- InChI
- InChI=1S/C7H14O3/c1-3-4-5-10-7(9)6(2)8/h6,8H,3-5H2,1-2H3
- InChI Key
- MRABAEUHTLLEML-UHFFFAOYSA-N
- Formula
- C7H14O3
- SMILES
- CCCCOC(=O)C(C)O
- Molecular Weight1
- 146.18
- CAS
- 138-22-7
- Other Names
-
- (S)-n-butyl lactate
- 2-Hydroxypropanoic acid butyl ester
- Butyl «alpha»-hydroxypropionate
- Butylester kyseliny mlecne
- Lactic acid n-butyl ester
- NSC 6533
- butyl (S)-2-hydroxypropanoate
- butyl 2-hydroxypropanoate
- butyl L-(+)-lactate
- butyl L-lactate
- lactic acid, butyl ester
- n-Butyl lactate
- propanoic acid, 2-hydroxy-, butyl ester
- 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).
- ΔvapH : Enthalpy of vaporization at a given temperature (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.
- 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 |
|---|---|---|---|
| ΔfG° | -365.12 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -590.12 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 17.24 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 56.62 | kJ/mol | Joback Calculated Property |
| log10WS | -0.99 | Crippen Calculated Property | |
| logPoct/wat | 0.710 | Crippen Calculated Property | |
| McVol | 122.800 | ml/mol | McGowan Calculated Property |
| Pc | 3287.81 | kPa | Joback Calculated Property |
| Inp | 997.00 | NIST | |
| I | [1508.00; 1520.00] |
|
|
| I | 1520.00 | NIST | |
| I | 1508.00 | NIST | |
| Tboil | 459.20 | K | NIST |
| Tc | 700.51 | K | Joback Calculated Property |
| Tfus | 245.00 ± 2.00 | K | NIST |
| Vc | 0.465 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [288.76; 343.59] | J/mol×K | [527.59; 700.51] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 290 300 310 320 330 340 550 600 650 700 | ||||
| Cp,gas | 288.76 | J/mol×K | 527.59 | Joback Calculated Property |
| Cp,gas | 298.85 | J/mol×K | 556.41 | Joback Calculated Property |
| Cp,gas | 308.56 | J/mol×K | 585.23 | Joback Calculated Property |
| Cp,gas | 317.88 | J/mol×K | 614.05 | Joback Calculated Property |
| Cp,gas | 326.83 | J/mol×K | 642.87 | Joback Calculated Property |
| Cp,gas | 335.40 | J/mol×K | 671.69 | Joback Calculated Property |
| Cp,gas | 343.59 | J/mol×K | 700.51 | Joback Calculated Property |
| η | [0.0001245; 0.0172601] | Pa×s | [286.63; 527.59] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-3 0.01 0.02 300 400 500 | ||||
| η | 0.0172601 | Pa×s | 286.63 | Joback Calculated Property |
| η | 0.0045782 | Pa×s | 326.79 | Joback Calculated Property |
| η | 0.0016237 | Pa×s | 366.95 | Joback Calculated Property |
| η | 0.0007065 | Pa×s | 407.11 | Joback Calculated Property |
| η | 0.0003570 | Pa×s | 447.27 | Joback Calculated Property |
| η | 0.0002019 | Pa×s | 487.43 | Joback Calculated Property |
| η | 0.0001245 | Pa×s | 527.59 | Joback Calculated Property |
| ΔvapH | [49.90; 58.70] | kJ/mol | [397.50; 425.50] |
|
| ΔvapH | 58.70 | kJ/mol | 397.50 | NIST |
| ΔvapH | 49.90 | kJ/mol | 425.50 | NIST |
