- InChI
- InChI=1S/C8H16O2/c1-3-5-7-10-8(9)6-4-2/h3-7H2,1-2H3
- InChI Key
- XUPYJHCZDLZNFP-UHFFFAOYSA-N
- Formula
- C8H16O2
- SMILES
- CCCCOC(=O)CCC
- Molecular Weight1
- 144.21
- CAS
- 109-21-7
- Other Names
-
- 1-Butyl butyrate
- BUTYL BUTANOATE
- BUTYL ESTER BUTANOIC ACID
- Butyl butylate
- Butyl butyrate
- Butyl ester of butanoic acid
- Butyl n-butyrate
- Butyric acid, butyl ester
- N-BUTYL BUTYRATE
- N-BUTYL N-BUTYRATE
- NSC 8458
- n-Butyl butanoate
- n-Butyl n-butanoate
- n-Butyric acid n-butyl ester
- ΔcH°liquid : Standard liquid 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).
- 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).
- 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.
- 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).
- Ttriple : Triple Point Temperature (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 |
|---|---|---|---|
| ΔcH°liquid | -4844.20 | kJ/mol | NIST |
| ΔfG° | -217.44 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -453.25 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 19.26 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 42.56 | kJ/mol | Joback Calculated Property |
| log10WS | -2.03 | Crippen Calculated Property | |
| logPoct/wat | 2.130 | Crippen Calculated Property | |
| McVol | 131.020 | ml/mol | McGowan Calculated Property |
| Pc | 2657.03 | kPa | Joback Calculated Property |
| Inp | [940.00; 1009.00] |
|
|
| Inp | 979.40 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | Outlier 940.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 998.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 1001.00 | NIST | |
| Inp | 998.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | Outlier 1009.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 987.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 994.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 979.40 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 975.00 | NIST | |
| I | [1183.00; 1251.00] |
|
|
| I | 1215.00 | NIST | |
| I | 1230.00 | NIST | |
| I | Outlier 1251.00 | NIST | |
| I | 1221.00 | NIST | |
| I | 1221.00 | NIST | |
| I | Outlier 1245.00 | NIST | |
| I | 1232.00 | NIST | |
| I | 1213.00 | NIST | |
| I | Outlier 1196.00 | NIST | |
| I | 1224.00 | NIST | |
| I | 1207.00 | NIST | |
| I | 1212.00 | NIST | |
| I | 1215.00 | NIST | |
| I | 1201.00 | NIST | |
| I | 1223.00 | NIST | |
| I | 1218.00 | NIST | |
| I | 1231.00 | NIST | |
| I | 1220.00 | NIST | |
| I | 1214.00 | NIST | |
| I | 1240.00 | NIST | |
| I | Outlier 1183.00 | NIST | |
| I | 1210.00 | NIST | |
| I | 1218.00 | NIST | |
| I | 1218.00 | NIST | |
| I | 1219.00 | NIST | |
| I | 1207.00 | NIST | |
| I | 1221.00 | NIST | |
| I | 1205.00 | NIST | |
| I | 1216.00 | NIST | |
| I | 1243.00 | NIST | |
| I | 1226.00 | NIST | |
| I | 1216.00 | NIST | |
| I | 1207.00 | NIST | |
| I | 1219.00 | NIST | |
| I | 1208.00 | NIST | |
| I | 1221.00 | NIST | |
| I | 1218.00 | NIST | |
| I | 1206.00 | NIST | |
| I | 1206.00 | NIST | |
| I | 1225.00 | NIST | |
| I | 1228.00 | NIST | |
| I | 1228.00 | NIST | |
| I | 1220.00 | NIST | |
| I | 1228.00 | NIST | |
| I | 1228.00 | NIST | |
| I | 1229.00 | NIST | |
| I | 1229.00 | NIST | |
| I | 1229.00 | NIST | |
| I | 1216.00 | NIST | |
| I | 1227.00 | NIST | |
| I | 1223.00 | NIST | |
| I | 1240.00 | NIST | |
| I | 1208.00 | NIST | |
| I | 1225.00 | NIST | |
