Butane, 1,4-dichloro- (CAS 110-56-5)

InChI

InChI=1S/C4H8Cl2/c5-3-1-2-4-6/h1-4H2

InChI Key

KJDRSWPQXHESDQ-UHFFFAOYSA-N

Formula

C4H8Cl2

SMILES

ClCCCCCl

Molecular Weight¹

127.01

CAS

110-56-5

Other Names

1,4-dichlorobutane
tetramethylene chloride

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).
C_sat : Molar heat capacity at saturation pressure (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_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).
log₁₀WS : Log10 of Water solubility in mol/l.
logP_oct/wat : Octanol/Water partition coefficient.
McVol : McGowan's characteristic volume (ml/mol).
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.
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).
¹: Molecular weight from the IUPAC atomic weights tables.

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Physical Properties
Temperature Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources

Physical Properties

Property	Value	Unit	Source
ω	0.3698		Relay (1.0) Calculated Property
Δ_cH°_liquid	-2534.80 ± 1.90	kJ/mol	NIST
Δ_fG°	-41.06	kJ/mol	Joback Calculated Property
Δ_fH°_gas	-183.40 ± 1.90	kJ/mol	NIST
Δ_fH°_liquid	[-229.80; -229.50]	kJ/mol
Δ_fH°_liquid	-229.80 ± 1.90	kJ/mol	NIST
Δ_fH°_liquid	-229.50	kJ/mol	NIST
Δ_fusH°	14.51	kJ/mol	Joback Calculated Property
Δ_vapH°	[46.36; 46.70]	kJ/mol
Δ_vapH°	46.36	kJ/mol	NIST
Δ_vapH°	Outlier 46.70	kJ/mol	NIST
Δ_vapH°	46.50 ± 0.10	kJ/mol	NIST
Δ_vapH°	46.40	kJ/mol	NIST
Δ_vapH°	46.37 ± 0.02	kJ/mol	NIST
Δ_vapH°	46.40 ± 0.10	kJ/mol	NIST
Δ_vapH°	46.40 ± 0.10	kJ/mol	NIST
Δ_vapH°	46.36 ± 0.02	kJ/mol	NIST
IE	11.03	eV	NIST
log₁₀WS	-2.45		Relay (1.0) Calculated Property
logP_oct/wat	2.244		Crippen Calculated Property
McVol	91.700	ml/mol	McGowan Calculated Property
P_c	3560.02	kPa	Joback Calculated Property
I_np	[867.40; 898.10]
I_np	867.40		NIST
I_np	895.00		NIST
I_np	874.00		NIST
I_np	874.00		NIST
I_np	874.00		NIST
I_np	874.00		NIST
I_np	898.10		NIST
I_np	894.10		NIST
I_np	874.00		NIST
I_np	894.10		NIST
T_boil	[308.15; 435.20]	K
T_boil	428.15	K	KDB
T_boil	435.20	K	NIST
T_boil	433.00	K	NIST
T_boil	427.10	K	NIST
T_boil	428.15 ± 1.50	K	NIST
T_boil	Outlier 322.00 ± 3.00	K	NIST
T_boil	427.15 ± 4.00	K	NIST
T_boil	434.65 ± 5.00	K	NIST
T_boil	426.25 ± 2.00	K	NIST
T_boil	Outlier 308.15 ± 2.50	K	NIST
T_boil	427.05 ± 0.50	K	NIST
T_boil	428.00 ± 1.00	K	NIST
T_boil	426.65 ± 0.50	K	NIST
T_c	616.53	K	Relay (1.0) Calculated Property
T_fus	234.50 ± 0.40	K	NIST
V_c	0.341	m³/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[141.72; 181.30]	J/mol×K	[365.98; 547.97]

