Chemical Properties of 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.

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	0.3064		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ΔcH°liquid	-2534.80 ± 1.90	kJ/mol	NIST
ΔfG°	-41.06	kJ/mol	Joback Calculated Property
ΔfH°gas	-183.40 ± 1.90	kJ/mol	NIST
ΔfH°liquid	[-229.80; -229.50]	kJ/mol
ΔfH°liquid	-229.80 ± 1.90	kJ/mol	NIST
ΔfH°liquid	-229.50	kJ/mol	NIST
ΔfusH°	14.51	kJ/mol	Joback Calculated Property
ΔvapH°	[46.36; 46.70]	kJ/mol
ΔvapH°	46.36	kJ/mol	NIST
ΔvapH°	Outlier 46.70	kJ/mol	NIST
ΔvapH°	46.50 ± 0.10	kJ/mol	NIST
ΔvapH°	46.40	kJ/mol	NIST
ΔvapH°	46.37 ± 0.02	kJ/mol	NIST
ΔvapH°	46.40 ± 0.10	kJ/mol	NIST
ΔvapH°	46.40 ± 0.10	kJ/mol	NIST
ΔvapH°	46.36 ± 0.02	kJ/mol	NIST
IE	11.03	eV	NIST
log10WS	-2.45		Relay (1.0) Calculated Property
logPoct/wat	2.244		Crippen Calculated Property
McVol	91.700	ml/mol	McGowan Calculated Property
Pc	3694.31	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Inp	[867.40; 898.10]
Inp	867.40		NIST
Inp	895.00		NIST
Inp	874.00		NIST
Inp	874.00		NIST
Inp	874.00		NIST
Inp	874.00		NIST
Inp	898.10		NIST
Inp	894.10		NIST
Inp	874.00		NIST
Inp	894.10		NIST
Tboil	[308.15; 435.20]	K
Tboil	428.15	K	KDB
Tboil	435.20	K	NIST
Tboil	433.00	K	NIST
Tboil	427.10	K	NIST
Tboil	428.15 ± 1.50	K	NIST
Tboil	Outlier 322.00 ± 3.00	K	NIST
Tboil	427.15 ± 4.00	K	NIST
Tboil	434.65 ± 5.00	K	NIST
Tboil	426.25 ± 2.00	K	NIST
Tboil	Outlier 308.15 ± 2.50	K	NIST
Tboil	427.05 ± 0.50	K	NIST
Tboil	428.00 ± 1.00	K	NIST
Tboil	426.65 ± 0.50	K	NIST
Tc	646.70	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tfus	[234.50; 235.50]	K
Tfus	235.50	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	234.50 ± 0.40	K	NIST
Vc	0.350	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[183.59; 184.00]	J/mol×K	[298.15; 298.15]
Cp,liquid	184.00	J/mol×K	298.15	NIST
Cp,liquid	183.59	J/mol×K	298.15	NIST
Csat	[181.25; 195.12]	J/mol×K	[284.16; 353.14]
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
Csat	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
ΔvapH	43.40	kJ/mol	380.50	NIST
Pvap	[2.21; 2.21]	kPa	[323.15; 323.15]
Pvap	2.21	kPa	323.15	Excess molar enthalpies and (vapour + liquid) equilibria for mixtures containing N,N-dialkylamides and a,x-dichloroalkanes
Pvap	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
ρl	[1110.54; 1143.49]	kg/m3	[288.15; 318.15]
ρl	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
ρl	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
ρl	1135.00	kg/m3	298.15	Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
ρl	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
ρl	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
ρl	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
ρl	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
ρl	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
ρl	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
ρl	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
ρl	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
ρl	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
csound,fluid	[1215.66; 1286.64]	m/s	[298.15; 318.15]
csound,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
csound,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
csound,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
Cp,gas	[117.15; 242.23]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.50340e+01
Coefficient B			3.97400e-01
Coefficient C			-2.34600e-04
Coefficient D			5.44000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	117.15	J/mol×K	273.00	Calculated Property
Cp,gas	138.67	J/mol×K	353.78	Calculated Property
Cp,gas	157.89	J/mol×K	434.56	Calculated Property
Cp,gas	174.97	J/mol×K	515.33	Calculated Property
Cp,gas	190.09	J/mol×K	596.11	Calculated Property
Cp,gas	203.41	J/mol×K	676.89	Calculated Property
Cp,gas	215.12	J/mol×K	757.67	Calculated Property
Cp,gas	225.37	J/mol×K	838.44	Calculated Property
Cp,gas	234.36	J/mol×K	919.22	Calculated Property
Cp,gas	242.23	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0016617; 0.0002020]	Pa×s	[235.00; 452.69]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.07817e+01
Coefficient B			1.02972e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			235.00
Temperature range, max.			452.69
η	0.0016617	Pa×s	235.00	Calculated Property
η	0.0011040	Pa×s	259.19	Calculated Property
η	0.0007865	Pa×s	283.38	Calculated Property
η	0.0005910	Pa×s	307.56	Calculated Property
η	0.0004630	Pa×s	331.75	Calculated Property
η	0.0003749	Pa×s	355.94	Calculated Property
η	0.0003119	Pa×s	380.13	Calculated Property
η	0.0002652	Pa×s	404.31	Calculated Property
η	0.0002297	Pa×s	428.50	Calculated Property
η	0.0002020	Pa×s	452.69	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[312.79; 432.68]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap 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
Pvap	1.33	kPa	312.79	Calculated Property
Pvap	2.89	kPa	326.11	Calculated Property
Pvap	5.84	kPa	339.43	Calculated Property
Pvap	11.09	kPa	352.75	Calculated Property
Pvap	19.93	kPa	366.07	Calculated Property
Pvap	34.17	kPa	379.40	Calculated Property
Pvap	56.17	kPa	392.72	Calculated Property
Pvap	88.96	kPa	406.04	Calculated Property
Pvap	136.28	kPa	419.36	Calculated Property
Pvap	202.65	kPa	432.68	Calculated Property
Pvap	[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 Pvap 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
Pvap	3.53e-03	kPa	235.85	Calculated Property
Pvap	0.18	kPa	280.87	Calculated Property
Pvap	2.58	kPa	325.88	Calculated Property
Pvap	17.72	kPa	370.90	Calculated Property
Pvap	74.69	kPa	415.92	Calculated Property
Pvap	227.10	kPa	460.93	Calculated Property
Pvap	550.91	kPa	505.95	Calculated Property
Pvap	1139.60	kPa	550.97	Calculated Property
Pvap	2103.57	kPa	595.98	Calculated Property
Pvap	3577.43	kPa	641.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[235.15; 436.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			6.98578e-02
Coefficient B			-1.17400e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			235.15
Temperature range, max.			436.15
γ	0.04	N/m	235.15	Calculated Property
γ	0.04	N/m	257.48	Calculated Property
γ	0.04	N/m	279.82	Calculated Property
γ	0.03	N/m	302.15	Calculated Property
γ	0.03	N/m	324.48	Calculated Property
γ	0.03	N/m	346.82	Calculated Property
γ	0.03	N/m	369.15	Calculated Property
γ	0.02	N/m	391.48	Calculated Property
γ	0.02	N/m	413.82	Calculated Property
γ	0.02	N/m	436.15	Calculated Property