| Pvap | [5.76e-03; 0.35] | kPa | [273.60; 322.90] |
|
|
T(K) Vapor pressure (kPa) 0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 280 300 320 | ||||
| Pvap | 5.76e-03 | kPa | 273.60 | Renewab... |
| Pvap | 6.27e-03 | kPa | 274.10 | Renewab... |
| Pvap | 8.23e-03 | kPa | 276.60 | Renewab... |
| Pvap | 8.68e-03 | kPa | 277.20 | Renewab... |
| Pvap | 9.96e-03 | kPa | 279.20 | Renewab... |
| Pvap | 0.01 | kPa | 280.70 | Renewab... |
| Pvap | 0.01 | kPa | 281.80 | Renewab... |
| Pvap | 0.01 | kPa | 283.20 | Renewab... |
| Pvap | 0.02 | kPa | 285.40 | Renewab... |
| Pvap | 0.02 | kPa | 287.30 | Renewab... |
| Pvap | 0.03 | kPa | 290.30 | Renewab... |
| Pvap | 0.03 | kPa | 291.80 | Renewab... |
| Pvap | 0.04 | kPa | 293.30 | Renewab... |
| Pvap | 0.04 | kPa | 296.20 | Renewab... |
| Pvap | 0.06 | kPa | 299.20 | Renewab... |
| Pvap | 0.07 | kPa | 302.20 | Renewab... |
| Pvap | 0.10 | kPa | 305.10 | Renewab... |
| Pvap | 0.11 | kPa | 308.10 | Renewab... |
| Pvap | 0.13 | kPa | 308.50 | Renewab... |
| Pvap | 0.15 | kPa | 311.00 | Renewab... |
| Pvap | 0.16 | kPa | 313.00 | Renewab... |
| Pvap | 0.19 | kPa | 314.50 | Renewab... |
| Pvap | 0.23 | kPa | 317.00 | Renewab... |
| Pvap | 0.25 | kPa | 318.90 | Renewab... |
| Pvap | 0.35 | kPa | 322.90 | Renewab... |
| n0 | 1.42180 | 293.15 | Vapor l... | |
| ρl | [937.32; 996.90] | kg/m3 | [278.15; 338.15] |
|
|
T(K) Liquid Density (kg/m3) 940 950 960 970 980 990 1000 280 300 320 | ||||
| ρl | 996.90 | kg/m3 | 278.15 | Thermop... |
| ρl | 994.47 | kg/m3 | 280.65 | Thermop... |
| ρl | 992.02 | kg/m3 | 283.15 | Thermop... |
| ρl | 989.58 | kg/m3 | 285.65 | Thermop... |
| ρl | 987.27 | kg/m3 | 288.15 | Experim... |
| ρl | 987.13 | kg/m3 | 288.15 | Thermop... |
| ρl | 984.67 | kg/m3 | 290.65 | Thermop... |
| ρl | 982.00 | kg/m3 | 293.15 | Investi... |
| ρl | 982.21 | kg/m3 | 293.15 | Thermop... |
| ρl | 981.50 | kg/m3 | 293.15 | Investi... |
| ρl | 982.37 | kg/m3 | 293.15 | Experim... |
| ρl | 979.75 | kg/m3 | 295.65 | Thermop... |
| ρl | 977.00 | kg/m3 | 298.15 | Investi... |
| ρl | 977.28 | kg/m3 | 298.15 | Self-ag... |
| ρl | 977.28 | kg/m3 | 298.15 | Thermop... |
| ρl | 977.45 | kg/m3 | 298.15 | Experim... |
| ρl | 974.81 | kg/m3 | 300.65 | Thermop... |
| ρl | 972.34 | kg/m3 | 303.15 | Thermop... |
| ρl | 972.51 | kg/m3 | 303.15 | Experim... |
| ρl | 973.10 | kg/m3 | 303.15 | Investi... |
| ρl | 969.86 | kg/m3 | 305.65 | Thermop... |
| ρl | 967.57 | kg/m3 | 308.15 | Experim... |
| ρl | 967.37 | kg/m3 | 308.15 | Thermop... |
| ρl | 968.40 | kg/m3 | 308.15 | Investi... |
| ρl | 964.89 | kg/m3 | 310.65 | Thermop... |
| ρl | 962.60 | kg/m3 | 313.15 | Experim... |
| ρl | 962.40 | kg/m3 | 313.15 | Thermop... |
| ρl | 963.50 | kg/m3 | 313.15 | Investi... |
| ρl | 959.90 | kg/m3 | 315.65 | Thermop... |
| ρl | 957.41 | kg/m3 | 318.15 | Thermop... |
| ρl | 958.50 | kg/m3 | 318.15 | Investi... |
| ρl | 957.62 | kg/m3 | 318.15 | Experim... |
