η | [0.0003480; 0.0003860] | Pa×s | [293.15; 308.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 3.50e-4 3.60e-4 3.70e-4 3.80e-4 295 300 305 | ||||
| η | 0.0003860 | Pa×s | 293.15 | Density... |
| η | 0.0003860 | Pa×s | 293.15 | Dynamic... |
| η | 0.0003670 | Pa×s | 298.15 | Density... |
| η | 0.0003840 | Pa×s | 298.15 | Densiti... |
| η | 0.0003670 | Pa×s | 298.15 | Dynamic... |
| η | 0.0003480 | Pa×s | 303.15 | Density... |
| η | 0.0003480 | Pa×s | 303.15 | Dynamic... |
| η | 0.0003510 | Pa×s | 308.15 | Densiti... |
| ΔfusH | [7.49; 7.49] | kJ/mol | [174.90; 174.90] |
|
| ΔfusH | 7.49 | kJ/mol | 174.90 | NIST |
| ΔfusH | 7.49 | kJ/mol | 174.90 | NIST |
| ΔfusH | 7.49 | kJ/mol | 174.90 | NIST |
| ΔvapH | [29.50; 34.50] | kJ/mol | [295.00; 343.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 29 30 31 32 33 34 300 320 340 | ||||
| ΔvapH | 32.50 | kJ/mol | 295.00 | NIST |
| ΔvapH | 34.50 | kJ/mol | 295.50 | NIST |
| ΔvapH | 33.40 | kJ/mol | 301.50 | NIST |
| ΔvapH | 32.20 ± 0.10 | kJ/mol | 304.00 | NIST |
| ΔvapH | 34.10 | kJ/mol | 305.50 | NIST |
| ΔvapH | 31.60 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 31.80 | kJ/mol | 323.00 | NIST |
| ΔvapH | 30.50 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 30.20 | kJ/mol | 330.00 | NIST |
| ΔvapH | 30.32 | kJ/mol | 330.10 | NIST |
| ΔvapH | 30.30 ± 0.10 | kJ/mol | 331.00 | NIST |
| ΔvapH | 29.50 ± 0.10 | kJ/mol | 343.00 | NIST |
| Pvap | [37.14; 1500.00] | kPa | [304.00; 436.08] |
|
|
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 1400 1600 350 400 | ||||
| Pvap | 37.14 | kPa | 304.00 | Isobari... |
| Pvap | 40.40 | kPa | 306.00 | Isobari... |
| Pvap | 43.89 | kPa | 308.00 | Isobari... |
| Pvap | 47.62 | kPa | 310.00 | Isobari... |
| Pvap | 51.60 | kPa | 312.00 | Isobari... |
| Pvap | 53.81 | kPa | 313.15 | Total V... |
| Pvap | 55.85 | kPa | 314.00 | Isobari... |
| Pvap | 60.38 | kPa | 316.00 | Isobari... |
| Pvap | 65.21 | kPa | 318.00 | Isobari... |
| Pvap | 70.34 | kPa | 320.00 | Isobari... |
| Pvap | 75.79 | kPa | 322.00 | Isobari... |
| Pvap | 79.21 | kPa | 323.15 | Isother... |
| Pvap | 81.58 | kPa | 324.00 | Isobari... |
| Pvap | 87.72 | kPa | 326.00 | Isobari... |
| Pvap | 94.23 | kPa | 328.00 | Isobari... |
| Pvap | 101.33 | kPa | 329.95 | Experim... |
| Pvap | 101.30 | kPa | 329.97 | Vapor-L... |
| Pvap | 101.12 | kPa | 330.00 | Isobari... |
| Pvap | 101.30 | kPa | 330.05 | Multiph... |
| Pvap | 108.41 | kPa | 332.00 | Isobari... |
| Pvap | 116.11 | kPa | 334.00 | Isobari... |
| Pvap | 124.25 | kPa | 336.00 | Isobari... |
| Pvap | 132.83 | kPa | 338.00 | Isobari... |
| Pvap | 600.00 | kPa | 393.01 | Experim... |
| Pvap | 1500.00 | kPa | 436.08 | Measure... |
| n0 | [1.34823; 1.36500] | [288.15; 318.15] |
|
|
|
T(K) Refractive Index 1.35 1.36 1.36 1.37 290 300 310 | ||||
| n0 | 1.36500 | 288.15 | Density... | |
| n0 | 1.36414 | 288.15 | Density... | |
| n0 | 1.35865 | 298.15 | Density... | |
| n0 | 1.35881 | 298.15 | Propert... | |
| n0 | 1.35850 | 298.15 | Molecul... | |
| n0 | 1.35850 | 298.15 | Thermod... | |
| n0 | 1.35893 | 298.15 | Densiti... | |
| n0 | 1.35881 | 298.15 | Density... | |
| n0 | 1.35890 | 298.15 | Vapor-l... | |
| n0 | 1.35880 | 298.15 | A Study... | |
| n0 | 1.35872 | 298.15 | Vapor-L... | |
| n0 | 1.36146 | 298.15 | Isobari... | |
| n0 | 1.35870 | 298.15 | Isobari... | |
| n0 | 1.35875 | 298.15 | Measure... | |
| n0 | 1.35893 | 298.15 | Isobari... | |
| n0 | 1.35906 | 298.15 | Excess ... | |
| n0 | 1.35670 | 303.15 | Densiti... | |
| n0 | 1.35367 | 308.15 | Density... | |
| n0 | 1.34860 | 318.15 | Excess ... | |
| n0 | 1.34900 | 318.15 | Thermod... | |
| n0 | 1.34823 | 318.15 | Density... | |