| I | 1228.00 | NIST | |
| I | 1227.00 | NIST | |
| I | 1215.00 | NIST | |
| Tboil | [436.75; 439.75] | K |
|
| Tboil | 438.28 | K | Measure... |
| Tboil | 438.09 | K | Vapor-L... |
| Tboil | 437.70 | K | NIST |
| Tboil | 437.00 | K | NIST |
| Tboil | 438.15 ± 2.00 | K | NIST |
| Tboil | 439.55 ± 1.00 | K | NIST |
| Tboil | 439.65 ± 1.00 | K | NIST |
| Tboil | 437.65 ± 1.00 | K | NIST |
| Tboil | 439.15 ± 1.00 | K | NIST |
| Tboil | 439.55 ± 0.30 | K | NIST |
| Tboil | 438.00 ± 2.00 | K | NIST |
| Tboil | 437.15 ± 1.00 | K | NIST |
| Tboil | 439.40 ± 1.00 | K | NIST |
| Tboil | 436.75 ± 1.00 | K | NIST |
| Tboil | 439.75 ± 1.00 | K | NIST |
| Tboil | 439.60 ± 0.40 | K | NIST |
| Tboil | 438.90 ± 1.50 | K | NIST |
| Tc | 612.10 ± 0.60 | K | NIST |
| Tfus | 252.08 | K | Joback Calculated Property |
| Ttriple | [181.58; 181.68] | K |
|
| Ttriple | 181.58 ± 0.10 | K | NIST |
| Ttriple | 181.68 ± 0.04 | K | NIST |
| Vc | 0.507 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [279.70; 346.77] | J/mol×K | [458.73; 633.80] |
|
| Cp,gas | 279.70 | J/mol×K | 458.73 | Joback Calculated Property |
| Cp,gas | 291.94 | J/mol×K | 487.91 | Joback Calculated Property |
| Cp,gas | 303.75 | J/mol×K | 517.09 | Joback Calculated Property |
| Cp,gas | 315.14 | J/mol×K | 546.26 | Joback Calculated Property |
| Cp,gas | 326.10 | J/mol×K | 575.44 | Joback Calculated Property |
| Cp,gas | 336.64 | J/mol×K | 604.62 | Joback Calculated Property |
| Cp,gas | 346.77 | J/mol×K | 633.80 | Joback Calculated Property |
| η | [0.0004860; 0.0009480] | Pa×s | [293.15; 343.15] |
|
| η | 0.0009480 | Pa×s | 293.15 | Density... |
| η | 0.0008760 | Pa×s | 298.15 | Density... |
| η | 0.0008120 | Pa×s | 303.15 | Density... |
| η | 0.0007550 | Pa×s | 308.15 | Density... |
| η | 0.0007050 | Pa×s | 313.15 | Density... |
| η | 0.0006590 | Pa×s | 318.15 | Density... |
| η | 0.0006180 | Pa×s | 323.15 | Density... |
| η | 0.0005810 | Pa×s | 328.15 | Density... |
| η | 0.0005480 | Pa×s | 333.15 | Density... |
| η | 0.0005170 | Pa×s | 338.15 | Density... |
| η | 0.0004860 | Pa×s | 343.15 | Density... |
| ΔfusH | [14.93; 14.93] | kJ/mol | [181.68; 181.70] |
|
| ΔfusH | 14.93 | kJ/mol | 181.68 | NIST |
| ΔfusH | 14.93 | kJ/mol | 181.70 | NIST |
| Pvap | [40.28; 164.01] | kPa | [405.54; 457.47] |
|
| Pvap | 40.28 | kPa | 405.54 | Vapor-L... |
| Pvap | 41.53 | kPa | 406.59 | Vapor-L... |
| Pvap | 42.86 | kPa | 407.56 | Vapor-L... |
| Pvap | 44.16 | kPa | 408.56 | Vapor-L... |
| Pvap | 45.06 | kPa | 409.28 | Vapor-L... |
| Pvap | 46.65 | kPa | 410.43 | Vapor-L... |
| Pvap | 48.06 | kPa | 411.38 | Vapor-L... |
| Pvap | 49.58 | kPa | 412.43 | Vapor-L... |
| Pvap | 50.53 | kPa | 413.11 | Vapor-L... |
| Pvap | 52.27 | kPa | 414.21 | Vapor-L... |
| Pvap | 53.34 | kPa | 414.92 | Vapor-L... |
| Pvap | 54.86 | kPa | 415.87 | Vapor-L... |
| Pvap | 56.21 | kPa | 416.72 | Vapor-L... |
| Pvap | 57.51 | kPa | 417.51 | Vapor-L... |
| Pvap | 58.78 | kPa | 418.27 | Vapor-L... |
| Pvap | 60.01 | kPa | 418.98 | Vapor-L... |
| Pvap | 61.31 | kPa | 419.74 | Vapor-L... |
| Pvap | 62.83 | kPa | 420.59 | Vapor-L... |
| Pvap | 64.02 | kPa | 421.26 | Vapor-L... |
| Pvap | 65.51 | kPa | 422.07 | Vapor-L... |
| Pvap | 66.81 | kPa | 422.76 | Vapor-L... |
| Pvap | 67.91 | kPa | 423.35 | Vapor-L... |
| Pvap | 69.74 | kPa | 424.29 | Vapor-L... |
| Pvap | 70.42 | kPa | 424.66 | Vapor-L... |
