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

• 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
ΔfG°	-12.29	kJ/mol	Joback Calculated Property
ΔfH°gas	-182.91	kJ/mol	Joback 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. Sol...
log10WS	-3.12		Estimat...
logPoct/wat	2.805		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	0.420	m3/kmol	Joback 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 Ca...
Cp,liquid	213.23	J/mol×K	286.65	Heat Ca...
Cp,liquid	213.91	J/mol×K	289.15	Heat Ca...
Cp,liquid	214.63	J/mol×K	291.65	Heat Ca...
Cp,liquid	202.64	J/mol×K	293.15	Tempera...
Cp,liquid	215.40	J/mol×K	294.15	Heat Ca...
Cp,liquid	216.12	J/mol×K	296.65	Heat Ca...
Cp,liquid	216.20	J/mol×K	298.15	NIST
Cp,liquid	204.33	J/mol×K	298.15	Tempera...
Cp,liquid	216.95	J/mol×K	299.15	Heat Ca...
Cp,liquid	217.75	J/mol×K	301.65	Heat Ca...
Cp,liquid	205.90	J/mol×K	303.15	Tempera...
Cp,liquid	218.44	J/mol×K	304.15	Heat Ca...
Cp,liquid	219.22	J/mol×K	306.65	Heat Ca...
Cp,liquid	207.47	J/mol×K	308.15	Tempera...
Cp,liquid	219.99	J/mol×K	309.15	Heat Ca...
Cp,liquid	221.00	J/mol×K	311.65	Heat Ca...
Cp,liquid	208.91	J/mol×K	313.15	Tempera...
Cp,liquid	221.78	J/mol×K	314.15	Heat Ca...
Cp,liquid	222.49	J/mol×K	316.65	Heat Ca...
Cp,liquid	210.48	J/mol×K	318.15	Tempera...
Cp,liquid	223.43	J/mol×K	319.15	Heat Ca...
Cp,liquid	224.31	J/mol×K	321.65	Heat Ca...
Cp,liquid	212.05	J/mol×K	323.15	Tempera...
Cp,liquid	224.70	J/mol×K	324.15	Heat Ca...
Cp,liquid	226.02	J/mol×K	326.65	Heat Ca...
Cp,liquid	213.62	J/mol×K	328.15	Tempera...
Cp,liquid	227.13	J/mol×K	329.15	Heat Ca...
Cp,liquid	228.86	J/mol×K	331.65	Heat Ca...
Cp,liquid	215.07	J/mol×K	333.15	Tempera...
Cp,liquid	228.99	J/mol×K	334.15	Heat Ca...
Cp,liquid	229.44	J/mol×K	336.65	Heat Ca...
Cp,liquid	216.63	J/mol×K	338.15	Tempera...
Cp,liquid	230.06	J/mol×K	339.15	Heat Ca...
Cp,liquid	231.22	J/mol×K	341.65	Heat Ca...
Cp,liquid	217.96	J/mol×K	343.15	Tempera...
Cp,liquid	231.83	J/mol×K	344.15	Heat Ca...
Cp,liquid	232.32	J/mol×K	346.65	Heat Ca...
Cp,liquid	219.05	J/mol×K	348.15	Tempera...
Cp,liquid	233.18	J/mol×K	349.15	Heat Ca...
Cp,liquid	234.56	J/mol×K	351.65	Heat Ca...
Cp,liquid	235.17	J/mol×K	353.15	Heat Ca...
Cp,liquid	220.98	J/mol×K	353.15	Tempera...
Cp,liquid	222.42	J/mol×K	358.15	Tempera...
Cp,liquid	223.87	J/mol×K	363.15	Tempera...
Cp,liquid	225.32	J/mol×K	368.15	Tempera...
Cp,liquid	226.65	J/mol×K	373.15	Tempera...
η	[0.0004778; 0.0007704]	Pa×s	[293.15; 333.15]
η	0.0007704	Pa×s	293.15	Viscosi...
η	0.0007173	Pa×s	298.15	Viscosi...
η	0.0006702	Pa×s	303.15	Viscosi...
η	0.0006283	Pa×s	308.15	Viscosi...
η	0.0005910	Pa×s	313.15	Viscosi...
η	0.0005580	Pa×s	318.15	Viscosi...
η	0.0005285	Pa×s	323.15	Viscosi...
η	0.0005019	Pa×s	328.15	Viscosi...
η	0.0004778	Pa×s	333.15	Viscosi...
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	Experim...
ν	0.0000008	m2/s	298.15	Experim...
ν	0.0000007	m2/s	313.15	Experim...
Pvap	[1.25; 5.96]	kPa	[298.15; 328.15]
Pvap	1.25	kPa	298.15	Isother...
Pvap	2.86	kPa	313.15	(Vapour...
Pvap	2.86	kPa	313.15	Excess ...
Pvap	5.96	kPa	328.15	Isother...
n0	[1.41680; 1.41720]		[298.15; 303.15]
n0	1.41710		298.15	Densiti...
n0	1.41720		298.15	(P,Vm,T...
n0	1.41680		303.15	Densiti...
ρl	[873.38; 873.50]	kg/m3	[298.15; 298.15]
ρl	873.50	kg/m3	298.15	Vapour ...
ρl	873.38	kg/m3	298.15	Experim...
csound,fluid	[922.90; 1219.10]	m/s	[293.15; 373.15]
csound,fluid	1219.10	m/s	293.15	Speed o...
csound,fluid	1200.10	m/s	298.15	Speed o...
csound,fluid	1181.90	m/s	303.15	Speed o...
csound,fluid	1165.20	m/s	308.15	Speed o...
csound,fluid	1143.70	m/s	313.15	Speed o...
csound,fluid	1128.10	m/s	318.15	Speed o...
csound,fluid	1106.00	m/s	323.15	Speed o...
csound,fluid	1087.00	m/s	328.15	Speed o...
csound,fluid	1068.80	m/s	333.15	Speed o...
csound,fluid	1050.20	m/s	338.15	Speed o...
csound,fluid	1031.70	m/s	343.15	Speed o...
csound,fluid	1013.30	m/s	348.15	Speed o...
csound,fluid	995.00	m/s	353.15	Speed o...
csound,fluid	976.90	m/s	358.15	Speed o...
csound,fluid	958.90	m/s	363.15	Speed o...
csound,fluid	940.60	m/s	368.15	Speed o...
csound,fluid	922.90	m/s	373.15	Speed o...

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 Yaw...
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 Vap...
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
• 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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