| ρl | [907.90; 935.01] | kg/m3 | [293.00; 313.15] |
|
|
T(K) Liquid Density (kg/m3) 910 915 920 925 930 935 295 300 305 310 | ||||
| ρl | 934.00 | kg/m3 | 293.00 | KDB |
| ρl | 935.01 | kg/m3 | 293.15 | Volumet... |
| ρl | 927.50 | kg/m3 | 298.15 | Isobari... |
| ρl | 927.30 | kg/m3 | 298.15 | Isobari... |
| ρl | 927.10 | kg/m3 | 298.15 | Vapor-l... |
| ρl | 926.90 | kg/m3 | 298.15 | Densiti... |
| ρl | 927.70 | kg/m3 | 298.15 | Liquid ... |
| ρl | 927.30 | kg/m3 | 298.15 | Experim... |
| ρl | 927.10 | kg/m3 | 298.15 | Ternary... |
| ρl | 928.46 | kg/m3 | 298.15 | Volumet... |
| ρl | 921.85 | kg/m3 | 303.15 | Volumet... |
| ρl | 920.50 | kg/m3 | 303.15 | Ternary... |
| ρl | 915.16 | kg/m3 | 308.15 | Volumet... |
| ρl | 908.49 | kg/m3 | 313.15 | Volumet... |
| ρl | 907.90 | kg/m3 | 313.15 | Ternary... |
| csound,fluid | [1110.02; 1200.38] | m/s | [288.15; 308.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1120 1140 1160 1180 1200 290 295 300 305 | ||||
| csound,fluid | 1200.38 | m/s | 288.15 | Densiti... |
| csound,fluid | 1178.95 | m/s | 293.15 | Densiti... |
| csound,fluid | 1155.93 | m/s | 298.15 | Densiti... |
| csound,fluid | 1132.98 | m/s | 303.15 | Densiti... |
| csound,fluid | 1110.02 | m/s | 308.15 | Densiti... |
| γ | 0.02 | N/m | 298.15 | Surface... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 4701.97] | kPa | [243.21; 506.55] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.47592e+01 | |||
| Coefficient B | -2.94089e+03 | |||
| Coefficient C | -3.99950e+01 | |||
| Temperature range, min. | 243.21 | |||
| Temperature range, max. | 506.55 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 | ||||
| Pvap | 1.33 | kPa | 243.21 | Calculated Property |
| Pvap | 8.24 | kPa | 272.47 | Calculated Property |
| Pvap | 33.89 | kPa | 301.73 | Calculated Property |
| Pvap | 104.88 | kPa | 330.99 | Calculated Property |
| Pvap | 264.06 | kPa | 360.25 | Calculated Property |
| Pvap | 569.61 | kPa | 389.51 | Calculated Property |
| Pvap | 1091.09 | kPa | 418.77 | Calculated Property |
| Pvap | 1903.99 | kPa | 448.03 | Calculated Property |
| Pvap | 3083.95 | kPa | 477.29 | Calculated Property |
| Pvap | 4701.97 | kPa | 506.55 | Calculated Property |
| Pvap | [9.06e-04; 4664.54] | kPa | [175.15; 506.80] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.85873e+01 | |||
| Coefficient B | -6.36277e+03 | |||
| Coefficient C | -9.58632e+00 | |||
| Coefficient D | 8.25370e-06 | |||
| Temperature range, min. | 175.15 | |||
| Temperature range, max. | 506.80 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 200 300 400 500 | ||||
| Pvap | 9.06e-04 | kPa | 175.15 | Calculated Property |
| Pvap | 0.09 | kPa | 212.00 | Calculated Property |
| Pvap | 1.90 | kPa | 248.85 | Calculated Property |
| Pvap | 16.12 | kPa | 285.70 | Calculated Property |
| Pvap | 77.21 | kPa | 322.55 | Calculated Property |
| Pvap | 254.55 | kPa | 359.40 | Calculated Property |
| Pvap | 651.98 | kPa | 396.25 | Calculated Property |
| Pvap | 1402.54 | kPa | 433.10 | Calculated Property |
| Pvap | 2670.14 | kPa | 469.95 | Calculated Property |
| Pvap | 4664.54 | kPa | 506.80 | Calculated Property |
Similar Compounds
Find more compounds similar to Acetic acid, methyl ester.
Mixtures
- 1-Propanol + Acetic acid, methyl ester
- 1-Butanol + Acetic acid, methyl ester
- Heptane + Acetic acid, methyl ester
- n-Hexane + Acetic acid, methyl ester
- Decane + Acetic acid, methyl ester
- Acetic acid, methyl ester + Methyl Alcohol
- Acetic acid, methyl ester + Water
- Acetic acid + Acetic acid, methyl ester
- Carbon dioxide + Acetic acid, methyl ester
- Acetic acid, methyl ester + Propanoic acid
- Methyl propionate + Acetic acid, methyl ester