| Pvap | 72.31 | kPa | 425.59 | Vapor-L... |
| Pvap | 73.25 | kPa | 426.07 | Vapor-L... |
| Pvap | 74.67 | kPa | 426.78 | Vapor-L... |
| Pvap | 76.02 | kPa | 427.43 | Vapor-L... |
| Pvap | 77.34 | kPa | 428.05 | Vapor-L... |
| Pvap | 78.82 | kPa | 428.69 | Vapor-L... |
| Pvap | 79.99 | kPa | 429.28 | Vapor-L... |
| Pvap | 81.71 | kPa | 430.02 | Vapor-L... |
| Pvap | 82.77 | kPa | 430.48 | Vapor-L... |
| Pvap | 84.03 | kPa | 431.04 | Vapor-L... |
| Pvap | 85.54 | kPa | 431.70 | Vapor-L... |
| Pvap | 86.67 | kPa | 432.27 | Vapor-L... |
| Pvap | 87.95 | kPa | 432.82 | Vapor-L... |
| Pvap | 89.55 | kPa | 433.42 | Vapor-L... |
| Pvap | 90.72 | kPa | 433.90 | Vapor-L... |
| Pvap | 91.87 | kPa | 434.46 | Vapor-L... |
| Pvap | 93.35 | kPa | 435.06 | Vapor-L... |
| Pvap | 94.70 | kPa | 435.61 | Vapor-L... |
| Pvap | 96.15 | kPa | 436.09 | Vapor-L... |
| Pvap | 97.30 | kPa | 436.56 | Vapor-L... |
| Pvap | 98.75 | kPa | 437.11 | Vapor-L... |
| Pvap | 100.18 | kPa | 437.66 | Vapor-L... |
| Pvap | 101.32 | kPa | 438.09 | Vapor-L... |
| Pvap | 101.30 | kPa | 438.28 | Measure... |
| Pvap | 102.63 | kPa | 438.67 | Vapor-L... |
| Pvap | 104.00 | kPa | 439.18 | Vapor-L... |
| Pvap | 105.50 | kPa | 439.66 | Vapor-L... |
| Pvap | 106.67 | kPa | 440.16 | Vapor-L... |
| Pvap | 108.31 | kPa | 440.68 | Vapor-L... |
| Pvap | 109.48 | kPa | 441.11 | Vapor-L... |
| Pvap | 110.68 | kPa | 441.60 | Vapor-L... |
| Pvap | 112.07 | kPa | 442.01 | Vapor-L... |
| Pvap | 113.34 | kPa | 442.53 | Vapor-L... |
| Pvap | 114.71 | kPa | 442.93 | Vapor-L... |
| Pvap | 116.00 | kPa | 443.44 | Vapor-L... |
| Pvap | 117.43 | kPa | 443.86 | Vapor-L... |
| Pvap | 118.65 | kPa | 444.34 | Vapor-L... |
| Pvap | 120.03 | kPa | 444.78 | Vapor-L... |
| Pvap | 121.28 | kPa | 445.21 | Vapor-L... |
| Pvap | 122.76 | kPa | 445.62 | Vapor-L... |
| Pvap | 124.03 | kPa | 446.04 | Vapor-L... |
| Pvap | 125.37 | kPa | 446.47 | Vapor-L... |
| Pvap | 126.64 | kPa | 446.87 | Vapor-L... |
| Pvap | 128.00 | kPa | 447.33 | Vapor-L... |
| Pvap | 129.33 | kPa | 447.74 | Vapor-L... |
| Pvap | 130.73 | kPa | 448.18 | Vapor-L... |
| Pvap | 132.01 | kPa | 448.54 | Vapor-L... |
| Pvap | 133.41 | kPa | 448.97 | Vapor-L... |
| Pvap | 134.68 | kPa | 449.36 | Vapor-L... |
| Pvap | 135.99 | kPa | 449.75 | Vapor-L... |
| Pvap | 137.35 | kPa | 450.15 | Vapor-L... |
| Pvap | 138.69 | kPa | 450.55 | Vapor-L... |
| Pvap | 140.07 | kPa | 450.94 | Vapor-L... |
| Pvap | 141.21 | kPa | 451.29 | Vapor-L... |
| Pvap | 142.69 | kPa | 451.71 | Vapor-L... |
| Pvap | 143.97 | kPa | 452.07 | Vapor-L... |
| Pvap | 145.69 | kPa | 452.55 | Vapor-L... |
| Pvap | 146.84 | kPa | 452.88 | Vapor-L... |
| Pvap | 148.17 | kPa | 453.25 | Vapor-L... |
| Pvap | 149.33 | kPa | 453.58 | Vapor-L... |
| Pvap | 150.73 | kPa | 453.95 | Vapor-L... |
| Pvap | 152.16 | kPa | 454.34 | Vapor-L... |
| Pvap | 153.29 | kPa | 454.65 | Vapor-L... |
| Pvap | 154.65 | kPa | 455.02 | Vapor-L... |
| Pvap | 155.97 | kPa | 455.37 | Vapor-L... |
| Pvap | 157.25 | kPa | 455.71 | Vapor-L... |
| Pvap | 158.69 | kPa | 456.09 | Vapor-L... |
| Pvap | 159.94 | kPa | 456.42 | Vapor-L... |
| Pvap | 161.37 | kPa | 456.79 | Vapor-L... |
| Pvap | 162.68 | kPa | 457.13 | Vapor-L... |
| Pvap | 164.01 | kPa | 457.47 | Vapor-L... |
| n0 | 1.40400 | 298.15 | Thermod... | |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [327.52; 466.20] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48960e+01 | |||
