- InChI
- InChI=1S/C3H6O3/c1-2(4)3(5)6/h2,4H,1H3,(H,5,6)
- InChI Key
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N
- Formula
- C3H6O3
- SMILES
- CC(O)C(=O)O
- Molecular Weight1
- 90.08
- CAS
- 50-21-5
- Other Names
-
- (.+-.)-lactic acid
- (.+/-.)-Lactic acid
- .alpha.-hydroxypropanoic acid
- .alpha.-hydroxypropionic acid
- 1-Hydroxyethane 1-carboxylic acid
- 1-Hydroxyethanecarboxylic acid
- 2-hydroxypropanoic acid
- 2-hydroxypropionic acid
- Ethylidenelactic acid
- Kyselina 2-hydroxypropanova
- Kyselina mlecna
- Milchsaure
- NSC 367919
- Ordinary lactic acid
- Propionic acid, 2-hydroxy-
- Purac FCC 80
- Racemic lactic acid
- biolac
- chem-cast
- dl-lactic acid
- milk acid
- propanoic acid, 2-hydroxy-
- tonsillosan
- «alpha»-Hydroxypropanoic acid
- «alpha»-Hydroxypropionic acid
- ω : Acentric Factor.
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- 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).
- 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-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 |
|---|---|---|---|
| ω | 0.6920 | Relay (1.0) Calculated Property | |
| ΔcH°solid | -1362.80 | kJ/mol | NIST |
| Tflash,cc | 383.15 | K | NCMS SOLV-DB |
| ΔfG° | -508.79 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -635.84 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 14.23 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 72.56 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 10.62 | eV | Relay (1.0) Calculated Property |
| log10WS | 1.30 | Relay (1.0) Calculated Property | |
| logPoct/wat | -1.810 | NCMS SOLV-DB | |
| McVol | 66.440 | ml/mol | McGowan Calculated Property |
| Pc | 5765.39 | kPa | Joback Calculated Property |
| Inp | [838.00; 838.00] |
|
|
| Inp | 838.00 | NIST | |
| Inp | 838.00 | NIST | |
| Tboil | [356.65; 398.20] | K |
|
| Tboil | 398.20 | K | Liquid-liquid equilibria of water + lactic acid + methyl isobutyl ketone |
| Tboil | 356.65 | K | NCMS SOLV-DB |
| Tc | 673.58 | K | Relay (1.0) Calculated Property |
| Tfus | [290.00; 291.15] | K |
|
| Tfus | 290.00 | K | The phase envelopes of alternative solvents (ionic liquid, CO2) and building blocks of biomass origin (lactic acid, propionic acid) |
| Tfus | 291.15 | K | NCMS SOLV-DB |
| Tfus | 290.00 ± 2.00 | K | NIST |
| Ttriple | 290.00 ± 0.20 | K | NIST |
| Vc | 0.257 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | 11.34 | kJ/mol | 289.90 | NIST |
| n0 | [1.42600; 1.43940] | [293.15; 298.15] |
|
|
| n0 | 1.43940 | 293.15 | (Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems | |
| n0 | 1.42600 | 298.15 | NCMS SOLV-DB | |
| ρl | [1199.91; 1202.57] | kg/m3 | [298.15; 298.20] |
|
| ρl | 1202.57 | kg/m3 | 298.15 | Extraction of Carboxylic Acids from Aqueous Solutions by Using [BMim][NTf2] and Salting-out Agents |
| ρl | 1199.91 | kg/m3 | 298.20 | Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [94.93; 204.09] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 8.37000e+00 | |||
| Coefficient B | 3.79520e-01 | |||
| Coefficient C | -2.45600e-04 | |||
| Coefficient D | 6.18000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 94.93 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 114.63 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 131.99 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 147.18 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 160.42 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 171.90 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 181.81 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 190.35 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 197.71 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 204.09 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0161406; 0.0002129] | Pa×s | [290.38; 486.37] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.48683e+01 | |||
| Coefficient B | 3.11927e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 290.38 | |||
| Temperature range, max. | 486.37 | |||
| η | 0.0161406 | Pa×s | 290.38 | Calculated Property |
| η | 0.0076293 | Pa×s | 312.16 | Calculated Property |
| η | 0.0039764 | Pa×s | 333.93 | Calculated Property |
| η | 0.0022447 | Pa×s | 355.71 | Calculated Property |
