Chemical Properties of Hexane, 1-chloro- (CAS 544-10-5)

InChI

InChI=1S/C6H13Cl/c1-2-3-4-5-6-7/h2-6H2,1H3

InChI Key

MLRVZFYXUZQSRU-UHFFFAOYSA-N

Formula

C6H13Cl

SMILES

CCCCCCCl

Molecular Weight¹

120.62

CAS

544-10-5

Other Names

• 1-Chlorohexane
• 1-Hexyl chloride
• Hexyl chloride
• N-HEXYL CHLORIDE

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• c_sound,fluid : Speed of sound in fluid (m/s).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.3746		Relay (1.0) Calculated Property
ΔfG°	-12.29	kJ/mol	Joback Calculated Property
ΔfH°gas	-201.61	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	15.49	kJ/mol	Joback Calculated Property
ΔvapH°	[42.00; 42.86]	kJ/mol
ΔvapH°	42.86	kJ/mol	NIST
ΔvapH°	Outlier 42.00	kJ/mol	NIST
ΔvapH°	42.83	kJ/mol	NIST
ΔvapH°	42.80 ± 0.10	kJ/mol	NIST
ΔvapH°	42.80 ± 0.10	kJ/mol	NIST
ΔvapH°	42.82 ± 0.06	kJ/mol	NIST
IE	[10.28; 10.31]	eV
IE	10.31	eV	NIST
IE	10.28 ± 0.05	eV	NIST
log10WS	[-3.12; -3.12]
log10WS	-3.12		Aq. Solubility Prediction
log10WS	-3.12		Estimated Solubility
logPoct/wat	2.806		Crippen Calculated Property
McVol	107.640	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
Pc	2982.79	kPa	Joback Calculated Property
Inp	[833.30; 859.70]
Inp	840.10		NIST
Inp	838.80		NIST
Inp	839.50		NIST
Inp	837.40		NIST
Inp	835.00		NIST
Inp	833.70		NIST
Inp	836.70		NIST
Inp	840.90		NIST
Inp	843.70		NIST
Inp	842.90		NIST
Inp	844.00		NIST
Inp	842.90		NIST
Inp	844.60		NIST
Inp	858.20		NIST
Inp	859.70		NIST
Inp	857.00		NIST
Inp	833.30		NIST
Inp	838.30		NIST
Inp	835.00		NIST
Inp	858.00		NIST
Inp	835.90		NIST
Inp	857.10		NIST
Inp	840.00		NIST
Inp	858.00		NIST
Inp	844.00		NIST
Inp	848.00		NIST
Inp	844.00		NIST
Inp	846.00		NIST
Inp	857.00		NIST
Inp	847.00		NIST
Inp	850.00		NIST
Inp	853.00		NIST
Inp	845.00		NIST
Inp	845.00		NIST
Inp	844.00		NIST
Inp	844.00		NIST
Inp	844.00		NIST
Inp	848.00		NIST
Inp	850.00		NIST
I	[1034.00; 1050.00]
I	Outlier 1034.00		NIST
I	1041.00		NIST
I	1041.00		NIST
I	1050.00		NIST
I	1047.00		NIST
I	1049.00		NIST
I	1050.00		NIST
I	1050.00		NIST
Tboil	[407.45; 408.22]	K
Tboil	407.45	K	KDB
Tboil	407.70	K	NIST
Tboil	408.22 ± 0.08	K	NIST
Tboil	408.10	K	NIST
Tboil	407.45 ± 0.30	K	NIST
Tc	594.60	K	NIST
Tfus	179.15 ± 1.20	K	NIST
Vc	0.410	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[185.96; 242.42]	J/mol×K	[374.11; 546.35]
Cp,gas	185.96	J/mol×K	374.11	Joback Calculated Property
Cp,gas	196.32	J/mol×K	402.82	Joback Calculated Property
Cp,gas	206.29	J/mol×K	431.52	Joback Calculated Property
Cp,gas	215.87	J/mol×K	460.23	Joback Calculated Property
Cp,gas	225.08	J/mol×K	488.94	Joback Calculated Property
Cp,gas	233.93	J/mol×K	517.64	Joback Calculated Property
Cp,gas	242.42	J/mol×K	546.35	Joback Calculated Property
Cp,liquid	[202.64; 235.17]	J/mol×K	[284.15; 373.15]
Cp,liquid	212.36	J/mol×K	284.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	213.23	J/mol×K	286.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	213.91	J/mol×K	289.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	214.63	J/mol×K	291.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	202.64	J/mol×K	293.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	215.40	J/mol×K	294.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	216.12	J/mol×K	296.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	204.33	J/mol×K	298.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	216.20	J/mol×K	298.15	NIST
Cp,liquid	216.95	J/mol×K	299.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	217.75	J/mol×K	301.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	205.90	J/mol×K	303.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	218.44	J/mol×K	304.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	219.22	J/mol×K	306.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	207.47	J/mol×K	308.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	219.99	J/mol×K	309.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	221.00	J/mol×K	311.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	208.91	J/mol×K	313.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	221.78	J/mol×K	314.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	222.49	J/mol×K	316.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	210.48	J/mol×K	318.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	223.43	J/mol×K	319.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	224.31	J/mol×K	321.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	212.05	J/mol×K	323.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	224.70	J/mol×K	324.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	226.02	J/mol×K	326.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	213.62	J/mol×K	328.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	227.13	J/mol×K	329.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	228.86	J/mol×K	331.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	215.07	J/mol×K	333.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	228.99	J/mol×K	334.