Chemical Properties of Propane, 2,3-dichloro-1,1,1-trifluoro- (CAS 338-75-0)

InChI

InChI=1S/C3H3Cl2F3/c4-1-2(5)3(6,7)8/h2H,1H2

InChI Key

QJMGASHUZRHZBT-UHFFFAOYSA-N

Formula

C3H3Cl2F3

SMILES

FC(F)(F)C(Cl)CCl

Molecular Weight¹

166.96

CAS

338-75-0

Other Names

• 2,3-dichloro-1,1,1-trifluoropropane
• R-243db

• C_p,gas : Ideal gas heat capacity (J/mol×K).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• IE : Ionization energy (eV).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ΔfusH°	10.22	kJ/mol	Joback Calculated Property
ΔvapH°	32.38	kJ/mol	Relay (1.0) Calculated Property
IE	11.45	eV	Relay (1.0) Calculated Property
logPoct/wat	2.395		Crippen Calculated Property
McVol	82.920	ml/mol	McGowan Calculated Property
Pc	3509.58	kPa	Joback Calculated Property
Tboil	[349.50; 349.90]	K
Tboil	349.90 ± 0.50	K	NIST
Tboil	349.50 ± 0.50	K	NIST
Tc	525.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value

Cheméo can also estimate Normal melting (fusion) point, Critical Volume, Enthalpy of formation at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ρl	[1382.30; 1500.80]	kg/m3	[273.15; 333.15]
ρl	1500.80	kg/m3	273.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1496.80	kg/m3	275.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1493.10	kg/m3	277.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1489.30	kg/m3	279.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1485.30	kg/m3	281.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1481.30	kg/m3	283.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1477.60	kg/m3	285.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1473.90	kg/m3	287.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1470.10	kg/m3	289.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1466.30	kg/m3	291.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1462.30	kg/m3	293.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1458.40	kg/m3	295.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1454.50	kg/m3	297.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1450.60	kg/m3	299.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1446.60	kg/m3	301.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1442.70	kg/m3	303.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1438.70	kg/m3	305.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1434.70	kg/m3	307.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1430.80	kg/m3	309.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1426.80	kg/m3	311.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1422.80	kg/m3	313.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1418.80	kg/m3	315.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1414.80	kg/m3	317.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1410.80	kg/m3	319.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1406.70	kg/m3	321.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1402.70	kg/m3	323.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1398.60	kg/m3	325.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1394.50	kg/m3	327.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1390.40	kg/m3	329.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1386.30	kg/m3	331.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
ρl	1382.30	kg/m3	333.15	Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[118.75; 213.86]	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			1.80610e+01
Coefficient B			4.69500e-01
Coefficient C			-4.04400e-04
Coefficient D			1.30700e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	118.75	J/mol×K	273.00	Calculated Property
Cp,gas	139.33	J/mol×K	353.78	Calculated Property
Cp,gas	156.44	J/mol×K	434.56	Calculated Property
Cp,gas	170.50	J/mol×K	515.33	Calculated Property
Cp,gas	181.92	J/mol×K	596.11	Calculated Property
Cp,gas	191.11	J/mol×K	676.89	Calculated Property
Cp,gas	198.48	J/mol×K	757.67	Calculated Property
Cp,gas	204.46	J/mol×K	838.44	Calculated Property
Cp,gas	209.45	J/mol×K	919.22	Calculated Property
Cp,gas	213.86	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[259.60; 371.67]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.52312e+01
Coefficient B			-3.30686e+03
Coefficient C			-3.83110e+01
Temperature range, min.			259.60
Temperature range, max.			371.67
Pvap	1.33	kPa	259.60	Calculated Property
Pvap	2.96	kPa	272.05	Calculated Property
Pvap	6.05	kPa	284.50	Calculated Property
Pvap	11.54	kPa	296.96	Calculated Property
Pvap	20.76	kPa	309.41	Calculated Property
Pvap	35.48	kPa	321.86	Calculated Property
Pvap	57.94	kPa	334.31	Calculated Property
Pvap	90.97	kPa	346.77	Calculated Property
Pvap	137.89	kPa	359.22	Calculated Property
Pvap	202.63	kPa	371.67	Calculated Property

Similar Compounds

Find more compounds similar to Propane, 2,3-dichloro-1,1,1-trifluoro-.

Sources

• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 ChEDL chemicals 1.5.2, from Marsh, K. N.; Abramson, A.; Ambrose, D.; Morton, D. W.; Nikitin, E.; Tsonopoulos, C.; Young, C. L. Vapor-Liquid Critical Properties of Elements and Compounds. 10. Organic Compounds Containing Halogens. J. Chem. Eng. Data 2007, 52, 1509-1538.
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Measurements of Density, Viscosity, and Vapor Pressure for 1,1,1-Trifluoro-2,3-dichloropropane
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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