- InChI
- InChI=1S/C9H18O2/c1-3-5-6-7-8-9(10)11-4-2/h3-8H2,1-2H3
- InChI Key
- TVQGDYNRXLTQAP-UHFFFAOYSA-N
- Formula
- C9H18O2
- SMILES
- CCCCCCC(=O)OCC
- Molecular Weight1
- 158.24
- CAS
- 106-30-9
- Other Names
-
- AETHER OENANTHICUS
- Cognac oil
- ENANTHYLIC ETHER
- ETHYL HEPTANOATE
- Enanthic acid ethyl ester
- Ethyl enanthate
- Ethyl ester of heptanoic acid
- Ethyl heptoate
- Ethyl heptylate
- Ethyl n-heptanoate
- Ethyl oenanthate
- Ethyl oenanthylate
- Grape oil
- NSC 8891
- Oenanthic ether
- Oleum vitis viniferae
- Wine oil
- ethyl enantate
- 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).
- 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.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×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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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -209.02 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -548.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -603.80 ± 1.50 | kJ/mol | NIST |
| ΔfusH° | 21.85 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [55.80; 56.00] | kJ/mol |
|
| ΔvapH° | 56.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 55.80 | kJ/mol | NIST |
| log10WS | [-2.74; -2.71] |
|
|
| log10WS | -2.71 | Aq. Sol... | |
| log10WS | -2.74 | Estimat... | |
| logPoct/wat | 2.520 | Crippen Calculated Property | |
| McVol | 145.110 | ml/mol | McGowan Calculated Property |
| Pc | 2356.90 | kPa | Develop... |
| Inp | [1068.00; 1108.00] |
|
|
| Inp | 1077.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1085.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1093.30 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | Outlier 1068.00 | NIST | |
| Inp | Outlier 1068.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1093.30 | NIST | |
| I | [1310.00; 1375.00] |
|
|
| I | 1328.00 | NIST | |
| I | Outlier 1375.00 | NIST | |
| I | 1325.00 | NIST | |
| I | Outlier 1369.00 | NIST | |
| I | Outlier 1367.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1324.00 | NIST | |
| I | 1352.00 | NIST | |
| I | 1329.00 | NIST | |
| I | 1328.00 | NIST | |
| I | Outlier 1372.00 | NIST | |
| I | 1323.00 | NIST | |
| I | 1324.00 | NIST | |
| I | 1324.00 | NIST | |
| I | 1334.00 | NIST | |
| I | 1337.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1326.00 | NIST | |
| I | 1331.00 | NIST | |
| I | 1327.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1324.00 | NIST | |
| I | 1331.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1317.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1310.00 | NIST | |
| I | 1342.00 | NIST | |
| I | 1315.00 | NIST | |
| I | 1321.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1342.00 | NIST | |
| I | 1330.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1349.00 | NIST | |
| I | 1315.00 | NIST | |
| I | 1317.00 | NIST | |
| I | 1327.00 | NIST | |
| I | 1331.00 | NIST | |
| I | 1331.00 | NIST | |
| I | 1321.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1335.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1321.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1331.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1328.00 | NIST | |