- Methyl propionate + Acetic acid, methyl ester + Water
- Acetic acid, methyl ester + Simvastatin
- Propane, 1,2-dichloro- + Acetic acid, methyl ester
- Isopropyl acetate + Acetic acid, methyl ester
- Dimethyl sulfide + Acetic acid, methyl ester
- Acetic acid, methyl ester + 2-Propanol, 1-methoxy-
- Acetic acid, methyl ester + Phosphoramidic acid, phenyl-, diphenyl ester
- Dimethyl Sulfoxide + Acetic acid, methyl ester
- Dimethyl Sulfoxide + Acetic acid, methyl ester + Methyl Alcohol
Find more mixtures with Acetic acid, methyl ester.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Experimental Determination of Densities and Isobaric Vapor Liquid Equilibria of Methyl Acetate and Ethyl Acetate with Alcohols (C3 and C4) at 0.3 MPa
- Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
- (Liquid + liquid) equilibria of (water + 1-propanol + solvent) at T = 298.2K
- Isothermal vapour liquid equilibrium with chemical reaction in the quaternary water + methanol + acetic acid + methyl acetate system, and in five binary subsystems
- Volumetric property for carbon dioxide + methyl acetate system at 313.15K
- Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
- Multiphase equilibria for mixtures containing water, acetic acid, propionic acid, methyl acetate and methyl propionate
- Solubility and limiting activity coefficient of simvastatin in different organic solvents
- Experimental measurements of vapor liquid equilibria at low pressure: Systems containing alcohols, esters and organic acids
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Excess molar volumes and excess molar enthalpies for binary mixtures of 1,2-dichloropropane with methyl ethanoate, methyl propanoate, and methyl butanoate at T = 298.15K
- Vapor-liquid equilibria of ternary systems with 1-ethyl-3-methylimidazolium ethyl sulfate using headspace gas chromatography
- Isobaric vapor-liquid equilibrium data for the binary system methyl acetate + isopropyl acetate and the quaternary system methyl acetate + methanol + isopropanol + isopropyl acetate at 101.3 kPa
- Vapor-liquid equilibrium measurements of dimethylsulfide, +ethanol, +dimethylether, +methylacetate with a static total pressure method
- Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
- Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
- Measurement and correlation of the solubilities of tetra(5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy) neopentane in different pure solvents
- Effect of bivalent cation inorganic salts on isobaric vapor-liquidequilibrium of methyl acetate - methanol system
- Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
- Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
- Measurement and correlation of solubility of D-camphor-10-sulfonic acid in pure solvents
- Separation of methyl acetate + methanol azeotropic mixture using ionic liquids as entrainers
- Isobaric vapor-liquid equilibrium of the binary system sec-butyl acetate + para-xylene and the quaternary system methyl acetate + para-xylene + sec-butyl acetate + acetic acid at 101.3 kPa
- Isobaric vapor-liquid equilibrium for methyl acetate + methanol system containing different ionic liquids at 101.3 kPa
- Solution thermodynamics of simvastatin in pure solvents and binary solvent mixtures
- Experimental isobaric vapor-liquid equilibrium for the binary and ternary systems with methanol, methyl acetate and dimethyl sulfoxide at 101.3 kPa
- Vapor-liquid equilibria of binary and ternary mixtures containing ethyl lactate and effect of ethyl lactate as entrainer
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Solubility and mixing thermodynamic properties of (2,4,6-trimethylbenzoyl) diphenylphosphine oxide in pure and binary solvents
- Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
- Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
- Isobaric vapor-liquid equilibrium for methanol + methyl acetate with ionic liquids [OMMIM][Tf2N] and [OMIM][Tf2N] as entrainers at 101.3 kPa
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
- Liquid--liquid equilibria for mixtures of {methyl acetate + methanol + n-alkane (C10--C12)} at several temperatures and 1 atm
- Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
- Molecular interactions in (2,4,6-trimethyl-1,3,5-trioxane + n-alkyl acetates) at T=(298.15, 303.15, and 308.15) K
- Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
- Densities, speeds of sound, and refractive indices of the ternary mixtures (toluene + methyl acetate + butyl acetate) and (toluene + methyl acetate + methyl heptanoate) at 298.15 K
- Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
- Physical and excess properties of (methyl acetate + methanol + 1-octyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide) and its binary mixtures at T = 298.15 K and atmospheric pressure
- Ternary excess molar volumes of {methyltrioctylammonium bis(trifluoromethylsulfonyl)imide + ethanol + methyl acetate, or ethyl acetate} systems at T = (298.15, 303.15, and 313.15) K
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Density, refraction index and vapor-liquid equilibria of N-methyl-2-hydroxyethylammonium butyrate plus (methyl acetate or ethyl acetate or propyl acetate) at several temperatures
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Thermodynamics of 4'-bromomethyl-2-cyanobiphenyl in different solvents
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Solid-liquid phase equilibrium and mixing properties of 2-Cyano-4'-methylbiphenyl in pure solvents
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Solubility measurement, model evaluation and thermodynamic analysis of rivaroxaban polymorphs in organic solvents
- Solid-liquid phase equilibrium and dissolution properties of ethyl vanillin in pure solvents
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Densities and interfacial tensions for fatty acid methyl esters (from methyl formate to methyl heptanoate) + water demixed mixtures at atmospheric pressure conditions
- Ternary liquid-liquid equilibria for systems containing (dimethyl carbonate or methyl acetate + methanol + 1-methylmidazole hydrogen sulfate) at 298.15 K and 318.15 K
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
- Studies on liquid liquid interactions of some ternary mixtures by density, viscosity, ultrasonic speed and refractive index measurements
- Effects of temperature and concentration on interactions in (methanol + ethyl acetate) and (ethanol + methyl acetate or ethyl acetate) systems: insights from apparent molar volume and apparent molar isentropic compressibility study
- Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
- Solubility of Amorphous Clopidogrel Hydrogen Sulfate in Different Pure Solvents
- Solubilities of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Different Pure Solvents
- Solubility of Agomelatine Crystal Form I and Form II in Pure Solvents and (Isopropanol + Water) Mixtures
- Measurement and Correlation of the Solubility of Vanillic Acid in Eight Pure and Water + Ethanol Mixed Solvents at Temperatures from (293.15 to 323.15) K
- Measurement and modeling of high pressure VLE for methyl acetate or ethyl acetate with 2-butanol. Isobaric data at 1.5 MPa
- A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