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	229.44	J/mol×K	336.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	216.63	J/mol×K	338.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	230.06	J/mol×K	339.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	231.22	J/mol×K	341.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	217.96	J/mol×K	343.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	231.83	J/mol×K	344.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	232.32	J/mol×K	346.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	219.05	J/mol×K	348.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	233.18	J/mol×K	349.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	234.56	J/mol×K	351.65	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	220.98	J/mol×K	353.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	235.17	J/mol×K	353.15	Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Cp,liquid	222.42	J/mol×K	358.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	223.87	J/mol×K	363.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	225.32	J/mol×K	368.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
Cp,liquid	226.65	J/mol×K	373.15	Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
η	[0.0004778; 0.0007704]	Pa×s	[293.15; 333.15]
η	0.0007704	Pa×s	293.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0007173	Pa×s	298.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0006702	Pa×s	303.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0006283	Pa×s	308.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0005910	Pa×s	313.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0005580	Pa×s	318.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0005285	Pa×s	323.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0005019	Pa×s	328.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
η	0.0004778	Pa×s	333.15	Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
ΔvapH	[35.67; 43.50]	kJ/mol	[328.00; 408.10]
ΔvapH	40.50 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	40.00 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	41.10	kJ/mol	347.50	NIST
ΔvapH	43.50	kJ/mol	348.50	NIST
ΔvapH	39.00 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	38.40 ± 0.10	kJ/mol	368.00	NIST
ΔvapH	35.67	kJ/mol	408.10	NIST
ν	[0.0000007; 0.0000009]	m2/s	[283.15; 313.15]
ν	0.0000009	m2/s	283.15	Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
ν	0.0000008	m2/s	298.15	Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
ν	0.0000007	m2/s	313.15	Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
Pvap	[1.25; 5.96]	kPa	[298.15; 328.15]
Pvap	1.25	kPa	298.15	Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
Pvap	2.86	kPa	313.15	(Vapour + liquid) equilibria and excess molar enthalpies for binary mixtures containing N,N-dialkylamides and 1-chloroalkanes
Pvap	2.86	kPa	313.15	Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
Pvap	5.96	kPa	328.15	Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
n0	[1.41680; 1.41720]		[298.15; 303.15]
n0	1.41710		298.15	Densities, Excess Molar Volumes, Viscosities, and Refractive Indices of Binary Mixtures of n-Butyl Acetate with 1-Chloroalkanes (C4 C8) at 298.15 K
n0	1.41720		298.15	(P,Vm,T) Measurements of (octane + 1-chlorohexane) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
n0	1.41680		303.15	Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
ρl	[873.38; 873.50]	kg/m3	[298.15; 298.15]
ρl	873.50	kg/m3	298.15	Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
ρl	873.38	kg/m3	298.15	Experimental and predicted data of excess molar enthalpies and excess molar volumes for the ternary system (1,3-dichlorobenzene + benzene + 1-chlorohexane) at T = 298.15 K
csound,fluid	[922.90; 1219.10]	m/s	[293.15; 373.15]
csound,fluid	1219.10	m/s	293.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1200.10	m/s	298.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1181.90	m/s	303.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1165.20	m/s	308.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1143.70	m/s	313.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1128.10	m/s	318.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1106.00	m/s	323.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1087.00	m/s	328.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1068.80	m/s	333.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1050.20	m/s	338.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1031.70	m/s	343.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	1013.30	m/s	348.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	995.00	m/s	353.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	976.90	m/s	358.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	958.90	m/s	363.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	940.60	m/s	368.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
csound,fluid	922.90	m/s	373.15	Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition

Datasets

1. Mass density, kg/m3 (2)
2. Speed of sound, m/s (1)

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	882.7
288.15	2000.00	884.4
288.15	4100.00	886.0
288.15	5900.00	887.5
288.15	8100.00	889.2
288.15	10100.00	890.7
288.15	12200.00	892.3
288.15	14200.00	893.8
288.15	16200.00	895.2
288.15	18200.00	896.7
288.15	20200.00	898.3
298.15	100.00	873.1
298.15	2000.00	874.8
298.15	4100.00	876.6
298.15	6100.00	878.3
298.15	8100.00	879.9
298.15	10200.00	881.7
298.15	12100.00	883.3
298.15	14200.00	885.0
298.15	16400.00	886.6
298.15	18400.00	888.1
298.15	20200.00	889.6
308.15	100.00	864.3
308.15	2000.00	866.1
308.15	4100.00	868.0
308.15	6100.00	869.7
308.15	8100.00	871.5
308.15	10200.00	873.3
308.15	12100.00	875.0
308.15	14200.00	876.7
308.15	16200.00	878.3
308.15	18300.00	879.9
308.15	20200.00	881.5
318.15	100.00	855.1
318.15	2000.00	857.0
318.15	4000.00	858.9
318.15	6100.00	860.9
318.15	8100.00	862.7
318.15	10100.00	864.6
318.15	11900.00	866.1
318.15	14100.00	868.1
318.15	16100.00	869.9
318.15	18000.00	871.4
318.15	20000.00	872.8
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	873.1
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
293.15	100.00	1219.1
293.15	5000.00	1240.5
293.15	9910.00	1264.5
293.15	19720.00	1310.0
293.15	29530.00	1352.6
293.15	39340.00	1392.6
293.15	49150.00	1430.1
293.15	58960.00	1465.7
293.15	68770.00	1499.3
293.15	78580.00	1531.5
293.15	88390.00	1562.3
293.15	98200.00	1591.9
293.15	108000.00	1620.6
293.15	117800.00	1648.2
293.15	127600.00	1675.2
293.15	137400.00	1701.5
293.15	147200.00	1727.1
293.15	157100.00	1752.2
293.15	166900.00	1776.7
293.15	176700.00	1800.6
293.15	186500.00	1824.0
293.15	196300.00	1846.5
313.15	100.00	1140.7
313.15	5000.00	1166.4
313.15	9910.00	1191.8
313.15	19720.00	1240.1
313.15	29530.00	1285.3
313.15	39340.00	1327.6
313.15	49150.00	1367.4
313.15	58960.00	1405.0
313.15	68770.00	1440.6
313.15	78580.00	1474.6
313.15	88390.00	1507.0
313.15	98200.00	1538.0
313.15	108000.00	1567.9
313.15	117800.00	1596.7
313.15	127600.00	1624.5
313.15	137400.00	1651.4
313.15	147200.00	1677.5
313.15	157100.00	1702.6
313.15	166900.00	1726.9
313.15	176700.00	1750.3
313.15	186500.00	1772.6
313.15	196300.00	1793.6
333.15	100.00	1068.8
333.15	5000.00	1097.1
333.15	9910.00	1124.4
333.15	19720.00	1176.0
333.15	29530.00	1224.0
333.15	39340.00	1268.8
333.15	49150.00	1310.8
333.15	58960.00	1350.4
333.15	68770.00	1387.7
333.15	78580.00	1423.2
333.15	88390.00	1457.0
333.15	98200.00	1489.4
333.15	108000.00	1520.4
333.15	117800.00	1550.3
333.15	127600.00	1579.1
333.15	137400.00	1607.0
333.15	147200.00	1633.9
333.15	157100.00	1659.9
333.15	166900.00	1684.9
333.15	176700.00	1708.9
333.15	186500.00	1731.8
333.15	196300.00	1753.5
353.15	100.00	995.0
353.15	5000.00	1026.2
353.15	9910.00	1055.4
353.15	19720.00	1110.7
353.15	29530.00	1162.0
353.15	39340.00	1209.8
353.15	49150.00	1254.5
353.15	58960.00	1296.3
353.15	68770.00	1335.8
353.15	78580.00	1373.0
353.15	88390.00	1408.3
353.15	98200.00	1441.9
353.15	108000.00	1474.0
353.15	117800.00	1504.7
353.15	127600.00	1534.3