| ρl | 954.91 | kg/m3 | 320.65 | Thermop... |
| ρl | 952.41 | kg/m3 | 323.15 | Thermop... |
| ρl | 953.90 | kg/m3 | 323.15 | Investi... |
| ρl | 952.63 | kg/m3 | 323.15 | Experim... |
| ρl | 949.90 | kg/m3 | 325.65 | Thermop... |
| ρl | 948.90 | kg/m3 | 328.15 | Investi... |
| ρl | 947.40 | kg/m3 | 328.15 | Thermop... |
| ρl | 944.88 | kg/m3 | 330.65 | Thermop... |
| ρl | 942.37 | kg/m3 | 333.15 | Thermop... |
| ρl | 944.10 | kg/m3 | 333.15 | Investi... |
| ρl | 939.85 | kg/m3 | 335.65 | Thermop... |
| ρl | 940.10 | kg/m3 | 338.15 | Investi... |
| ρl | 937.32 | kg/m3 | 338.15 | Thermop... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 992.75 |
| 288.15 | 100.00 | 987.86 |
| 293.15 | 100.00 | 982.96 |
| 298.15 | 100.00 | 977.96 |
| 303.15 | 100.00 | 973.09 |
| 308.15 | 100.00 | 967.74 |
| 313.15 | 100.00 | 963.05 |
| 318.15 | 100.00 | 957.98 |
| 323.15 | 100.00 | 952.44 |
| 328.15 | 100.00 | 947.31 |
| 333.15 | 100.00 | 942.28 |
| 338.15 | 100.00 | 937.09 |
| 283.15 | 2500.00 | 994.4 |
| 288.15 | 2500.00 | 989.52 |
| 293.15 | 2500.00 | 984.69 |
| 298.15 | 2500.00 | 979.83 |
| 303.15 | 2500.00 | 974.98 |
| 308.15 | 2500.00 | 970.01 |
| 313.15 | 2500.00 | 965.11 |
| 318.15 | 2500.00 | 960.06 |
| 323.15 | 2500.00 | 954.61 |
| 328.15 | 2500.00 | 949.44 |
| 333.15 | 2500.00 | 944.52 |
| 338.15 | 2500.00 | 939.39 |
| 283.15 | 5000.00 | 996.14 |
| 288.15 | 5000.00 | 991.32 |
| 293.15 | 5000.00 | 986.5 |
| 298.15 | 5000.00 | 981.74 |
| 303.15 | 5000.00 | 976.81 |
| 308.15 | 5000.00 | 971.95 |
| 313.15 | 5000.00 | 967.03 |
| 318.15 | 5000.00 | 962.11 |
| 323.15 | 5000.00 | 956.73 |
| 328.15 | 5000.00 | 951.63 |
| 333.15 | 5000.00 | 946.72 |
| 338.15 | 5000.00 | 941.78 |
| 283.15 | 7500.00 | 997.77 |
| 288.15 | 7500.00 | 993.09 |
| 293.15 | 7500.00 | 988.29 |
| 298.15 | 7500.00 | 983.49 |
| 303.15 | 7500.00 | 978.72 |
| 308.15 | 7500.00 | 973.85 |
| 313.15 | 7500.00 | 969.06 |
| 318.15 | 7500.00 | 964.16 |
| 323.15 | 7500.00 | 958.74 |
| 328.15 | 7500.00 | 953.79 |
| 333.15 | 7500.00 | 948.91 |
| 338.15 | 7500.00 | 943.99 |
| 283.15 | 10000.00 | 999.41 |
| 288.15 | 10000.00 | 994.7 |
| 293.15 | 10000.00 | 990.02 |
| 298.15 | 10000.00 | 985.26 |
| 303.15 | 10000.00 | 980.54 |
| 308.15 | 10000.00 | 975.59 |
| 313.15 | 10000.00 | 970.96 |
| 318.15 | 10000.00 | 966.04 |
| 323.15 | 10000.00 | 960.79 |
| 328.15 | 10000.00 | 955.86 |
| 333.15 | 10000.00 | 951.02 |
| 338.15 | 10000.00 | 946.05 |
| 283.15 | 20000.00 | 1005.87 |
| 288.15 | 20000.00 | 1001.18 |
| 293.15 | 20000.00 | 996.69 |
| 298.15 | 20000.00 | 992.04 |
| 303.15 | 20000.00 | 987.67 |
| 308.15 | 20000.00 | 982.84 |
| 313.15 | 20000.00 | 978.27 |
| 318.15 | 20000.00 | 973.62 |
| 323.15 | 20000.00 | 968.64 |
| 328.15 | 20000.00 | 963.73 |
| 333.15 | 20000.00 | 959.28 |
| 338.15 | 20000.00 | 954.42 |
| 283.15 | 30000.00 | 1011.69 |
| 288.15 | 30000.00 | 1007.12 |
| 293.15 | 30000.00 | 1002.96 |
| 298.15 | 30000.00 | 998.37 |
