- InChI
- InChI=1S/C12H10O2/c13-12(14)8-10-6-3-5-9-4-1-2-7-11(9)10/h1-7H,8H2,(H,13,14)
- InChI Key
- PRPINYUDVPFIRX-UHFFFAOYSA-N
- Formula
- C12H10O2
- SMILES
- O=C(O)Cc1cccc2ccccc12
- Molecular Weight1
- 186.21
- CAS
- 86-87-3
- Other Names
-
- 1-Naphthtaleneacetic acid
- 1-Naphthylacetic acid
- 1-naphthaceneacetic acid
- 1-naphthaleneethanoic acid
- 2-(1-Naphthyl)acetic acid
- ANU
- Agronaa
- Alman
- Alphaspra
- Appl-Set
- Biokor
- Celmone
- Etifix
- Fruitofix
- Fruitone N
- Klingtite
- Liqui-Stik
- N 10
- NAA
- NSC 15772
- Nafusaku
- Naphthalene-1-acetic acid
- Naphthaleneacetic acid
- Naphthylacetic acid
- Naphyl-1-essigsaeure
- Niagara-Stik
- Nu-Tone
- Phymone
- Phyomone
- Pimacol-Sol
- Planofix
- Planofixe
- Pomoxon
- Primacol
- Rasin
- Rhizopon B
- Rhodofix
- Stafast
- Stop-Drop
- Tekkam
- Tip-Off
- Transplantone
- Tre-hold
- Vardhak
- ethanoic acid, 1-naphthalene-
- «alpha»-NAA
- «alpha»-Naphthaleneacetic acid
- «alpha»-Naphthylacetic acid
- «alpha»-Naphthyleneacetic 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).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid 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).
- ΔsubH° : Enthalpy of sublimation at standard conditions (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).
- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.7179 | Relay (1.0) Calculated Property | |
| ΔcH°solid | -5792.09 ± 0.79 | kJ/mol | NIST |
| ΔfH°gas | -249.61 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | -359.19 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 27.65 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 112.30 ± 0.90 | kJ/mol | NIST |
| ΔvapH° | 94.25 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [7.71; 7.99] | eV |
|
| IE | 7.71 | eV | NIST |
| IE | 7.99 | eV | NIST |
| log10WS | -2.65 | Aq. Solubility Prediction | |
| logPoct/wat | 2.467 | Crippen Calculated Property | |
| McVol | 144.160 | ml/mol | McGowan Calculated Property |
| Pc | 3380.21 | kPa | Joback Calculated Property |
| Tboil | 609.13 | K | Relay (1.0) Calculated Property |
| Tc | 895.79 | K | Relay (1.0) Calculated Property |
| Tfus | [403.06; 406.48] | K |
|
| Tfus | 403.06 | K | Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K |
| Tfus | 406.48 | K | Aq. Solubility Prediction |
| Tfus | 405.95 ± 0.20 | K | NIST |
| Vc | 0.518 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate Standard Gibbs free energy of formation for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [22.26; 22.26] | kJ/mol | [405.30; 405.30] |
|
| ΔfusH | 22.26 | kJ/mol | 405.30 | NIST |
| ΔfusH | 22.26 | kJ/mol | 405.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [177.97; 436.85] | 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 | -5.44690e+01 | |||
| Coefficient B | 1.05250e+00 | |||
| Coefficient C | -8.02480e-04 | |||
| Coefficient D | 2.41300e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 177.97 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 228.13 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 271.16 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 307.83 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 338.89 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 365.11 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 387.26 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 406.09 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 422.36 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 436.85 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0019195; 0.0003494] | Pa×s | [405.16; 637.49] |
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 | -1.09301e+01 | |||
| Coefficient B | 1.89390e+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. | 405.16 | |||
| Temperature range, max. | 637.49 | |||
| η | 0.0019195 | Pa×s | 405.16 | Calculated Property |
| η | 0.0014507 | Pa×s | 430.98 | Calculated Property |
| η | 0.0011317 | Pa×s | 456.79 | Calculated Property |
| η | 0.0009066 | Pa×s | 482.61 | Calculated Property |
| η | 0.0007428 | Pa×s | 508.42 | Calculated Property |
| η | 0.0006205 | Pa×s | 534.23 | Calculated Property |
| η | 0.0005269 | Pa×s | 560.05 | Calculated Property |
| η | 0.0004540 | Pa×s | 585.86 | Calculated Property |
| η | 0.0003961 | Pa×s | 611.68 | Calculated Property |
| η | 0.0003494 | Pa×s | 637.49 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Naphthaleneacetic acid.
Mixtures
- 1-Naphthaleneacetic acid + Methyl Alcohol
- Ethanol + 1-Naphthaleneacetic acid
- 2-Propanol + 1-Naphthaleneacetic acid
- Toluene + 1-Naphthaleneacetic acid
- 1-Naphthaleneacetic acid + Acetone
- Acetonitrile + 1-Naphthaleneacetic acid
- 1-Naphthaleneacetic acid + 1,4-Dioxane
- 1-Naphthaleneacetic acid + Ethane, 1,2-dichloro-
- 1-Naphthaleneacetic acid + Ethyl Acetate
- 1-Naphthaleneacetic acid + Tetrahydrofuran
- 1-Naphthaleneacetic acid + Methyl Alcohol + Water
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
- Joback Method
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
These property values are available through the Cheméo API. A free account gives you an access key.