Chemical Properties of Butane, 1-chloro- (CAS 109-69-3)

InChI

InChI=1S/C4H9Cl/c1-2-3-4-5/h2-4H2,1H3

InChI Key

VFWCMGCRMGJXDK-UHFFFAOYSA-N

Formula

C4H9Cl

SMILES

CCCCCl

Molecular Weight¹

92.57

CAS

109-69-3

Other Names

• 1-Chlorobutane
• Butyl chloride
• Chlorure de butyle
• N-BUTYL CHLORIDE
• N-PROPYLCARBINYL CHLORIDE
• NBC wormer
• NCI-C06155
• NSC 8419
• Sure Shot
• n-C4H9Cl

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• 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_fH°_liquid : Liquid phase 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.
• NFPA Health : NFPA Health 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).
• γ : Surface Tension (N/m).
• 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).
• Z_c : Critical Compressibility.
• 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	0.2180		KDB
ΔcH°liquid	[-2704.10; -2695.80]	kJ/mol
ΔcH°liquid	-2695.80 ± 1.10	kJ/mol	NIST
ΔcH°liquid	-2704.10 ± 8.40	kJ/mol	NIST
μ	2.00	debye	KDB
ΔfG°	-38.81	kJ/mol	KDB
ΔfH°gas	[-154.60; -147.40]	kJ/mol
ΔfH°gas	-147.40	kJ/mol	KDB
ΔfH°gas	-154.60 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-188.20 ± 1.20	kJ/mol	NIST
ΔfusH°	10.31	kJ/mol	Joback Calculated Property
ΔvapH°	28.88	kJ/mol	Joback Calculated Property
IE	[10.46; 10.94]	eV
IE	10.64 ± 0.19	eV	NIST
IE	10.63	eV	NIST
IE	10.46 ± 0.05	eV	NIST
IE	10.94	eV	NIST
IE	10.50 ± 0.07	eV	NIST
IE	10.67 ± 0.03	eV	NIST
IE	10.84	eV	NIST
log10WS	[-2.03; -2.03]
log10WS	-2.03		Aq. Sol...
log10WS	-2.03		Estimat...
logPoct/wat	2.025		Crippen Calculated Property
McVol	79.460	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
Pc	3680.00	kPa	KDB
Inp	[607.00; 659.61]
Inp	646.10		NIST
Inp	641.60		NIST
Inp	647.30		NIST
Inp	642.50		NIST
Inp	639.60		NIST
Inp	639.00		NIST
Inp	638.30		NIST
Inp	Outlier 659.61		NIST
Inp	639.00		NIST
Inp	639.50		NIST
Inp	640.00		NIST
Inp	630.40		NIST
Inp	654.00		NIST
Inp	641.00		NIST
Inp	631.00		NIST
Inp	648.00		NIST
Inp	644.00		NIST
Inp	641.00		NIST
Inp	641.00		NIST
Inp	653.00		NIST
Inp	644.00		NIST
Inp	646.00		NIST
Inp	648.00		NIST
Inp	641.00		NIST
Inp	Outlier 607.00		NIST
Inp	Outlier 612.00		NIST
Inp	638.00		NIST
Inp	637.00		NIST
Inp	637.00		NIST
Inp	637.00		NIST
Inp	637.00		NIST
Inp	641.00		NIST
Inp	637.00		NIST
Inp	641.00		NIST
Inp	642.00		NIST
Inp	635.00		NIST
Inp	642.00		NIST
Inp	648.30		NIST
Inp	639.10		NIST
Inp	631.00		NIST
Inp	637.00		NIST
Inp	648.30		NIST
I	[832.00; 858.00]
I	832.00		NIST
I	842.00		NIST