- Differential Scanning Calorimetry Data and Solubility of Rosmarinic Acid in Different Pure Solvents and in Binary Mixtures (Methyl Acetate + Water) and (Ethyl Acetate + Water) from 293.2 to 313.2 K
- Measurement and Correlation of the Solubility of p-Coumaric Acid in Nine Pure and Water + Ethanol Mixed Solvents at Temperatures from 293.15 to 333.15 K
- Measurement and Correlation of Solubility on Reactive Crystallization of Methyl D-(-)-4-Hydroxy-phenylglycinate
- Solubilities of Three Flavonoids in Different Natural Deep Eutectic Solvents at T = (288.15 to 328.15) K
- Determination of Vapor Liquid Equilibrium of Methyl Acetate + Methanol + 1-Alkyl-3-methylimidazolium Dialkylphosphates at 101.3 kPa
- Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
- Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
- Determination and Correlation of Solubility and Thermodynamic Properties of trans-Cinnamyl Alcohol in Pure and Binary Solvents from 253.15 K to 293.15 K
- Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
- Vapor-Liquid Equilibrium Data for Binary Mixtures of Dimethyl Carbonate with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, Isopropyl Acetate, n-Butyl Acetate, and Isoamyl Acetate at 93.13 kPa
- Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
- Solution Thermodynamics of Benzotriazole in Different Pure Solvents
- Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
- 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
- Determination of Solubility and Thermodynamic Properties of Benzophenone in Different Pure Solvents
- Thermodynamic Study of Solubility for Imatinib Mesylate in Nine Monosolvents and Two Binary Solvent Mixtures from 278.15 to 318.15 K
- Solubility Determination of Nicotinamide and Its Application for the Cocrystallization with Benzoic Acid
- Measurement and Correlation of Solubility of 3-Hydroxy-2-naphthoic Acid in Ten Pure and Binary Mixed Organic Solvents from T = (293.15 to 333.15 K)
- Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
- Measurement and Correlation of Solubility and Thermodynamic Properties of Vinpocetine in Nine Pure Solvents and (Ethanol + Water) Binary Solvent
- Solubility Determination and Correlation of Glibenclamide in 11 Monosolvents and (Acetone + Acetonitrile) Binary Solvents from 283.15 K to 323.15 K
- Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) K
- Isobaric Vapor-Liquid Equilibrium Measurements for Separation of Azeotrope (Methanol + Methyl Acetate)
- Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
- Measurement and Correlation of the Solubility of Tetramethylpyrazine in Nine Monosolvents and Two Binary Solvent Systems
- Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
- Determination and Modeling of Solubility of 4-Aminobenzamide in Different Pure Solvents
- Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
- Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa
- Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
- Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
- Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
- Measurement and Correlation of the Solubility of Aminocaproic Acid in Some Pure and Binary Solvents
- Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
- Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
- Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
- Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
- Isobaric Vapor-Liquid Equilibria and Excess Properties for the Binary Systems of Methyl Esters + Heptane
- Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
- Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
- Liquid-Liquid Equilibria of Methyl Acetate + Methanol + Octane or Nonane
- Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