C_p,gas	141.72	J/mol×K	365.98	Joback Calculated Property
C_p,gas	149.07	J/mol×K	396.31	Joback Calculated Property
C_p,gas	156.10	J/mol×K	426.64	Joback Calculated Property
C_p,gas	162.84	J/mol×K	456.97	Joback Calculated Property
C_p,gas	169.27	J/mol×K	487.30	Joback Calculated Property
C_p,gas	175.43	J/mol×K	517.64	Joback Calculated Property
C_p,gas	181.30	J/mol×K	547.97	Joback Calculated Property
C_p,liquid	[183.59; 184.00]	J/mol×K	[298.15; 298.15]
C_p,liquid	184.00	J/mol×K	298.15	NIST
C_p,liquid	183.59	J/mol×K	298.15	NIST
C_sat	[181.25; 195.12]	J/mol×K	[284.16; 353.14]

C_sat	181.25	J/mol×K	284.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	181.71	J/mol×K	286.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	182.15	J/mol×K	289.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	182.62	J/mol×K	291.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	182.99	J/mol×K	294.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	183.49	J/mol×K	296.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	183.76	J/mol×K	298.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	183.89	J/mol×K	299.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	184.47	J/mol×K	301.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	184.80	J/mol×K	304.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	185.71	J/mol×K	308.56	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	185.83	J/mol×K	309.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	186.41	J/mol×K	311.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	186.88	J/mol×K	314.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	187.38	J/mol×K	316.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	187.89	J/mol×K	319.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	188.52	J/mol×K	321.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	188.85	J/mol×K	324.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	189.48	J/mol×K	326.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	190.01	J/mol×K	329.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	190.54	J/mol×K	331.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	190.99	J/mol×K	334.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	191.48	J/mol×K	336.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	192.00	J/mol×K	339.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	192.36	J/mol×K	341.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	193.05	J/mol×K	344.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	193.63	J/mol×K	346.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	194.00	J/mol×K	349.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	194.70	J/mol×K	351.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
C_sat	195.12	J/mol×K	353.14	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
η	[0.0003463; 0.0041179]	Pa×s	[194.68; 365.98]

η	0.0041179	Pa×s	194.68	Joback Calculated Property
η	0.0020936	Pa×s	223.23	Joback Calculated Property
η	0.0012409	Pa×s	251.78	Joback Calculated Property
η	0.0008182	Pa×s	280.33	Joback Calculated Property
η	0.0005826	Pa×s	308.88	Joback Calculated Property
η	0.0004394	Pa×s	337.43	Joback Calculated Property
η	0.0003463	Pa×s	365.98	Joback Calculated Property
Δ_vapH	43.40	kJ/mol	380.50	NIST
P_vap	[2.21; 2.21]	kPa	[323.15; 323.15]
P_vap	2.21	kPa	323.15	Excess molar enthalpies and (vapour + liquid) equilibria for mixtures containing N,N-dialkylamides and a,x-dichloroalkanes
P_vap	2.21	kPa	323.15	Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
n₀	[1.45190; 1.45220]		[298.15; 298.15]
n₀	1.45200		298.15	Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
n₀	1.45190		298.15	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
n₀	1.45220		298.15	Isothermal (vapour + liquid) equilibria for (nitromethane or nitroethane + 1,4-dichlorobutane) binary systems at temperatures between (343.15 and 363.15) K
ρ_l	[1110.54; 1143.49]	kg/m³	[288.15; 318.15]

ρ_l	1143.49	kg/m³	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρ_l	1143.43	kg/m³	288.15	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
ρ_l	1135.00	kg/m³	298.15	Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
ρ_l	1133.94	kg/m³	298.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρ_l	1132.57	kg/m³	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρ_l	1132.50	kg/m³	298.15	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
ρ_l	1123.00	kg/m³	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρ_l	1121.61	kg/m³	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρ_l	1121.54	kg/m³	308.15	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
ρ_l	1112.00	kg/m³	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρ_l	1110.61	kg/m³	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρ_l	1110.54	kg/m³	318.15	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
c_sound,fluid	[1215.66; 1286.64]	m/s	[298.15; 318.15]
c_sound,fluid	1286.64	m/s	298.15	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
c_sound,fluid	1251.00	m/s	308.15	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
c_sound,fluid	1215.66	m/s	318.15	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
γ	[0.03; 0.03]	N/m	[293.15; 313.15]