I	858.00		NIST
Tboil	[351.52; 351.60]	K
Tboil	351.60	K	KDB
Tboil	351.52	K	Study o...
Tboil	351.53	K	Isobari...
Tboil	351.52	K	Vapor-L...
Tc	[542.00; 542.00]	K
Tc	542.00	K	KDB
Tc	542.00	K	NIST
Tfus	[149.95; 150.12]	K
Tfus	150.10	K	KDB
Tfus	150.12	K	Aq. Sol...
Tfus	150.05	K	NIST
Tfus	149.95 ± 0.05	K	NIST
Tfus	150.05 ± 0.20	K	NIST
Vc	0.312	m3/kmol	KDB
Zc	0.2547810		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[118.92; 159.72]	J/mol×K	[328.35; 500.65]
Cp,gas	118.92	J/mol×K	328.35	Joback Calculated Property
Cp,gas	126.38	J/mol×K	357.07	Joback Calculated Property
Cp,gas	133.57	J/mol×K	385.78	Joback Calculated Property
Cp,gas	140.49	J/mol×K	414.50	Joback Calculated Property
Cp,gas	147.15	J/mol×K	443.22	Joback Calculated Property
Cp,gas	153.56	J/mol×K	471.93	Joback Calculated Property
Cp,gas	159.72	J/mol×K	500.65	Joback Calculated Property
Cp,liquid	[156.22; 173.09]	J/mol×K	[284.15; 353.15]
Cp,liquid	156.22	J/mol×K	284.15	Heat Ca...
Cp,liquid	156.75	J/mol×K	286.65	Heat Ca...
Cp,liquid	157.28	J/mol×K	289.15	Heat Ca...
Cp,liquid	157.70	J/mol×K	291.65	Heat Ca...
Cp,liquid	158.27	J/mol×K	294.15	Heat Ca...
Cp,liquid	158.86	J/mol×K	296.65	Heat Ca...
Cp,liquid	158.90	J/mol×K	298.15	NIST
Cp,liquid	159.53	J/mol×K	298.15	NIST
Cp,liquid	159.64	J/mol×K	298.15	NIST
Cp,liquid	159.48	J/mol×K	299.15	Heat Ca...
Cp,liquid	160.05	J/mol×K	301.65	Heat Ca...
Cp,liquid	160.50	J/mol×K	304.15	Heat Ca...
Cp,liquid	161.06	J/mol×K	306.65	Heat Ca...
Cp,liquid	161.59	J/mol×K	309.15	Heat Ca...
Cp,liquid	162.24	J/mol×K	311.65	Heat Ca...
Cp,liquid	162.92	J/mol×K	314.15	Heat Ca...
Cp,liquid	163.42	J/mol×K	316.65	Heat Ca...
Cp,liquid	164.11	J/mol×K	319.15	Heat Ca...
Cp,liquid	164.82	J/mol×K	321.65	Heat Ca...
Cp,liquid	165.00	J/mol×K	324.15	Heat Ca...
Cp,liquid	165.97	J/mol×K	326.65	Heat Ca...
Cp,liquid	166.72	J/mol×K	329.15	Heat Ca...
Cp,liquid	167.29	J/mol×K	331.65	Heat Ca...
Cp,liquid	167.78	J/mol×K	334.15	Heat Ca...
Cp,liquid	168.53	J/mol×K	336.65	Heat Ca...
Cp,liquid	169.12	J/mol×K	339.15	Heat Ca...
Cp,liquid	170.01	J/mol×K	341.65	Heat Ca...
Cp,liquid	170.43	J/mol×K	344.15	Heat Ca...
Cp,liquid	170.49	J/mol×K	346.65	Heat Ca...
Cp,liquid	171.50	J/mol×K	349.15	Heat Ca...
Cp,liquid	173.02	J/mol×K	351.65	Heat Ca...
Cp,liquid	173.09	J/mol×K	353.15	Heat Ca...
η	[0.0003540; 0.0004993]	Pa×s	[283.15; 318.15]
η	0.0004993	Pa×s	283.15	Experim...
η	0.0004993	Pa×s	283.15	Viscosi...
η	0.0004701	Pa×s	288.15	Viscosi...
η	0.0004701	Pa×s	288.15	Experim...
