- InChI
- InChI=1S/C10H12/c1-8-4-2-5-9-6-3-7-10(8)9/h2,4-5H,3,6-7H2,1H3
- InChI Key
- LNNSODHYZXCEJP-UHFFFAOYSA-N
- Formula
- C10H12
- SMILES
- Cc1cccc2c1CCC2
- Molecular Weight1
- 132.21
- CAS
- 824-22-6
- Other Names
-
- 2,3-dihydro-4-methyl-1H-indene
- 4-Methylindan
- 4-Methylindane
- 4-methyl-2,3-dihydro-1H-indene
- Indan, 4-methyl-
- ω : Acentric Factor.
- 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).
- 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).
- 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 |
|---|---|---|---|
| ω | 0.3623 | Relay (1.0) Calculated Property | |
| ΔfG° | 194.93 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 25.56 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 11.98 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 54.27 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.36 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.37 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.484 | Crippen Calculated Property | |
| McVol | 117.140 | ml/mol | McGowan Calculated Property |
| Pc | 3403.91 | kPa | Joback Calculated Property |
| Inp | [1120.60; 1157.00] |
|
|
| Inp | 1144.00 | NIST | |
| Inp | 1120.60 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1122.00 | NIST | |
| Inp | 1126.00 | NIST | |
| Inp | 1133.65 | NIST | |
| Inp | 1141.60 | NIST | |
| Inp | 1147.70 | NIST | |
| Inp | 1151.40 | NIST | |
| Inp | 1141.60 | NIST | |
| Inp | 1147.70 | NIST | |
| Inp | 1151.40 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1138.00 | NIST | |
| Inp | 1142.00 | NIST | |
| Inp | 1146.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1121.00 | NIST | |
| I | [1467.90; 1506.00] |
|
|
| I | 1467.90 | NIST | |
| I | 1506.00 | NIST | |
| I | 1468.00 | NIST | |
| I | 1468.00 | NIST | |
| Tboil | 480.77 | K | Relay (1.0) Calculated Property |
| Tc | 714.60 | K | Relay (1.0) Calculated Property |
| Tfus | 234.55 | K | Relay (1.0) Calculated Property |
| Vc | 0.435 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [139.76; 383.71] | 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 | -6.76900e+01 | |||
| Coefficient B | 9.33320e-01 | |||
| Coefficient C | -6.92920e-04 | |||
| Coefficient D | 2.11000e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 139.76 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 185.12 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 224.35 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 258.14 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 287.14 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 312.02 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 333.45 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 352.10 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 368.63 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 383.71 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0015225; 0.0003571] | Pa×s | [276.10; 491.01] |
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 | -9.80064e+00 | |||
| Coefficient B | 9.14790e+02 | |||
| 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. | 276.10 | |||
| Temperature range, max. | 491.01 | |||
| η | 0.0015225 | Pa×s | 276.10 | Calculated Property |
| η | 0.0011696 | Pa×s | 299.98 | Calculated Property |
| η | 0.0009341 | Pa×s | 323.86 | Calculated Property |
| η | 0.0007694 | Pa×s | 347.74 | Calculated Property |
| η | 0.0006497 | Pa×s | 371.62 | Calculated Property |
| η | 0.0005600 | Pa×s | 395.50 | Calculated Property |
| η | 0.0004909 | Pa×s | 419.37 | Calculated Property |
| η | 0.0004365 | Pa×s | 443.25 | Calculated Property |
| η | 0.0003928 | Pa×s | 467.13 | Calculated Property |
| η | 0.0003571 | Pa×s | 491.01 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [350.03; 509.25] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41478e+01 | |||
| Coefficient B | -3.88133e+03 | |||
| Coefficient C | -7.00000e+01 | |||
| Temperature range, min. | 350.03 | |||
| Temperature range, max. | 509.25 | |||
| Pvap | 1.33 | kPa | 350.03 | Calculated Property |
| Pvap | 3.04 | kPa | 367.72 | Calculated Property |
| Pvap | 6.31 | kPa | 385.41 | Calculated Property |
| Pvap | 12.13 | kPa | 403.10 | Calculated Property |
| Pvap | 21.83 | kPa | 420.79 | Calculated Property |
| Pvap | 37.14 | kPa | 438.49 | Calculated Property |
| Pvap | 60.17 | kPa | 456.18 | Calculated Property |
| Pvap | 93.45 | kPa | 473.87 | Calculated Property |
| Pvap | 139.87 | kPa | 491.56 | Calculated Property |
| Pvap | 202.66 | kPa | 509.25 | Calculated Property |
Similar Compounds
Find more compounds similar to 1H-Indene, 2,3-dihydro-4-methyl-.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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