- InChI
- InChI=1S/C3H6Cl2O/c4-1-3(6)2-5/h3,6H,1-2H2
- InChI Key
- DEWLEGDTCGBNGU-UHFFFAOYSA-N
- Formula
- C3H6Cl2O
- SMILES
- OC(CCl)CCl
- Molecular Weight1
- 128.99
- CAS
- 96-23-1
- Other Names
-
- .alpha.,.gamma.-dichlorohydrin
- .alpha.-dichlorohydrin
- 1,3-Dichloro-2-hydroxypropane
- 1,3-Dichloro-2-propanol
- 1,3-Dichlorohydrin
- 1,3-Dichloroisopropanol
- 1,3-Dichloroisopropyl alcohol
- 1,3-Dichloropropan-2-ol
- 1,3-Dichloropropanol-2
- 2-Chloro-1-(chloromethyl)ethanol
- Dichlorohydrin
- Enodrin
- Glycerol 1,3-dichlorohydrin
- Glycerol «alpha»,«gamma»-dichlorohydrin
- Glycerol «alpha»,«gamma»-dichlorohydrin
- NSC 70982
- Propylene dichlorohydrin
- S-Dichloroisopropyl alcohol
- S-Glycerol dichlorohydrin
- U 25,354
- UN 2750
- glycerol-.alpha.,.gamma.-dichlorohydrin
- glycerol-1,3-dichlorohydrin
- sym-Dichloroisopropyl alcohol
- sym-Glycerol dichlorohydrin
- «alpha»,«gamma»-Dichlorohydrin
- «alpha»-Dichlorohydrin
- «alpha»,«gamma»-Dichlorohydrin
- «alpha»-Dichlorohydrin
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- ΔfH°liquid : Liquid phase 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).
- 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 |
|---|---|---|---|
| ΔcH°liquid | [-1701.06; -1700.00] | kJ/mol |
|
| ΔcH°liquid | -1700.00 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -1701.06 ± 0.12 | kJ/mol | NIST |
| ΔfG° | -188.74 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -294.24 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -385.00 ± 1.00 | kJ/mol | NIST |
| ΔfusH° | 12.49 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 47.33 | kJ/mol | Joback Calculated Property |
| log10WS | -0.11 | Aq. Sol... | |
| logPoct/wat | 0.825 | Crippen Calculated Property | |
| McVol | 83.480 | ml/mol | McGowan Calculated Property |
| Pc | 4565.38 | kPa | Joback Calculated Property |
| Inp | [852.90; 885.00] |
|
|
| Inp | 852.90 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 885.00 | NIST | |
| I | 1765.00 | NIST | |
| Tboil | [447.00; 448.30] | K |
|
| Tboil | 447.50 | K | NIST |
| Tboil | 447.00 | K | NIST |
| Tboil | 448.30 ± 0.50 | K | NIST |
| Tboil | 448.30 ± 0.50 | K | NIST |
| Tboil | 448.30 ± 0.50 | K | NIST |
| Tc | 615.83 | K | Joback Calculated Property |
| Tfus | 229.23 | K | Joback Calculated Property |
| Vc | 0.315 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [142.19; 171.37] | J/mol×K | [434.64; 615.83] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 140 145 150 155 160 165 170 450 500 550 600 | ||||
| Cp,gas | 142.19 | J/mol×K | 434.64 | Joback Calculated Property |
| Cp,gas | 147.67 | J/mol×K | 464.84 | Joback Calculated Property |
| Cp,gas | 152.89 | J/mol×K | 495.04 | Joback Calculated Property |
| Cp,gas | 157.86 | J/mol×K | 525.23 | Joback Calculated Property |
| Cp,gas | 162.59 | J/mol×K | 555.43 | Joback Calculated Property |
| Cp,gas | 167.09 | J/mol×K | 585.63 | Joback Calculated Property |
| Cp,gas | 171.37 | J/mol×K | 615.83 | Joback Calculated Property |