| η | 0.0013535 | Pa×s | 377.49 | Calculated Property |
| η | 0.0008624 | Pa×s | 399.26 | Calculated Property |
| η | 0.0005758 | Pa×s | 421.04 | Calculated Property |
| η | 0.0004000 | Pa×s | 442.81 | Calculated Property |
| η | 0.0002875 | Pa×s | 464.59 | Calculated Property |
| η | 0.0002129 | Pa×s | 486.37 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [379.47; 584.23] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.23768e+01 | |||
| Coefficient B | -3.48122e+03 | |||
| Coefficient C | -9.15110e+01 | |||
| Temperature range, min. | 379.47 | |||
| Temperature range, max. | 584.23 | |||
| Pvap | 1.33 | kPa | 379.47 | Calculated Property |
| Pvap | 3.23 | kPa | 402.22 | Calculated Property |
| Pvap | 6.94 | kPa | 424.97 | Calculated Property |
| Pvap | 13.52 | kPa | 447.72 | Calculated Property |
| Pvap | 24.30 | kPa | 470.47 | Calculated Property |
| Pvap | 40.89 | kPa | 493.23 | Calculated Property |
| Pvap | 65.07 | kPa | 515.98 | Calculated Property |
| Pvap | 98.75 | kPa | 538.73 | Calculated Property |
| Pvap | 143.95 | kPa | 561.48 | Calculated Property |
| Pvap | 202.65 | kPa | 584.23 | Calculated Property |
| Pvap | [6.49e-03; 6753.41] | kPa | [291.15; 616.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.15361e+02 | |||
| Coefficient B | -1.18844e+04 | |||
| Coefficient C | -1.41753e+01 | |||
| Coefficient D | 1.00178e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 291.15 | |||
| Temperature range, max. | 616.00 | |||
| Pvap | 6.49e-03 | kPa | 291.15 | Calculated Property |
| Pvap | 0.14 | kPa | 327.24 | Calculated Property |
| Pvap | 1.50 | kPa | 363.34 | Calculated Property |
| Pvap | 9.93 | kPa | 399.43 | Calculated Property |
| Pvap | 46.37 | kPa | 435.53 | Calculated Property |
| Pvap | 168.07 | kPa | 471.62 | Calculated Property |
| Pvap | 505.01 | kPa | 507.72 | Calculated Property |
| Pvap | 1319.35 | kPa | 543.81 | Calculated Property |
| Pvap | 3104.12 | kPa | 579.91 | Calculated Property |
| Pvap | 6753.41 | kPa | 616.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Lactic acid.
Mixtures
- Proline + Lactic acid
- Betaine + Lactic acid
- Betaine + Lactic acid + Water
- Lactic acid + Carbon dioxide
- Lactic acid + 1-Butanol + Water
- Lactic acid + 1-Pentanol + Water
- Lactic acid + 1-Hexanol + Water
- Methyl Isobutyl Ketone + Lactic acid + Water
- Lactic acid + 1-Decanol + Water
- Lactic acid + 1-Octanol + Water
- Lactic acid + Choline chloride
- Lactic acid + Choline chloride + Water
- Lactic acid + Choline chloride + Carbon dioxide
- Toluene + Lactic acid + Tridodecylamine
- Lactic acid + 1-Octanol + Tridodecylamine
- Methyl Isobutyl Ketone + Lactic acid + Tridodecylamine
- Lactic acid + Tridodecylamine + Pentane, 2,2,4-trimethyl-
- Lactic acid + Tridodecylamine + Cyclohexane
- Monoethanolamine + Lactic acid + M-(2-Hydroxyethyl)lactamide
- Lactic acid + Guanidine, N,N,N',N'-tetramethyl-
Find more mixtures with Lactic acid.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- The phase envelopes of alternative solvents (ionic liquid, CO2) and building blocks of biomass origin (lactic acid, propionic acid)
- A new low transition temperature mixture (LTTM) formed by choline chloride + lactic acid: Characterization as solvent for CO2 capture
- Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
- Liquid-liquid equilibria of water + lactic acid + methyl isobutyl ketone
- Acoustic, volumetric, transport, optical and rheological properties of benzyltripropylammonium based Deep Eutectic Solvents
- (Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems
- Physical properties of seven deep eutectic solvents based on L-proline or betaine
- Specific Heat Capacities of Two Functional Ionic Liquids and Two Functional Deep Eutectic Solvents for the Absorption of SO2
- Synthesis and Physical and Thermodynamic Properties of Lactic Acid and Malic Acid-Based Natural Deep Eutectic Solvents
- Extraction of Carboxylic Acids from Aqueous Solutions by Using [BMim][NTf2] and Salting-out Agents
- Vapor Liquid Equilibria of the Mixtures Involved in the Esterification of Lactic Acid with Methanol
- Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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