η	0.0004770	Pa×s	288.15	Densiti...
η	0.0004433	Pa×s	293.15	Viscosi...
η	0.0004433	Pa×s	293.15	Experim...
η	0.0004214	Pa×s	298.15	Viscosi...
η	0.0004214	Pa×s	298.15	Experim...
η	0.0004212	Pa×s	298.15	Densiti...
η	0.0004273	Pa×s	298.15	Measure...
η	0.0004290	Pa×s	298.15	Densiti...
η	0.0004050	Pa×s	303.15	Experim...
η	0.0004050	Pa×s	303.15	Viscosi...
η	0.0004090	Pa×s	303.15	Densiti...
η	0.0003885	Pa×s	308.15	Viscosi...
η	0.0003900	Pa×s	308.15	Densiti...
η	0.0003885	Pa×s	308.15	Experim...
η	0.0003645	Pa×s	313.15	Measure...
η	0.0003642	Pa×s	313.15	Experim...
η	0.0003720	Pa×s	313.15	Densiti...
η	0.0003642	Pa×s	313.15	Viscosi...
η	0.0003640	Pa×s	313.15	Densiti...
η	0.0003540	Pa×s	318.15	Densiti...
ΔvapH	[29.40; 37.20]	kJ/mol	[304.00; 358.00]
ΔvapH	35.60	kJ/mol	304.00	NIST
ΔvapH	32.70 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	37.20	kJ/mol	318.00	NIST
ΔvapH	35.00	kJ/mol	323.00	NIST
ΔvapH	31.80 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	30.90 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	30.90	kJ/mol	349.50	NIST
ΔvapH	30.00	kJ/mol	351.60	KDB
ΔvapH	30.39	kJ/mol	351.70	NIST
ΔvapH	30.00 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	29.40 ± 0.10	kJ/mol	358.00	NIST
ν	[0.0000004; 0.0000006]	m2/s	[283.15; 313.15]
ν	0.0000006	m2/s	283.15	Experim...
ν	0.0000005	m2/s	298.15	Thermop...
ν	0.0000005	m2/s	298.15	Viscosi...
ν	0.0000005	m2/s	298.15	Experim...
ν	0.0000004	m2/s	313.15	Thermop...
ν	0.0000004	m2/s	313.15	Viscosi...
ν	0.0000004	m2/s	313.15	Experim...
Pvap	[4.98; 101.40]	kPa	[278.15; 351.61]
Pvap	4.98	kPa	278.15	Isother...
Pvap	6.51	kPa	283.15	Isother...
Pvap	8.40	kPa	288.15	Experim...
Pvap	8.40	kPa	288.15	Experim...
Pvap	8.40	kPa	288.15	Isother...
Pvap	8.38	kPa	288.15	Isother...
Pvap	10.69	kPa	293.15	Isother...
Pvap	13.52	kPa	298.15	Experim...
Pvap	13.52	kPa	298.15	Experim...
Pvap	13.50	kPa	298.15	Isother...
Pvap	13.72	kPa	298.15	(Vapour...
Pvap	13.52	kPa	298.15	(Vapour...
Pvap	13.52	kPa	298.15	Isother...
Pvap	16.97	kPa	303.15	Isother...
Pvap	21.04	kPa	308.15	Experim...
Pvap	21.05	kPa	308.15	Isother...
Pvap	20.66	kPa	308.15	(Vapour...
Pvap	21.04	kPa	308.15	Isother...
Pvap	21.04	kPa	308.15	Experim...
Pvap	25.72	kPa	313.15	Excess ...
Pvap	25.72	kPa	313.15	(Vapour...
Pvap	25.88	kPa	313.15	Isother...
Pvap	31.59	kPa	318.15	Isother...
Pvap	31.46	kPa	318.15	(Vapour...
Pvap	38.26	kPa	323.15	Isother...
Pvap	40.87	kPa	325.00	Isobari...
Pvap	44.16	kPa	327.14	Isobari...