Similar Compounds

Find more compounds similar to Butane, 1,4-dichloro-.

Mixtures

• Butane, 1,4-dichloro- + Methyl formate
• Ethyl formate + Butane, 1,4-dichloro-
• Formic acid, propyl ester + Butane, 1,4-dichloro-
• Formic acid, butyl ester + Butane, 1,4-dichloro-
• Formic acid, pentyl ester + Butane, 1,4-dichloro-
• Butane, 1,4-dichloro- + Methane, nitro-
• Propanoic acid, butyl ester + Butane, 1,4-dichloro-
• Butane, 1,4-dichloro- + Acetic acid, butyl ester
• Butanoic acid, butyl ester + Butane, 1,4-dichloro-
• Butane, 1,4-dichloro- + Ethyl Acetate
• Butane, 1,4-dichloro- + Butanoic acid, ethyl ester
• Pentanoic acid, ethyl ester + Butane, 1,4-dichloro-
• Propanoic acid, ethyl ester + Butane, 1,4-dichloro-
• Butane, 1,4-dichloro- + Ethane, nitro-
• Butane, 1,4-dichloro- + Cyclopentanone
• 2-Butanone + Butane, 1,4-dichloro-
• 2-Pyrrolidinone, 1-methyl- + Butane, 1,4-dichloro-
• Formamide, N,N-dimethyl- + Butane, 1,4-dichloro-
• Butane, 1,4-dichloro- + N,N-Dimethylacetamide
• Butane, 1,4-dichloro- + Acetic acid, propyl ester

Find more mixtures with Butane, 1,4-dichloro-.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• 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
• 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
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) V. Hex and Vex for 25 binary mixtures {xCu-1H2u-1CO2CH3 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
• 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 molar enthalpies and (vapour + liquid) equilibria for mixtures containing N,N-dialkylamides and a,x-dichloroalkanes
• Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) VII. HE m and VE m for 20 binary mixtures {xCu 1H2u 1CO2C3H7 + (1 x)a,x-ClCH2(CH2)v 2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6. An analysis of behavior using the COSMO-RS methodology
• Isothermal (vapour + liquid) equilibria for (nitromethane or nitroethane + 1,4-dichlorobutane) binary systems at temperatures between (343.15 and 363.15) K
• Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
• The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
• Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
• 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 + r,o-Dichloroalkane
• 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 Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) 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
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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