| I | 1334.00 | NIST | |
| Tboil | [460.30; 461.70] | K |
|
| Tboil | 461.70 | K | KDB |
| Tboil | 461.70 | K | NIST |
| Tboil | 461.70 ± 0.30 | K | NIST |
| Tboil | 460.30 ± 2.00 | K | NIST |
| Tc | 634.30 ± 0.60 | K | NIST |
| Tfus | [206.90; 207.12] | K |
|
| Tfus | 207.05 | K | KDB |
| Tfus | 207.12 | K | Aq. Sol... |
| Tfus | 206.90 ± 0.50 | K | NIST |
| Vc | 0.564 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [322.89; 395.29] | J/mol×K | [481.61; 655.29] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 320 340 360 380 400 500 550 600 650 | ||||
| Cp,gas | 322.89 | J/mol×K | 481.61 | Joback Calculated Property |
| Cp,gas | 336.15 | J/mol×K | 510.56 | Joback Calculated Property |
| Cp,gas | 348.92 | J/mol×K | 539.50 | Joback Calculated Property |
| Cp,gas | 361.21 | J/mol×K | 568.45 | Joback Calculated Property |
| Cp,gas | 373.04 | J/mol×K | 597.40 | Joback Calculated Property |
| Cp,gas | 384.40 | J/mol×K | 626.35 | Joback Calculated Property |
| Cp,gas | 395.29 | J/mol×K | 655.29 | Joback Calculated Property |
| η | [0.0002395; 0.0033103] | Pa×s | [263.35; 481.61] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 300 350 400 450 | ||||
| η | 0.0033103 | Pa×s | 263.35 | Joback Calculated Property |
| η | 0.0016384 | Pa×s | 299.73 | Joback Calculated Property |
| η | 0.0009442 | Pa×s | 336.10 | Joback Calculated Property |
| η | 0.0006060 | Pa×s | 372.48 | Joback Calculated Property |
| η | 0.0004209 | Pa×s | 408.86 | Joback Calculated Property |
| η | 0.0003103 | Pa×s | 445.23 | Joback Calculated Property |
| η | 0.0002395 | Pa×s | 481.61 | Joback Calculated Property |
| n0 | [1.38421; 1.42006] | [278.15; 358.15] |
|
|
|
T(K) Refractive Index 1.39 1.39 1.4 1.4 1.41 1.41 1.42 1.42 300 350 | ||||
| n0 | 1.42006 | 278.15 | Thermop... | |
| n0 | 1.41784 | 283.15 | Thermop... | |
| n0 | 1.41562 | 288.15 | Thermop... | |
| n0 | 1.41341 | 293.15 | Thermop... | |
| n0 | 1.41119 | 298.15 | Thermop... | |
| n0 | 1.40896 | 303.15 | Thermop... | |
| n0 | 1.40673 | 308.15 | Thermop... | |
| n0 | 1.40445 | 313.15 | Thermop... | |
| n0 | 1.40216 | 318.15 | Thermop... | |
| n0 | 1.39988 | 323.15 | Thermop... | |
| n0 | 1.39761 | 328.15 | Thermop... | |
| n0 | 1.39535 | 333.15 | Thermop... | |
| n0 | 1.39311 | 338.15 | Thermop... | |
| n0 | 1.39088 | 343.15 | Thermop... | |
| n0 | 1.38866 | 348.15 | Thermop... | |
| n0 | 1.38645 | 353.15 | Thermop... | |
| n0 | 1.38421 | 358.15 | Thermop... | |
| ρl | 881.30 | kg/m3 | 293.15 | Phase e... |
| λ | [0.11; 0.15] | W/m×K | [250.38; 393.46] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.12 0.12 0.13 0.13 0.14 0.14 0.15 0.15 250 300 350 | ||||
| λ | 0.15 | W/m×K | 250.38 | Measure... |
| λ | 0.15 | W/m×K | 260.21 | Measure... |
| λ | 0.14 | W/m×K | 270.16 | Measure... |
| λ | 0.14 | W/m×K | 280.02 | Measure... |
| λ | 0.14 | W/m×K | 289.93 | Measure... |
| λ | 0.14 | W/m×K | 299.84 | Measure... |
| λ | 0.13 | W/m×K | 309.90 | Measure... |
| λ | 0.13 | W/m×K | 319.73 | Measure... |
| λ | 0.13 | W/m×K | 329.73 | Measure... |
| λ | 0.13 | W/m×K | 337.72 | Measure... |
| λ | 0.13 | W/m×K | 341.71 | Measure... |
| λ | 0.13 | W/m×K | 347.65 | Measure... |