353.15	137400.00	1562.7
353.15	147200.00	1590.1
353.15	157100.00	1616.4
353.15	166900.00	1641.8
353.15	176700.00	1666.1
353.15	186500.00	1689.4
353.15	196300.00	1711.4
373.15	100.00	922.9
373.15	5000.00	957.0
373.15	9910.00	989.6
373.15	19720.00	1050.4
373.15	29530.00	1105.8
373.15	39340.00	1156.5
373.15	49150.00	1203.2
373.15	58960.00	1246.3
373.15	68770.00	1286.9
373.15	78580.00	1324.8
373.15	88390.00	1360.8
373.15	98200.00	1395.1
373.15	108000.00	1427.9
373.15	117800.00	1459.6
373.15	127600.00	1490.1
373.15	137400.00	1519.6
373.15	147200.00	1548.1
373.15	157100.00	1575.5
373.15	166900.00	1601.7
373.15	176700.00	1626.5
373.15	186500.00	1649.5
373.15	196300.00	1670.6
393.15	100.00	853.3
393.15	5000.00	893.8
393.15	9910.00	928.6
393.15	19720.00	993.2
393.15	29530.00	1051.8
393.15	39340.00	1105.2
393.15	49150.00	1154.2
393.15	58960.00	1199.4
393.15	68770.00	1241.4
393.15	78580.00	1280.8
393.15	88390.00	1318.0
393.15	98200.00	1353.3
393.15	108000.00	1387.2
393.15	117800.00	1419.7
393.15	127600.00	1451.2
393.15	137400.00	1481.6
393.15	147200.00	1511.1
393.15	157100.00	1539.5
393.15	166900.00	1566.9
393.15	176700.00	1592.8
393.15	186500.00	1617.2
393.15	196300.00	1639.7
413.15	100.00	784.0
413.15	5000.00	829.4
413.15	9910.00	867.7
413.15	19720.00	938.1
413.15	29530.00	1001.1
413.15	39340.00	1057.7
413.15	49150.00	1109.0
413.15	58960.00	1155.8
413.15	68770.00	1198.9
413.15	78580.00	1239.1
413.15	88390.00	1276.9
413.15	98200.00	1312.8
413.15	108000.00	1347.4
413.15	117800.00	1380.6
413.15	127600.00	1413.0
413.15	137400.00	1444.5
413.15	147200.00	1475.2
413.15	157100.00	1504.9
413.15	166900.00	1533.7
413.15	176700.00	1560.9
413.15	186500.00	1586.4
413.15	196300.00	1609.7
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[307.59; 431.58]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.55612e+01
Coefficient B			-3.86347e+03
Coefficient C			-5.46410e+01
Temperature range, min.			307.59
Temperature range, max.			431.58
Pvap	1.33	kPa	307.59	Calculated Property
Pvap	2.93	kPa	321.37	Calculated Property
Pvap	5.98	kPa	335.14	Calculated Property
Pvap	11.39	kPa	348.92	Calculated Property
Pvap	20.49	kPa	362.70	Calculated Property
Pvap	35.04	kPa	376.47	Calculated Property
Pvap	57.36	kPa	390.25	Calculated Property
Pvap	90.31	kPa	404.03	Calculated Property
Pvap	137.38	kPa	417.80	Calculated Property
Pvap	202.67	kPa	431.58	Calculated Property
Pvap	[0.69; 104.41]	kPa	[288.15; 409.15]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.03644e+02
Coefficient B			-8.56728e+03
Coefficient C			-1.32703e+01
Coefficient D			1.04706e-05
Temperature range, min.			288.15
Temperature range, max.			409.15
Pvap	0.69	kPa	288.15	Calculated Property
Pvap	1.53	kPa	301.59	Calculated Property
Pvap	3.15	kPa	315.04	Calculated Property
Pvap	6.03	kPa	328.48	Calculated Property
Pvap	10.86	kPa	341.93	Calculated Property
Pvap	18.53	kPa	355.37	Calculated Property
Pvap	30.18	kPa	368.82	Calculated Property
Pvap	47.22	kPa	382.26	Calculated Property
Pvap	71.31	kPa	395.71	Calculated Property
Pvap	104.41	kPa	409.15	Calculated Property

