- InChI
- InChI=1S/C10H7Cl/c11-10-7-3-5-8-4-1-2-6-9(8)10/h1-7H
- InChI Key
- JTPNRXUCIXHOKM-UHFFFAOYSA-N
- Formula
- C10H7Cl
- SMILES
- Clc1cccc2ccccc12
- Molecular Weight1
- 162.62
- CAS
- 90-13-1
- Other Names
-
- .alpha.-chloronaphthalene
- 1-CHLORONAPHTHALENE
- 1-Chlornaftalen
- 1-Chloronapthalene
- 1-NAPHTHYL CHLORIDE
- 1-Naphthalenyl chloride
- ALPHA-CHLORONAPHTHALENE
- Monochloro naphthalene
- NSC 6166
- alpha-Naphthyl chloride
- «alpha»-Chlornaphthalene
- «alpha»-Chloronaphthalene
- «alpha»-naphthyl chloride
- «alpha»-Chlornaphthalene
- «alpha»-Chloronaphthalene
- «alpha»-naphthyl chloride
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- 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).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ΔcH°liquid | -5009.20 ± 8.40 | kJ/mol | NIST |
| EA | 0.28 ± 0.00 | eV | NIST |
| ΔfG° | 230.82 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 115.00 ± 9.60 | kJ/mol | NIST |
| ΔfH°liquid | 49.80 ± 8.40 | kJ/mol | NIST |
| ΔfusH° | 16.52 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [62.00; 65.30] | kJ/mol |
|
| ΔvapH° | 64.70 | kJ/mol | NIST |
| ΔvapH° | 62.00 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 64.00 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 65.30 ± 5.00 | kJ/mol | NIST |
| IE | 8.13 | eV | NIST |
| log10WS | [-3.93; -3.93] |
|
|
| log10WS | -3.93 | Aq. Sol... | |
| log10WS | -3.93 | Estimat... | |
| logPoct/wat | 3.493 | Crippen Calculated Property | |
| McVol | 120.780 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 3655.35 | kPa | Joback Calculated Property |
| Inp | [236.15; 1382.00] |
|
|
| Inp | 1356.10 | NIST | |
| Inp | 1354.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1382.00 | NIST | |
| Inp | 1368.00 | NIST | |
| Inp | 1349.00 | NIST | |
| Inp | 236.62 | NIST | |
| Inp | 236.15 | NIST | |
| Inp | 236.90 | NIST | |
| Inp | 1356.10 | NIST | |
| I | [1962.00; 1962.00] |
|
|
| I | 1962.00 | NIST | |
| I | 1962.00 | NIST | |
| Tboil | 516.27 | K | Joback Calculated Property |
| Tc | 760.74 | K | Joback Calculated Property |
| Tfus | 270.70 ± 0.50 | K | NIST |
| Vc | 0.459 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [234.54; 294.46] | J/mol×K | [516.27; 760.74] |
|
| Cp,gas | 234.54 | J/mol×K | 516.27 | Joback Calculated Property |
| Cp,gas | 246.83 | J/mol×K | 557.01 | Joback Calculated Property |
| Cp,gas | 258.09 | J/mol×K | 597.76 | Joback Calculated Property |
| Cp,gas | 268.40 | J/mol×K | 638.50 | Joback Calculated Property |
| Cp,gas | 277.85 | J/mol×K | 679.25 | Joback Calculated Property |
| Cp,gas | 286.50 | J/mol×K | 719.99 | Joback Calculated Property |
| Cp,gas | 294.46 | J/mol×K | 760.74 | Joback Calculated Property |
| Cp,liquid | [211.28; 212.60] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 212.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 211.28 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 211.37 | J/mol×K | 298.15 | NIST |
| η | [0.0003504; 0.0015676] | Pa×s | [304.02; 516.27] |
|
| η | 0.0015676 | Pa×s | 304.02 | Joback Calculated Property |
| η | 0.0010722 | Pa×s | 339.39 | Joback Calculated Property |