| η | [0.0003215; 0.0828767] | Pa×s | [229.23; 434.64] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.02 0.04 0.06 0.08 250 300 350 400 | ||||
| η | 0.0828767 | Pa×s | 229.23 | Joback Calculated Property |
| η | 0.0180080 | Pa×s | 263.47 | Joback Calculated Property |
| η | 0.0055588 | Pa×s | 297.70 | Joback Calculated Property |
| η | 0.0021867 | Pa×s | 331.94 | Joback Calculated Property |
| η | 0.0010242 | Pa×s | 366.17 | Joback Calculated Property |
| η | 0.0005461 | Pa×s | 400.40 | Joback Calculated Property |
| η | 0.0003215 | Pa×s | 434.64 | Joback Calculated Property |
| ΔvapH | 50.40 | kJ/mol | 374.50 | NIST |
| ρl | [1332.47; 1362.66] | kg/m3 | [293.15; 318.15] |
|
|
T(K) Liquid Density (kg/m3) 1330 1335 1340 1345 1350 1355 1360 1365 300 310 | ||||
| ρl | 1362.66 | kg/m3 | 293.15 | The stu... |
| ρl | 1356.46 | kg/m3 | 298.15 | Volumet... |
| ρl | 1356.74 | kg/m3 | 298.15 | The stu... |
| ρl | 1350.55 | kg/m3 | 303.15 | Volumet... |
| ρl | 1350.72 | kg/m3 | 303.15 | The stu... |
| ρl | 1344.61 | kg/m3 | 308.15 | Volumet... |
| ρl | 1344.71 | kg/m3 | 308.15 | The stu... |
| ρl | 1338.56 | kg/m3 | 313.15 | Volumet... |
| ρl | 1338.65 | kg/m3 | 313.15 | The stu... |
| ρl | 1332.47 | kg/m3 | 318.15 | Volumet... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [337.47; 472.51] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.72693e+01 | |||
| Coefficient B | -5.45806e+03 | |||
| Coefficient C | -1.60670e+01 | |||
| Temperature range, min. | 337.47 | |||
| Temperature range, max. | 472.51 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 337.47 | Calculated Property |
| Pvap | 2.84 | kPa | 352.47 | Calculated Property |
| Pvap | 5.68 | kPa | 367.48 | Calculated Property |
| Pvap | 10.74 | kPa | 382.48 | Calculated Property |
| Pvap | 19.29 | kPa | 397.49 | Calculated Property |
| Pvap | 33.15 | kPa | 412.49 | Calculated Property |
| Pvap | 54.78 | kPa | 427.50 | Calculated Property |
| Pvap | 87.36 | kPa | 442.50 | Calculated Property |
| Pvap | 134.97 | kPa | 457.51 | Calculated Property |
| Pvap | 202.66 | kPa | 472.51 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Propanol, 1,3-dichloro-.
Mixtures
- 2-Propanol, 1,3-dichloro- + 2-Propen-1-ol
- 2-Propanol, 1,3-dichloro- + Acetic acid ethenyl ester
- 2-Propanol, 1,3-dichloro- + Ethyl Acetate
- 2-Propanol, 1,3-dichloro- + Acetic acid, 1,1-dimethylethyl ester
- 2-Propanol, 1,3-dichloro- + Water
Sources
- Crippen Method
- Volumetric properties for binary and ternary mixtures of allyl alcohol, 1,3-dichloro-2-propanol and 1-ethyl-3-methyl imidazolium ethyl sulfate [Emim][EtSO4] from T = 298.15 to 318.15 K at ambient pressure
- The study of excess molar volumes and related properties for binary mixtures containing benzyl alcohol and 1,3-dichloro-2-propanol with vinyl acetate, ethyl acetate and t-butyl acetate at T = 293.15 to 313.15 K and P = 0.087 MPa
- Liquid Liquid Equilibria for the System Water + 1,3-Dichloro-2-propanol + Epichlorohydrin from (283.2 to 303.2) K
- Joback Method
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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