Similar Compounds

Find more compounds similar to Hexane, 1-chloro-.

Mixtures

• Acetic acid, butyl ester + Hexane, 1-chloro-
• Hexane, 1-chloro- + Tetrahydrofuran
• Tetrahydropyran + Hexane, 1-chloro-
• 1,3-Dioxolane + Hexane, 1-chloro-
• Hexane, 1-chloro- + 1,4-Dioxane
• Octane + Hexane, 1-chloro-
• Formamide, N,N-dimethyl- + Hexane, 1-chloro-
• N,N-Dimethylacetamide + Hexane, 1-chloro-
• 2-Pyrrolidinone, 1-methyl- + Hexane, 1-chloro-
• Benzene + Benzene, 1,3-dichloro- + Hexane, 1-chloro-
• n-Hexane + Hexane, 1-chloro-
• Hexane, 1-iodo- + Hexane, 1-chloro-
• Benzene + Hexane, 1-chloro-
• Benzene + Benzene, 1,2-dichloro- + Hexane, 1-chloro-
• Hexane, 1-chloro- + 1,8-Diaminooctane
• Hexane, 1-chloro- + 1,10-Diaminodecane
• 1,12-Dodecanediamine + Hexane, 1-chloro-

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Densities, Excess Molar Volumes, Viscosities, and Refractive Indices of Binary Mixtures of n-Butyl Acetate with 1-Chloroalkanes (C4 C8) at 298.15 K
• Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
• (P,Vm,T) Measurements of (octane + 1-chlorohexane) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
• (Vapour + liquid) equilibria and excess molar enthalpies for binary mixtures containing N,N-dialkylamides and 1-chloroalkanes
• Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
• Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
• Experimental and predicted data of excess molar enthalpies and excess molar volumes for the ternary system (1,3-dichlorobenzene + benzene + 1-chlorohexane) at T = 298.15 K
• Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
• Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
• Does Alkyl Chain Length Really Matter? Structure-Property Relationships in Thermochemistry of Ionic Liquids.
• Speed of Sound of Hexane + 1-Chlorohexane, Hexane + 1-Iodohexane, and 1-Chlorohexane + 1-Iodohexane at Saturation Condition
• Excess Molar Enthalpies and Excess Molar Volumes of the Ternary System 1,2-Dichlorobenzene + Benzene +1-Chlorohexane at 298.15 K
• Viscosities and Densities of Binary Mixtures of Hexane with 1-Chlorohexane between 293.15 K and 333.15 K
• Temperature Dependence of the Thermophysical Properties of 1-Chlorohexane, 1-Iodohexane, 1-Iodoheptane, and 1-Chlorononane at Saturation Condition
• Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
• Speeds of Sound, Densities, and Isentropic Compressibilities of 1-Chlorohexane at Temperatures from (293.15 to 413.15) K and Pressures up to 200 MPa
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + 1-Chloroalkane
• Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems 1-Methyl-2-pyrrolidone + 1-Chloroalkane or + r,u-Dichloroalkane
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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