| λ | 0.12 | W/m×K | 353.60 | Measure... |
| λ | 0.12 | W/m×K | 363.50 | Measure... |
| λ | 0.12 | W/m×K | 373.51 | Measure... |
| λ | 0.12 | W/m×K | 383.64 | Measure... |
| λ | 0.11 | W/m×K | 393.46 | Measure... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 351.20 | K | 1.90 | NIST |
Datasets
- Molar heat capacity at constant pressure, J/K/mol (1)
- Mass density, kg/m3 (1)
- Speed of sound, m/s (1)
Molar heat capacity at constant pressure, J/K/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 305.40 | 100.00 | 318.30 |
| 305.40 | 4040.00 | 317.70 |
| 305.40 | 8190.00 | 317.30 |
| 305.40 | 12090.00 | 316.80 |
| 305.50 | 16070.00 | 316.40 |
| 315.70 | 100.00 | 322.50 |
| 315.80 | 4190.00 | 322.00 |
| 315.90 | 8150.00 | 321.60 |
| 315.90 | 12260.00 | 320.50 |
| 316.00 | 16160.00 | 319.60 |
| 326.50 | 100.00 | 326.80 |
| 326.50 | 4140.00 | 325.90 |
| 326.60 | 8170.00 | 325.20 |
| 326.60 | 12110.00 | 324.30 |
| 326.20 | 16030.00 | 323.60 |
| 335.30 | 100.00 | 330.30 |
| 335.30 | 4060.00 | 330.10 |
| 335.40 | 8050.00 | 328.60 |
| 335.40 | 12030.00 | 327.60 |
| 335.50 | 16070.00 | 326.90 |
| 345.10 | 100.00 | 334.20 |
| 345.20 | 4070.00 | 333.50 |
| 345.60 | 8230.00 | 332.50 |
| 345.70 | 12160.00 | 332.20 |
| 345.70 | 16230.00 | 330.50 |
| 354.20 | 100.00 | 337.80 |
| 354.20 | 4120.00 | 337.30 |
| 354.30 | 8010.00 | 336.50 |
| 354.40 | 12390.00 | 335.60 |
| 354.50 | 16250.00 | 334.50 |
| 364.90 | 100.00 | 342.10 |
| 365.30 | 3870.00 | 341.30 |
| 365.60 | 8320.00 | 340.30 |
| 365.70 | 12160.00 | 339.50 |
| 365.80 | 15950.00 | 338.30 |
| 374.80 | 100.00 | 346.10 |
| 375.00 | 3980.00 | 345.50 |
| 375.50 | 8020.00 | 344.00 |
| 375.70 | 12070.00 | 342.60 |
| 375.90 | 16040.00 | 341.40 |
| 384.00 | 100.00 | 349.80 |
| 385.00 | 4020.00 | 349.10 |
| 385.40 | 8040.00 | 347.10 |
| 385.50 | 11880.00 | 346.10 |
| 385.70 | 15890.00 | 345.60 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 303.20 | 100.00 | 860.8 |
| 303.20 | 3020.00 | 864.5 |
| 303.10 | 6000.00 | 867.7 |
| 303.20 | 9010.00 | 871.2 |
| 303.21 | 11950.00 | 874.5 |
| 303.19 | 14980.00 | 877.5 |
| 312.96 | 100.00 | 851.2 |
| 313.06 | 3060.00 | 854.7 |
| 313.13 | 6090.00 | 858.1 |
| 313.17 | 9070.00 | 861.4 |
| 313.18 | 12000.00 | 864.7 |
| 313.17 | 15010.00 | 867.9 |
| 323.09 | 100.00 | 841.6 |
| 323.11 | 3100.00 | 845.2 |
| 323.14 | 6110.00 | 848.8 |
| 323.10 | 9100.00 | 852.5 |
| 323.13 | 12060.00 | 855.8 |
| 323.09 | 15150.00 | 859.2 |
| 333.05 | 100.00 | 832.1 |
| 333.14 | 3010.00 | 835.6 |
| 333.18 | 6080.00 | 839.7 |
| 333.14 | 9020.00 | 843.2 |
| 333.14 | 12010.00 | 846.8 |
| 333.20 | 15070.00 | 850.5 |
| 343.02 | 100.00 | 823.0 |
| 343.06 | 3010.00 | 827.1 |
| 343.23 | 6050.00 | 831.0 |
| 343.20 | 9000.00 | 834.8 |
| 343.22 | 12100.00 | 838.5 |
| 343.19 | 15000.00 | 842.1 |
| 352.85 | 100.00 | 815.1 |
| 352.95 | 3090.00 | 819.4 |
| 353.11 | 6070.00 | 823.2 |
| 353.06 | 9090.00 | 827.5 |
| 353.14 | 12070.00 | 831.2 |
| 353.23 | 15010.00 | 835.1 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 293.27 | 110.00 | 1254.03 |
| 303.20 | 100.00 | 1219.89 |
| 313.04 | 90.00 | 1185.84 |
| 323.08 | 110.00 | 1145.28 |
| 332.61 | 100.00 | 1119.94 |
| 343.14 | 100.00 | 1075.42 |