Pvap	46.87	kPa	328.66	Isobari...
Pvap	48.37	kPa	329.60	Isobari...
Pvap	48.83	kPa	329.78	Isobari...
Pvap	51.33	kPa	331.28	Isobari...
Pvap	53.30	kPa	332.28	Isobari...
Pvap	54.07	kPa	332.68	Isobari...
Pvap	59.61	kPa	335.44	Isobari...
Pvap	65.42	kPa	338.11	Isobari...
Pvap	72.23	kPa	341.04	Isobari...
Pvap	80.00	kPa	344.14	Isobari...
Pvap	87.52	kPa	346.84	Isobari...
Pvap	92.35	kPa	348.63	Isobari...
Pvap	101.30	kPa	351.53	Isobari...
Pvap	101.40	kPa	351.61	Isobari...
n0	[1.39131; 1.40750]		[283.15; 313.15]
n0	1.40750		283.15	Volumet...
n0	1.40481		288.15	Volumet...
n0	1.40450		288.15	Excess ...
n0	1.40212		293.15	Volumet...
n0	1.39950		298.15	Volumet...
n0	1.39910		298.15	Isother...
n0	1.39930		298.15	Excess ...
n0	1.39953		298.15	Isother...
n0	1.39950		298.15	Volumet...
n0	1.39960		298.15	Densiti...
n0	1.39953		298.15	Isother...
n0	1.39672		303.15	Volumet...
n0	1.39410		308.15	Excess ...
n0	1.39395		308.15	Volumet...
n0	1.39133		313.15	Volumet...
n0	1.39131		313.15	Volumet...
ρl	[835.30; 925.80]	kg/m3	[253.15; 338.15]
ρl	925.80	kg/m3	253.15	Density...
ρl	917.40	kg/m3	263.15	Density...
ρl	907.30	kg/m3	273.15	Density...
ρl	896.60	kg/m3	283.15	Density...
ρl	892.18	kg/m3	288.15	Densiti...
ρl	892.10	kg/m3	288.15	Densiti...
ρl	891.75	kg/m3	288.15	Excess ...
ρl	886.00	kg/m3	293.00	KDB
ρl	885.90	kg/m3	293.15	Density...
ρl	880.69	kg/m3	298.15	Surface...
ρl	881.17	kg/m3	298.15	Volumet...
ρl	880.69	kg/m3	298.15	Densiti...
ρl	880.69	kg/m3	298.15	Surface...
ρl	881.12	kg/m3	298.15	Densiti...
ρl	880.86	kg/m3	298.15	Volumet...
ρl	880.69	kg/m3	298.15	Thermod...
ρl	880.69	kg/m3	298.15	Surface...
ρl	880.40	kg/m3	298.15	Density...
ρl	881.05	kg/m3	298.15	Densiti...
ρl	874.90	kg/m3	303.15	Density...
ρl	875.10	kg/m3	303.15	Excess ...
ρl	869.93	kg/m3	308.15	Densiti...
ρl	870.00	kg/m3	308.15	Volumet...
ρl	869.86	kg/m3	308.15	Densiti...
ρl	863.83	kg/m3	313.15	Excess ...
ρl	863.90	kg/m3	313.15	Density...
ρl	858.52	kg/m3	318.15	Densiti...
ρl	858.67	kg/m3	318.15	Volumet...
ρl	858.58	kg/m3	318.15	Densiti...
ρl	852.10	kg/m3	323.15	Density...
ρl	835.30	kg/m3	338.15	Density...
csound,fluid	[1037.26; 1119.00]	m/s	[298.15; 318.15]
csound,fluid	1119.00	m/s	298.15	Speeds ...
csound,fluid	1078.01	m/s	308.15	Speeds ...
csound,fluid	1037.26	m/s	318.15	Speeds ...
γ	[0.02; 0.02]	N/m	[283.15; 313.15]
γ	0.02	N/m	283.15	Surface...
γ	0.02	N/m	288.15	Surface...
γ	0.02	N/m	293.15	Surface...
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	313.15	Surface...