γ	0.03	N/m	293.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	298.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	303.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	308.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	313.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	1143.7
288.15	500.00	1144.1
288.15	1000.00	1144.5
288.15	1500.00	1144.8
288.15	2000.00	1145.2
288.15	2500.00	1145.5
288.15	3000.00	1145.9
288.15	3600.00	1146.4
288.15	4100.00	1146.7
288.15	4600.00	1147.0
288.15	5100.00	1147.4
288.15	5600.00	1147.7
288.15	6100.00	1148.1
288.15	6600.00	1148.5
288.15	7100.00	1148.9
288.15	7600.00	1149.2
288.15	8100.00	1149.5
288.15	8600.00	1149.9
288.15	9200.00	1150.3
288.15	9600.00	1150.7
288.15	10100.00	1151.0
288.15	10600.00	1151.3
288.15	11100.00	1151.7
288.15	11600.00	1152.0
288.15	12100.00	1152.4
288.15	12600.00	1152.7
288.15	13100.00	1153.1
288.15	13500.00	1153.3
288.15	14200.00	1153.8
288.15	14700.00	1154.1
288.15	15200.00	1154.4
288.15	15700.00	1154.8
288.15	16300.00	1155.2
288.15	16800.00	1155.6
288.15	17300.00	1155.9
288.15	17800.00	1156.2
288.15	18300.00	1156.5
288.15	18800.00	1156.8
288.15	19100.00	1157.1
288.15	19700.00	1157.4
288.15	20200.00	1157.8
298.15	100.00	1133.7
298.15	500.00	1134.0
298.15	1000.00	1134.4
298.15	1500.00	1134.8
298.15	2000.00	1135.2
298.15	2500.00	1135.6
298.15	3100.00	1136.1
298.15	3600.00	1136.4
298.15	4100.00	1136.8
298.15	4600.00	1137.2
298.15	5100.00	1137.6
298.15	5600.00	1137.9
298.15	6100.00	1138.4
298.15	6600.00	1138.7
298.15	7100.00	1139.1
298.15	7600.00	1139.4
298.15	8100.00	1139.8
298.15	8600.00	1140.2
298.15	9200.00	1140.6
298.15	9600.00	1141.0
298.15	10100.00	1141.4
298.15	10700.00	1141.8
298.15	11100.00	1142.1
298.15	11600.00	1142.4
298.15	12100.00	1142.8
298.15	12600.00	1143.2
298.15	13100.00	1143.6
298.15	13600.00	1143.9
298.15	14100.00	1144.2
298.15	14700.00	1144.6
298.15	15200.00	1145.0
298.15	15700.00	1145.4
298.15	16200.00	1145.8
298.15	16700.00	1146.1
298.15	17200.00	1146.5
298.15	17800.00	1146.9
298.15	18300.00	1147.2
298.15	18800.00	1147.6
298.15	19200.00	1147.9
298.15	19700.00	1148.2
298.15	20200.00	1148.7
308.15	100.00	1122.3
308.15	500.00	1122.7
308.15	1000.00	1123.1
308.15	1500.00	1123.5
308.15	2000.00	1123.9
308.15	2500.00	1124.3
308.15	3100.00	1124.8
308.15	3600.00	1125.2
308.15	4100.00	1125.6
308.15	4600.00	1126.0
308.15	5100.00	1126.4
308.15	5600.00	1126.9
308.15	6100.00	1127.2
308.15	6600.00	1127.5
308.15	7100.00	1128.0
308.15	7600.00	1128.4
308.15	8100.00	1128.8
308.15	8600.00	1129.2
308.15	9200.00	1129.6
308.15	9600.00	1130.0
308.15	10100.00	1130.4
308.15	10600.00	1130.9
308.15	11100.00	1131.2
308.15	11600.00	1131.5
308.15	12100.00	1131.9
308.15	12600.00	1132.4
308.15	13100.00	1132.6
308.15	13600.00	1133.1
308.15	14100.00	1133.5
308.15	14700.00	1133.9
308.15	15100.00	1134.2
308.15	15700.00	1134.6
308.15	16200.00	1135.0
308.15	16700.00	1135.3
308.15	17200.00	1135.7
308.15	17800.00	1136.1
308.15	18300.00	1136.5
308.15	18800.00	1136.8
308.15	19200.00	1137.2
308.15	19700.00	1137.6
308.15	20200.00	1138.0
318.15	100.00	1112.0
318.15	500.00	1112.4
318.15	1000.00	1112.8
318.15	1500.00	1113.2
318.15	2000.00	1113.7
318.15	2500.00	1114.1
318.15	3100.00	1114.7
318.15	3500.00	1115.0
318.15	4100.00	1115.5
318.15	4600.00	1115.9
318.15	5100.00	1116.3
318.15	5600.00	1116.8
318.15	6100.00	1117.3
318.15	6600.00	1117.7
318.15	7100.00	1118.1
318.15	7600.00	1118.4
318.15	8100.00	1118.9
318.15	8600.00	1119.3
318.15	9200.00	1119.8
318.15	9600.00	1120.2
318.15	10100.00	1120.6
318.15	10600.00	1121.0
318.15	11100.00	1121.4
318.15	11600.00	1121.8
318.15	12100.00	1122.1
318.15	12600.00	1122.6
318.15	13000.00	1123.0
318.15	13600.00	1123.3
318.15	14200.00	1123.9
318.15	14700.00	1124.4
318.15	15200.00	1124.7
318.15	15700.00	1125.1
318.15	16300.00	1125.4
318.15	16800.00	1126.0
318.15	17300.00	1126.3
318.15	17800.00	1126.5
318.15	18300.00	1127.0
318.15	18800.00	1127.4
318.15	19200.00	1127.7
318.15	19700.00	1128.0
318.15	20200.00	1128.4
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	1133.7
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.65]	kPa	[312.79; 432.68]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.62874e+01
Coefficient B			-4.19096e+03
Coefficient C			-5.08480e+01
Temperature range, min.			312.79
Temperature range, max.			432.68