| 303.15 | 30000.00 | 993.96 |
| 308.15 | 30000.00 | 989.43 |
| 313.15 | 30000.00 | 985.03 |
| 318.15 | 30000.00 | 980.42 |
| 323.15 | 30000.00 | 975.86 |
| 328.15 | 30000.00 | 971.08 |
| 333.15 | 30000.00 | 966.7 |
| 338.15 | 30000.00 | 962.07 |
| 283.15 | 40000.00 | 1017.42 |
| 288.15 | 40000.00 | 1012.83 |
| 293.15 | 40000.00 | 1008.73 |
| 298.15 | 40000.00 | 1004.29 |
| 303.15 | 40000.00 | 1000.06 |
| 308.15 | 40000.00 | 995.62 |
| 313.15 | 40000.00 | 991.43 |
| 318.15 | 40000.00 | 986.96 |
| 323.15 | 40000.00 | 982.37 |
| 328.15 | 40000.00 | 977.8 |
| 333.15 | 40000.00 | 973.8 |
| 338.15 | 40000.00 | 969.19 |
| 283.15 | 50000.00 | 1022.85 |
| 288.15 | 50000.00 | 1018.14 |
| 293.15 | 50000.00 | 1014.33 |
| 298.15 | 50000.00 | 1009.82 |
| 303.15 | 50000.00 | 1005.69 |
| 308.15 | 50000.00 | 1001.41 |
| 313.15 | 50000.00 | 997.35 |
| 318.15 | 50000.00 | 993.12 |
| 323.15 | 50000.00 | 988.47 |
| 328.15 | 50000.00 | 984.21 |
| 333.15 | 50000.00 | 980.2 |
| 338.15 | 50000.00 | 975.64 |
| 283.15 | 60000.00 | 1027.71 |
| 288.15 | 60000.00 | 1023.26 |
| 293.15 | 60000.00 | 1019.37 |
| 298.15 | 60000.00 | 1015.17 |
| 303.15 | 60000.00 | 1011.27 |
| 308.15 | 60000.00 | 1007.05 |
| 313.15 | 60000.00 | 1002.99 |
| 318.15 | 60000.00 | 998.83 |
| 323.15 | 60000.00 | 994.3 |
| 328.15 | 60000.00 | 990.17 |
| 333.15 | 60000.00 | 986.43 |
| 338.15 | 60000.00 | 982.05 |
| Reference | ||
Similar Compounds
Find more compounds similar to Butyl lactate.
Mixtures
- 1-Butanol + Butyl lactate
- Butyl lactate + Water
- Butyl lactate + Sulfur dioxide
- 1-Propanol + Butyl lactate
- Propylene Glycol + Butyl lactate
- 1,3-Propanediol + Butyl lactate
- Carbon dioxide + Butyl lactate
- 1-Butanol + Butyl lactate + Water
Sources
- Crippen Method
- Crippen Method
- Vapor liquid equilibria and excess volumes of the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate at 101.325 kPa
- High-pressure phase behavior of propyl lactate and butyl lactate in supercritical carbon dioxide
- The pqT behaviour of the lactate family
- Self-aggregation of liquids from biomass in aqueous solution
- Feasibility of bio-based lactate esters as extractant for biobutanol recovery: (Liquid + liquid) equilibria
- Investigation of SO2 solubilities in some biobased solvents and their thermodynamic properties
- Renewable platform chemicals: Evaluation of thermochemical data of alkyl lactates with complementary experimental and computational methods
- Experimental measurements and modelling of volumetric properties, refractive index and viscosity of selected binary systems with butyl lactate at 288.15 to 323.15 K and atmospheric pressure. New UNIFAC-VISCO interaction parameters.
- Thermophysical Properties of Lactates
- Investigation of the Solubilities of Carbon Dioxide in Some Low Volatile Solvents and Their Thermodynamic Properties
- Joback Method
- McGowan Method
- NIST Webbook
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