Datasets

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	897.36
100.00	288.15	892.04
100.00	293.15	886.36
100.00	298.15	880.82
100.00	303.15	875.21
100.00	308.15	869.76
100.00	313.15	863.9
100.00	318.15	858.39
100.00	323.15	852.47
100.00	328.15	846.87
2000.00	283.15	899.21
2000.00	288.15	893.99
2000.00	293.15	888.35
2000.00	298.15	882.9
2000.00	303.15	877.35
2000.00	308.15	871.94
2000.00	313.15	866.24
2000.00	318.15	860.79
2000.00	323.15	854.85
2000.00	328.15	849.38
5000.00	283.15	902.05
5000.00	288.15	896.87
5000.00	293.15	891.37
5000.00	298.15	886.01
5000.00	303.15	880.6
5000.00	308.15	875.3
5000.00	313.15	869.77
5000.00	318.15	864.38
5000.00	323.15	858.68
5000.00	328.15	853.41
7000.00	283.15	903.87
7000.00	288.15	898.76
7000.00	293.15	893.36
7000.00	298.15	888.03
7000.00	303.15	882.68
7000.00	308.15	877.49
7000.00	313.15	871.92
7000.00	318.15	866.7
7000.00	323.15	861.15
7000.00	328.15	855.89
10000.00	283.15	906.6
10000.00	288.15	901.58
10000.00	293.15	896.28
10000.00	298.15	890.99
10000.00	303.15	885.78
10000.00	308.15	880.77
10000.00	313.15	875.27
10000.00	318.15	870.14
10000.00	323.15	864.65
10000.00	328.15	859.47
20000.00	283.15	915.16
20000.00	288.15	910.38
20000.00	293.15	905.24
20000.00	298.15	900.33
20000.00	303.15	895.41
20000.00	308.15	890.56
20000.00	313.15	885.35
20000.00	318.15	880.62
20000.00	323.15	875.43
20000.00	328.15	870.67
30000.00	283.15	923.05
30000.00	288.15	918.48
30000.00	293.15	913.5
30000.00	298.15	908.81
30000.00	303.15	904.1
30000.00	308.15	899.63
30000.00	313.15	894.59
30000.00	318.15	890.1
30000.00	323.15	885.16
30000.00	328.15	880.58
40000.00	283.15	930.41
40000.00	288.15	925.97
40000.00	293.15	921.24
40000.00	298.15	916.74
40000.00	303.15	912.24
40000.00	308.15	907.72
40000.00	313.15	903.08
40000.00	318.15	898.75
40000.00	323.15	894.16
40000.00	328.15	889.73
50000.00	283.15	937.2
50000.00	288.15	932.96
50000.00	293.15	928.33
50000.00	298.15	924.0
50000.00	303.15	919.76
50000.00	308.15	915.48
50000.00	313.15	910.86
50000.00	318.15	906.72
50000.00	323.15	902.27
50000.00	328.15	897.97
60000.00	283.15	943.68
60000.00	288.15	939.57
60000.00	293.15	935.0
60000.00	298.15	930.86
60000.00	303.15	926.77
60000.00	308.15	922.6
60000.00	313.15	918.16
60000.00	318.15	914.22
60000.00	323.15	910.0
60000.00	328.15	905.8
65000.00	283.15	946.75
65000.00	288.15	942.66
65000.00	293.15	938.38
65000.00	298.15	934.15
65000.00	303.15	930.08
65000.00	308.15	925.91
65000.00	313.15	921.77
65000.00	318.15	917.73
65000.00	323.15	913.54
65000.00	328.15	909.45
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	891.8
288.15	2000.00	893.6
288.15	4100.00	895.6
288.15	6100.00	897.5
288.15	8100.00	899.4
288.15	10100.00	901.3
288.15	12100.00	903.0
288.15	14100.00	904.9
288.15	16300.00	906.7
288.15	18400.00	908.5
288.15	20200.00	910.3
298.15	100.00	880.6
298.15	2000.00	882.6
298.15	4100.00	884.9
298.15	6100.00	886.8
298.15	8100.00	888.7
298.15	10100.00	890.9
298.15	12100.00	892.8
298.15	14200.00	894.7
298.15	16200.00	896.5
298.15	18300.00	898.5
298.15	20400.00	900.2
308.15	100.00	870.0
308.15	2000.00	872.1
308.15	4100.00	874.4
308.15	6100.00	876.5
308.15	8100.00	878.6
308.15	10100.00	880.8
308.15	12100.00	882.9
308.15	14200.00	884.9
308.15	16200.00	886.8