| η | 0.0007878 | Pa×s | 374.77 | Joback Calculated Property |
| η | 0.0006105 | Pa×s | 410.14 | Joback Calculated Property |
| η | 0.0004927 | Pa×s | 445.52 | Joback Calculated Property |
| η | 0.0004103 | Pa×s | 480.89 | Joback Calculated Property |
| η | 0.0003504 | Pa×s | 516.27 | Joback Calculated Property |
| ΔfusH | [12.90; 12.90] | kJ/mol | [270.70; 270.70] |
|
| ΔfusH | 12.90 | kJ/mol | 270.70 | NIST |
| ΔfusH | 12.90 | kJ/mol | 270.70 | NIST |
| ΔvapH | [57.80; 59.60] | kJ/mol | [373.00; 453.00] |
|
| ΔvapH | 58.60 | kJ/mol | 373.00 | NIST |
| ΔvapH | 57.80 | kJ/mol | 417.50 | NIST |
| ΔvapH | 59.60 | kJ/mol | 453.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 385.20 | K | 0.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [393.75; 566.81] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.44380e+01 | |||
| Coefficient B | -4.44868e+03 | |||
| Coefficient C | -7.93600e+01 | |||
| Temperature range, min. | 393.75 | |||
| Temperature range, max. | 566.81 | |||
| Pvap | 1.33 | kPa | 393.75 | Calculated Property |
| Pvap | 3.01 | kPa | 412.98 | Calculated Property |
| Pvap | 6.23 | kPa | 432.21 | Calculated Property |
| Pvap | 11.96 | kPa | 451.44 | Calculated Property |
| Pvap | 21.52 | kPa | 470.67 | Calculated Property |
| Pvap | 36.66 | kPa | 489.89 | Calculated Property |
| Pvap | 59.53 | kPa | 509.12 | Calculated Property |
| Pvap | 92.74 | kPa | 528.35 | Calculated Property |
| Pvap | 139.31 | kPa | 547.58 | Calculated Property |
| Pvap | 202.66 | kPa | 566.81 | Calculated Property |
| Pvap | [1.26e-04; 3460.46] | kPa | [269.15; 785.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.48921e+02 | |||
| Coefficient B | -1.35878e+04 | |||
| Coefficient C | -1.93077e+01 | |||
| Coefficient D | 8.49730e-06 | |||
| Temperature range, min. | 269.15 | |||
| Temperature range, max. | 785.00 | |||
| Pvap | 1.26e-04 | kPa | 269.15 | Calculated Property |
| Pvap | 0.03 | kPa | 326.47 | Calculated Property |
| Pvap | 0.89 | kPa | 383.78 | Calculated Property |
| Pvap | 9.03 | kPa | 441.10 | Calculated Property |
| Pvap | 46.60 | kPa | 498.42 | Calculated Property |
| Pvap | 158.40 | kPa | 555.73 | Calculated Property |
| Pvap | 413.68 | kPa | 613.05 | Calculated Property |
| Pvap | 915.55 | kPa | 670.37 | Calculated Property |
| Pvap | 1831.54 | kPa | 727.68 | Calculated Property |
| Pvap | 3460.46 | kPa | 785.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Naphthalene, 1-chloro-.
Mixtures
- Naphthalene, 1-chloro- + Buckminsterfullerene
- Naphthalene, 1-chloro- + Octane + Thiophene, tetrahydro-, 1,1-dioxide
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Ternary Liquid-Liquid Equilibria for Systems of (Sulfolane + Toluene or Chloronaphthalene + Octane)
- Solubility of Bromoderivatives C60Brn (n = 6, 8, 24) in 1-Chloronaphthalene and 1-Bromonaphthalene in the Temperature Range (10 to 60) deg C
- Temperature Dependence of Solubility of Individual Light Fullerenes and Industrial Fullerene Mixture in 1-Chloronaphthalene and 1-Bromonaphthalene
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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