P_vap	1.33	kPa	312.79	Calculated Property
P_vap	2.89	kPa	326.11	Calculated Property
P_vap	5.84	kPa	339.43	Calculated Property
P_vap	11.09	kPa	352.75	Calculated Property
P_vap	19.93	kPa	366.07	Calculated Property
P_vap	34.17	kPa	379.40	Calculated Property
P_vap	56.17	kPa	392.72	Calculated Property
P_vap	88.96	kPa	406.04	Calculated Property
P_vap	136.28	kPa	419.36	Calculated Property
P_vap	202.65	kPa	432.68	Calculated Property
P_vap	[3.53e-03; 3577.43]	kPa	[235.85; 641.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is P_vap in kPa, T in K
Coefficient A			7.77758e+01
Coefficient B			-7.95407e+03
Coefficient C			-9.14431e+00
Coefficient D			4.66169e-06
Coefficient E			0.00000e+00
Temperature range, min.			235.85
Temperature range, max.			641.00

P_vap	3.53e-03	kPa	235.85	Calculated Property
P_vap	0.18	kPa	280.87	Calculated Property
P_vap	2.58	kPa	325.88	Calculated Property
P_vap	17.72	kPa	370.90	Calculated Property
P_vap	74.69	kPa	415.92	Calculated Property
P_vap	227.10	kPa	460.93	Calculated Property
P_vap	550.91	kPa	505.95	Calculated Property
P_vap	1139.60	kPa	550.97	Calculated Property
P_vap	2103.57	kPa	595.98	Calculated Property
P_vap	3577.43	kPa	641.00	Calculated Property

Similar Compounds

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Mixtures

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Sources

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Chemical Properties of Butane, 1,4-dichloro- (CAS 110-56-5)

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