308.15	18300.00	888.8
308.15	20200.00	890.6
318.15	100.00	859.1
318.15	2000.00	861.5
318.15	4000.00	863.8
318.15	6100.00	866.3
318.15	8100.00	868.7
318.15	10100.00	870.9
318.15	12100.00	873.1
318.15	14100.00	875.1
318.15	16200.00	877.2
318.15	18400.00	879.3
318.15	20200.00	881.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	880.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	897.21
283.15	2500.00	899.51
283.15	5000.00	901.82
283.15	10000.00	906.3
283.15	15000.00	910.57
283.15	20000.00	914.69
283.15	25000.00	918.63
283.15	30000.00	922.33
283.15	35000.00	926.05
293.15	100.00	886.18
293.15	2500.00	888.63
293.15	5000.00	891.13
293.15	10000.00	895.89
293.15	20000.00	904.73
293.15	25000.00	908.9
293.15	30000.00	912.88
293.15	35000.00	916.77
298.15	100.00	880.63
298.15	2500.00	883.17
298.15	5000.00	885.72
298.15	10000.00	890.65
298.15	15000.00	895.36
298.15	20000.00	899.79
298.15	25000.00	904.09
298.15	30000.00	908.22
298.15	35000.00	912.17
303.15	100.00	874.92
303.15	2500.00	877.59
303.15	5000.00	880.23
303.15	10000.00	885.43
303.15	15000.00	890.24
303.15	20000.00	894.84
303.15	25000.00	899.24
303.15	30000.00	903.46
303.15	35000.00	907.47
313.15	100.00	863.82
313.15	2500.00	866.65
313.15	5000.00	869.49
313.15	10000.00	874.93
313.15	15000.00	880.07
313.15	20000.00	884.94
313.15	25000.00	889.61
313.15	30000.00	894.04
313.15	35000.00	898.33
323.15	100.00	852.43
323.15	2500.00	855.47
323.15	5000.00	858.54
323.15	10000.00	864.35
323.15	15000.00	869.85
323.15	20000.00	875.03
323.15	25000.00	879.94
323.15	30000.00	884.62
323.15	35000.00	889.1
333.15	100.00	840.79
333.15	2500.00	844.06
333.15	5000.00	847.37
333.15	10000.00	853.61
333.15	15000.00	859.47
333.15	20000.00	864.97
333.15	25000.00	870.17
333.15	30000.00	875.12
333.15	35000.00	879.82
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	13.52	880.805
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[255.28; 373.41]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.45467e+01
Coefficient B			-3.09635e+03
Coefficient C			-3.81330e+01
Temperature range, min.			255.28
Temperature range, max.			373.41
Pvap	1.33	kPa	255.28	Calculated Property
Pvap	3.01	kPa	268.41	Calculated Property
Pvap	6.21	kPa	281.53	Calculated Property
Pvap	11.90	kPa	294.66	Calculated Property
Pvap	21.41	kPa	307.78	Calculated Property
Pvap	36.48	kPa	320.91	Calculated Property
Pvap	59.30	kPa	334.03	Calculated Property
Pvap	92.48	kPa	347.16	Calculated Property
Pvap	139.11	kPa	360.28	Calculated Property
Pvap	202.66	kPa	373.41	Calculated Property
Pvap	[2.33e-06; 3601.12]	kPa	[150.05; 537.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.92413e+01
Coefficient B			-6.56700e+03
Coefficient C			-9.70121e+00
Coefficient D			7.48517e-06
Temperature range, min.			150.05
Temperature range, max.			537.00
Pvap	2.33e-06	kPa	150.05	Calculated Property
Pvap	3.87e-03	kPa	193.04	Calculated Property
Pvap	0.31	kPa	236.04	Calculated Property
Pvap	5.25	kPa	279.03	Calculated Property
Pvap	36.74	kPa	322.03	Calculated Property
Pvap	150.09	kPa	365.02	Calculated Property
Pvap	435.10	kPa	408.02	Calculated Property
Pvap	1006.70	kPa	451.01	Calculated Property
Pvap	2003.11	kPa	494.01	Calculated Property
Pvap	3601.12	kPa	537.00	Calculated Property