- Excess Properties and Isobaric Vapor-Liquid Equilibria for Binary Mixtures of Methyl Esters + tert-Butanol
- Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
- Excess Molar Enthalpies of Methyl Acetate and (1-Propanol, 2-Propanol, 1-Butanol, 2-Butanol, and 1-Pentanol) at T = (298.15 and 308.15) K and P = (5.0 and 10.0) MPa
- Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + Ethyl Lactate and Methyl Acetate + Ethyl Lactate
- Solubility of 1H-1,2,4-Triazole in Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, Ethyl Formate, Methyl Acetate, Ethyl Acetate, and Butyl Acetate at (283 to 363) K
- Solubility of 3-Nitrophthalic Acid in Different Solvents between 278 K and 353 K
- Liquid-Liquid Equilibrium of Ternary and Quaternary Systems Including Methyl Acetate, Benzene, Toluene, and Water at 283.2 K under Atmosphere
- Vapor-Liquid Equilibrium and Liquid-Liquid Equilibrium of Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Acetate
- Critical Assessment of CO2 Solubility in Volatile Solvents at 298.15 K
- Article Isobaric Vapor Liquid Equilibrium for Methanol + Methyl Acetate + 1-Octyl-3-methylimidazolium Hexafluorophosphate at 101.3 kPa
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Solubility of Veratric Acid in Eight Monosolvents and Ethanol + 1-Butanol at Various Temperatures
- Experimental Measurements of Vapor Liquid Equilibrium Data for the Binary Systems of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa
- Experimental Determination of Vapor Liquid Equilibria. Binary Systems of Methyl Acetate, Ethyl Acetate, and Propyl Acetate with 1-Propanol at 0.6 MPa
- Measurement and Correlation of Solubility and Dissolution Thermodynamic Properties of Furan-2-carboxylic Acid in Pure and Binary Solvents
- Experimental VLE data of Methyl Acetate or Ethyl Acetate with 2-Butanol at 0.3 and 0.6 MPa. Quality assessment and predictions.
- Experimental Measurement and Correlation of Solubility Data and Thermodynamic Properties of Protocatechuic Acid in Four Organic Solvents
- Liquid Liquid Equilibrium for Ternary System Methanol + Methyl Acetate + 1,3-Dimethylimidazolium Dimethylphosphate at Several Temperatures and Atmospheric Pressure
- Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
- Isobaric Vapor-Liquid Equilibria for Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
- Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
- Liquid Liquid Equilibria of Mixtures Containing Methyl Acetate + Methanol + Hexane or Heptane
- Densities and Viscosities of 1-Butyl-3-methylimidazolium Tetrafluoroborate + Molecular Solvent Binary Mixtures
- Solubility of Lovastatin in Ethyl Acetate, Propyl Acetate, Isopropyl Acetate, Butyl Acetate, sec-Butyl Acetate, Isobutyl Acetate, tert-Butyl Acetate, and 2-Butanone, between (285 and 313) K
- Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K
- Solubility of Valsartan in Different Organic Solvents and Ethanol + Water Binary Mixtures from (278.15 to 313.15) K
- Isobaric Vapor-Liquid Equilibria for the Binary Systems Benzene + Methyl Ethanoate, Benzene + Butyl Ethanoate, and Benzene + Methyl Heptanoate at 101.31kPa
- Solubility of Captopril in 2-Propanol, Acetone, Acetonitrile, Methyl Acetate, Ethyl Acetate, and Butyl Acetate
- Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Ternary Excess Molar Volumes of {Methyltrioctylammonium Bis[(trifluoromethyl)sulfonyl]imide + Methanol + Methyl Acetate or Ethyl Acetate} Systems at (298.15, 303.15, and 313.15) K
- Surface Tension Data of Aqueous Binary Mixtures of Methyl, Ethyl, Propyl, and Butyl Acetates at 298.15 K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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