| Coefficient B | -3.86487e+03 | |||
| Coefficient C | -6.29560e+01 | |||
| Temperature range, min. | 327.52 | |||
| Temperature range, max. | 466.20 | |||
| Pvap | 1.33 | kPa | 327.52 | Calculated Property |
| Pvap | 2.98 | kPa | 342.93 | Calculated Property |
| Pvap | 6.12 | kPa | 358.34 | Calculated Property |
| Pvap | 11.71 | kPa | 373.75 | Calculated Property |
| Pvap | 21.07 | kPa | 389.16 | Calculated Property |
| Pvap | 35.96 | kPa | 404.56 | Calculated Property |
| Pvap | 58.59 | kPa | 419.97 | Calculated Property |
| Pvap | 91.70 | kPa | 435.38 | Calculated Property |
| Pvap | 138.49 | kPa | 450.79 | Calculated Property |
| Pvap | 202.67 | kPa | 466.20 | Calculated Property |
| Pvap | [1.59e-07; 2464.08] | kPa | [181.15; 616.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.26165e+01 | |||
| Coefficient B | -8.70435e+03 | |||
| Coefficient C | -9.68492e+00 | |||
| Coefficient D | 4.03773e-06 | |||
| Temperature range, min. | 181.15 | |||
| Temperature range, max. | 616.00 | |||
| Pvap | 1.59e-07 | kPa | 181.15 | Calculated Property |
| Pvap | 4.31e-04 | kPa | 229.47 | Calculated Property |
| Pvap | 0.05 | kPa | 277.78 | Calculated Property |
| Pvap | 1.36 | kPa | 326.10 | Calculated Property |
| Pvap | 12.78 | kPa | 374.42 | Calculated Property |
| Pvap | 65.71 | kPa | 422.73 | Calculated Property |
| Pvap | 226.67 | kPa | 471.05 | Calculated Property |
| Pvap | 595.90 | kPa | 519.37 | Calculated Property |
| Pvap | 1296.05 | kPa | 567.68 | Calculated Property |
| Pvap | 2464.08 | kPa | 616.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Butanoic acid, butyl ester.
Mixtures
- Butanoic acid, butyl ester + Ethane, 1,2-dichloro-
- Butanoic acid, butyl ester + Propane, 1,3-dichloro-
- Butanoic acid, butyl ester + Butane, 1,4-dichloro-
- Butanoic acid, butyl ester + Pentane, 1,5-dichloro-
- Butanoic acid, butyl ester + Hexane, 1,6-dichloro-
- Butanoic acid, butyl ester + Carbonic acid, dimethyl ester
- 2-Propanol, 2-methyl- + Butanoic acid, butyl ester
- Butanoic acid, butyl ester + Ethane, 1,2-dibromo-
- Butanoic acid, butyl ester + Propane, 1,3-dibromo-
- Butanoic acid, butyl ester + Butane, 1,4-dibromo-
- Butanoic acid, butyl ester + Pentane, 1,5-dibromo-
- Butanoic acid, butyl ester + Hexane, 1,6-dibromo-
- Butanoic acid, butyl ester + Carbon dioxide
- Butanoic acid, butyl ester + Dodecane
- Butanoic acid, butyl ester + Dodecane + 1-Octanol
- Butanoic acid, butyl ester + Acetic acid + Water
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Liquid-liquid equilibrium of water + acetic acid + butyl butyrate at 298 K and 1 atmosphere
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6
- Thermodynamic study of (alkyl esters + alpha,beta-alkyl dihalides) VI.H and V for 20 binary mixtures {xCu-1H2u-1CO2(CH2)3CH3 + (1 - x)alpha,omega-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, alpha = 1, and v = omega = 2 to 6
- Below the room temperature measurements of solubilities in ester absorbents for CO2 capture
- Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
- Excess molar volumes and enthalpies of mixing for the ternary system (butyl butyrate + 1-octanol + dodecane) at the temperature 308.15 K.
- Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol
- Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.