Similar Compounds

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

Mixtures

• Tetrahydropyran + Butane, 1-chloro-
• Butane, 1-chloro- + Tetrahydrofuran
• Diisopropyl ether + Butane, 1-chloro-
• Butane, 1-chloro- + Acetic acid, butyl ester
• Butane, 1-ethoxy- + Butane, 1-chloro-
• Butane, 1-chloro- + Propane, 2-methoxy-2-methyl-
• Butane, 1-chloro- + Heptane
• Butane, 1-chloro- + Cyclohexane
• Toluene + Butane, 1-chloro-
• Butane, 1-chloro- + Ethane, nitro-
• Butane, 1-chloro- + Methane, nitro-
• Butane, 1-chloro- + 1-Octanol
• Butane, 1-chloro- + 1-Decanol
• Butane, 1-chloro- + 1,4-Dioxane
• 1,3-Dioxolane + Butane, 1-chloro-
• Formamide, N,N-dimethyl- + Butane, 1-chloro-
• Butane, 1-chloro- + N,N-Dimethylacetamide
• Butane, 1-chloro- + Cyclopentanone
• 2-Pyrrolidinone, 1-methyl- + Butane, 1-chloro-
• n-Hexane + Butane, 1-chloro-

Find more mixtures with Butane, 1-chloro-.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Thermophysical Properties of Mixtures of Tetrahydropyran with Chlorobutanes
• Surface Tension of Mixtures of Tetrahydrofuran or Tetrahydropyran with Isomeric Chlorobutanes
• Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
• Densities, Excess Molar Volumes, Viscosities, and Refractive Indices of Binary Mixtures of n-Butyl Acetate with 1-Chloroalkanes (C4 C8) at 298.15 K
• Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
• Study of tetrahydropyran-chlorobutane VLE using the a o and o o approaches
• Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
• Excess molar volume and viscosity study for the ternary system tetrahydrofuran (1) + 1-chlorobutane (2) + 2-butanol (3) at 283.15, 298.15 and 313.15 K
• Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
• Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
• Limiting activity coefficients of 1-chlorobutane in water and in aqueous solutions of substances involved in synthesis of ionic liquids
• Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
• Isothermal vapor liquid equilibria and excess Gibbs free energies in some binary nitroalkane + chloroalkane mixtures at temperatures from 298.15 K to 318.15 K
• Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
• Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
• Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
• Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
• (Vapour + liquid) equilibria and excess molar enthalpies for binary mixtures containing N,N-dialkylamides and 1-chloroalkanes
• Isothermal (vapour + liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone + chloroalkane) mixtures at temperatures from 298.15 K to 318.15 K
• Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
• Surface and bulk behaviour of some (n-hexane + chloroalkane) mixtures
• (Vapour + liquid) equilibrium and excess Gibbs functions of ternary mixtures containing 1-butanol or 2-butanol, n-hexane, and 1-chlorobutane at T = 298.15 K
• (Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
• Volumetric and acoustic behaviour of systems containing n-hexane, or n-heptane and isomeric chlorobutanes
• Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Thermodynamic study of 2-methyl-tetrahydrofuran with isomeric chlorobutanes
• Volumetric properties for binary and ternary systems consist of 1-chlorobutane, n-butylamine and isobutanol at 298.15 K with application of the Prigogine-Flory-Patterson theory and ERAS-Model
• Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
• Excess properties from p.rho.T data for n-heptane + isomeric chlorobutane mixtures
• The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
• Measurements, Correlations, and Predictions of Viscosities for the Ternary Mixture (2-Butanol + Hexane + 1-Chlorobutane) at 298.15 K and 313.15 K
• Vapor-Liquid Equilibrium and Volumetric Measurements for Binary Mixtures of 1,4-Dioxane with Isomeric Chlorobutanes
• Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
• Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature
• Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
• Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
• 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
• Solubility of Imidazoles, Benzimidazoles, and Phenylimidazoles in Dichloromethane, 1-Chlorobutane, Toluene, and 2-Nitrotoluene
• Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
• Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
• Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Volumetric Properties of Short-Chain Chloroalkanes
• Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
• Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + 1-Chloroalkane
• Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
• Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems 1-Methyl-2-pyrrolidone + 1-Chloroalkane or + r,u-Dichloroalkane
• Densities and Excess Volumes of the 1-Chlorobutane + n-Hexane System at Temperatures from (283.15 to 333.15) K and Pressures from (0.1 to 35) MPa
• Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
• Isothermal Vapor-Liquid Equilibrium of Binary Mixtures Containing 1-Chlorobutane, Ethanol, or Acetonitrile
• Phase Behavior, Densities, and Isothermal Compressibility of Carbon Dioxide + 1-Bromobutane, Carbon Dioxide + 1-Chlorobutane, and Carbon Dioxide + 1-Methylimidazole
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
• Isothermal Vapor-Liquid Equilibrium of Ternary Mixtures Containing 2-Methyl-1-propanol or 2-Methyl-2-propanol, n-Hexane, and 1-Chlorobutane at 298.15 K
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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