| 353.04 | 110.00 | 1044.19 |
| 363.11 | 100.00 | 1008.42 |
| 372.84 | 90.00 | 971.9 |
| 382.87 | 100.00 | 941.96 |
| 392.49 | 100.00 | 909.29 |
| 401.72 | 110.00 | 876.2 |
| 412.92 | 100.00 | 837.29 |
| 422.78 | 110.00 | 800.01 |
| 432.75 | 100.00 | 768.89 |
| 441.74 | 90.00 | 736.98 |
| 452.13 | 100.00 | 703.21 |
| 293.55 | 1040.00 | 1263.87 |
| 302.87 | 1020.00 | 1230.26 |
| 313.07 | 1000.00 | 1189.64 |
| 323.15 | 1020.00 | 1154.57 |
| 332.75 | 980.00 | 1123.74 |
| 343.15 | 1020.00 | 1086.84 |
| 352.67 | 1000.00 | 1053.08 |
| 362.35 | 1010.00 | 1014.12 |
| 371.83 | 1020.00 | 987.06 |
| 382.34 | 1020.00 | 948.49 |
| 392.73 | 980.00 | 912.95 |
| 401.77 | 1030.00 | 883.74 |
| 412.69 | 1050.00 | 841.82 |
| 422.42 | 1000.00 | 807.44 |
| 432.36 | 1120.00 | 778.68 |
| 441.56 | 1020.00 | 750.38 |
| 451.89 | 990.00 | 714.64 |
| 462.89 | 1110.00 | 677.9 |
| 471.98 | 1010.00 | 647.85 |
| 482.54 | 1000.00 | 610.64 |
| 293.40 | 2560.00 | 1278.44 |
| 303.46 | 2500.00 | 1233.57 |
| 313.11 | 2510.00 | 1200.03 |
| 323.11 | 2490.00 | 1164.66 |
| 332.84 | 2500.00 | 1127.35 |
| 451.94 | 2540.00 | 731.06 |
| 463.03 | 2520.00 | 699.91 |
| 472.16 | 2540.00 | 667.91 |
| 482.35 | 2490.00 | 636.04 |
| 293.20 | 4000.00 | 1290.82 |
| 303.00 | 4050.00 | 1253.21 |
| 312.99 | 4070.00 | 1207.7 |
| 323.12 | 3990.00 | 1173.82 |
| 332.85 | 4010.00 | 1140.43 |
| 343.20 | 4050.00 | 1101.44 |
| 352.64 | 4010.00 | 1073.47 |
| 362.37 | 4060.00 | 1038.84 |
| 371.97 | 4040.00 | 1005.36 |
| 382.36 | 3940.00 | 970.18 |
| 392.65 | 4020.00 | 936.25 |
| 401.75 | 4030.00 | 907.66 |
| 412.64 | 4050.00 | 868.48 |
| 422.45 | 4040.00 | 836.46 |
| 432.43 | 4070.00 | 805.62 |
| 441.62 | 4050.00 | 783.09 |
| 452.05 | 4040.00 | 748.01 |
| 463.13 | 4040.00 | 714.4 |
| 472.23 | 4040.00 | 687.28 |
| 483.02 | 4020.00 | 655.14 |
| 293.74 | 5550.00 | 1291.01 |
| 303.04 | 5540.00 | 1254.0 |
| 313.12 | 5550.00 | 1223.42 |
| 323.12 | 5530.00 | 1181.98 |
| 333.57 | 5530.00 | 1140.54 |
| 343.18 | 5510.00 | 1114.79 |
| 352.70 | 5540.00 | 1079.0 |
| 362.26 | 5530.00 | 1045.42 |
| 372.00 | 5590.00 | 1016.18 |
| 382.32 | 5500.00 | 983.52 |
| 392.67 | 5520.00 | 946.64 |
| 401.62 | 5620.00 | 919.87 |
| 412.54 | 5550.00 | 885.03 |
| 422.48 | 5560.00 | 854.66 |
| 432.45 | 5500.00 | 819.99 |
| 441.62 | 5570.00 | 795.09 |
| 452.08 | 5580.00 | 763.54 |
| 463.22 | 5530.00 | 728.32 |
| 382.36 | 7030.00 | 991.78 |
| 392.69 | 6990.00 | 960.26 |
| 401.59 | 6980.00 | 932.15 |
| 412.71 | 7010.00 | 898.63 |
| 422.53 | 6970.00 | 866.85 |
| 432.47 | 6990.00 | 831.89 |
| 441.61 | 7020.00 | 810.86 |
| 452.07 | 7050.00 | 781.2 |
| 463.25 | 7020.00 | 748.5 |
| 472.22 | 7040.00 | 716.46 |
| 483.13 | 7020.00 | 690.38 |
| 294.07 | 8560.00 | 1302.85 |
| 303.06 | 8580.00 | 1271.63 |
| 313.03 | 8520.00 | 1229.84 |
| 323.14 | 8520.00 | 1198.91 |
| 332.87 | 8520.00 | 1168.42 |
| 343.18 | 8540.00 | 1133.1 |
| 352.86 | 8580.00 | 1098.06 |
| 362.06 | 8560.00 | 1073.66 |
| 372.00 | 8580.00 | 1035.47 |
| 382.40 | 8550.00 | 1003.61 |
| 392.72 | 8520.00 | 974.33 |
| 401.43 | 8550.00 | 945.5 |
| 412.77 | 8460.00 | 910.68 |
| 422.49 | 8460.00 | 880.79 |
| 432.50 | 8520.00 | 845.66 |
| 441.61 | 8500.00 | 822.18 |
| 452.07 | 8500.00 | 791.7 |
| 463.26 | 8550.00 | 758.92 |
| 472.22 | 8560.00 | 727.9 |
| 483.34 | 8540.00 | 700.94 |
| 293.99 | 10050.00 | 1302.01 |
| 303.06 | 10060.00 | 1275.7 |
| 313.06 | 9950.00 | 1235.73 |
| 323.14 | 9970.00 | 1202.86 |
| 332.88 | 10020.00 | 1171.25 |
| 343.18 | 10030.00 | 1146.59 |
| 352.81 | 9950.00 | 1114.93 |
| 362.02 | 9960.00 | 1086.09 |
| 372.00 | 9980.00 | 1054.29 |
| 382.38 | 10030.00 | 1013.95 |
| 392.70 | 10020.00 | 988.42 |
| 342.92 | 2540.00 | 1095.65 |
| 352.61 | 2510.00 | 1056.91 |
| 362.38 | 2500.00 | 1028.17 |
| 371.91 | 2580.00 | 995.52 |
| 382.38 | 2510.00 | 958.12 |
| 392.65 | 2490.00 | 924.2 |
| 401.70 | 2510.00 | 892.06 |
| 412.73 | 2540.00 | 858.95 |
| 422.35 | 2540.00 | 826.98 |
| 432.43 | 2500.00 | 790.22 |
| 441.59 | 2560.00 | 766.2 |
| 472.22 | 5550.00 | 706.95 |
| 483.07 | 5540.00 | 677.03 |
| 293.91 | 7040.00 | 1299.58 |
| 303.06 | 7040.00 | 1262.89 |
| 313.09 | 7070.00 | 1225.84 |
| 323.13 | 7000.00 | 1188.04 |
| 332.88 | 7010.00 | 1156.97 |
| 343.18 | 7060.00 | 1119.21 |
| 352.76 | 7070.00 | 1088.79 |
| 361.99 | 7040.00 | 1061.57 |
| 372.00 | 7060.00 | 1029.84 |
| 401.51 | 10090.00 | 955.49 |
| 412.74 | 10010.00 | 920.21 |
| 422.51 | 9930.00 | 896.93 |
| 432.49 | 10010.00 | 865.32 |
| 441.61 | 10030.00 | 837.4 |
| 452.07 | 10040.00 | 804.8 |
| 463.25 | 10030.00 | 765.58 |
| 472.22 | 10050.00 | 743.93 |
| 483.14 | 10030.00 | 706.31 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [345.12; 483.23] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53528e+01 | |||
| Coefficient B | -4.15873e+03 | |||
| Coefficient C | -6.90720e+01 | |||
| Temperature range, min. | 345.12 | |||
| Temperature range, max. | 483.23 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 345.12 | Calculated Property |
| Pvap | 2.95 | kPa | 360.47 | Calculated Property |
| Pvap | 6.02 | kPa | 375.81 | Calculated Property |
| Pvap | 11.48 | kPa | 391.16 | Calculated Property |
| Pvap | 20.66 | kPa | 406.50 | Calculated Property |
| Pvap | 35.31 | kPa | 421.85 | Calculated Property |
| Pvap | 57.72 | kPa | 437.19 | Calculated Property |
| Pvap | 90.72 | kPa | 452.54 | Calculated Property |
| Pvap | 137.70 | kPa | 467.88 | Calculated Property |
| Pvap | 202.64 | kPa | 483.23 | Calculated Property |
Similar Compounds
Find more compounds similar to Heptanoic acid, ethyl ester.
Mixtures
- Heptanoic acid, ethyl ester + Formic acid + Water
- Heptanoic acid, ethyl ester + Acetic acid + Water
- Carbon dioxide + Heptanoic acid, ethyl ester
Sources
- Crippen Method
- Phase equilibrium of (water + formic or acetic acid + ethyl heptanoate) ternary liquid systems at different temperatures
- Measurement of speed of sound and thermal diffusivity of ethyl heptanoate using light scattering method
- Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
- Isobaric heat capacities of ethyl heptanoate and ethyl cinnamate at pressures up to 16.3 MPa
- Thermophysical properties of fatty acid methyl and ethyl esters
- Densities and Viscosities of Ethyl Heptanoate and Ethyl Octanoate at Temperatures from 303 to 353 K and at Pressures up to 15 MPa
- Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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