Chemical Properties of Butane, 1,4-dibromo- (CAS 110-52-1)

InChI

InChI=1S/C4H8Br2/c5-3-1-2-4-6/h1-4H2

InChI Key

ULTHEAFYOOPTTB-UHFFFAOYSA-N

Formula

C4H8Br2

SMILES

BrCCCCBr

Molecular Weight¹

215.91

CAS

110-52-1

Other Names

• 1,4-Butylene bromide
• 1,4-Dibrombutan
• 1,4-dibromobutane
• BrCH2CH2CH2CH2Br
• DBB
• Dibromo-1,4 butane
• tetramethylene dibromide

• 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_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.
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (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.

Physical Properties

Property	Value	Unit	Source
ω	0.5240		Relay (1.0) Calculated Property
ΔfG°	11.44	kJ/mol	Joback Calculated Property
ΔfH°gas	-85.98	kJ/mol	NIST
ΔfH°liquid	-140.10 ± 5.10	kJ/mol	NIST
ΔfusH°	16.69	kJ/mol	Joback Calculated Property
ΔvapH°	[52.60; 53.09]	kJ/mol
ΔvapH°	53.09	kJ/mol	NIST
ΔvapH°	52.60	kJ/mol	NIST
ΔvapH°	53.05	kJ/mol	NIST
ΔvapH°	53.09 ± 0.12	kJ/mol	NIST
IE	[10.15; 10.27]	eV
IE	10.15	eV	NIST
IE	10.27	eV	NIST
log10WS	-3.01		Relay (1.0) Calculated Property
logPoct/wat	2.556		Crippen Calculated Property
McVol	102.220	ml/mol	McGowan Calculated Property
Pc	4665.71	kPa	Joback Calculated Property
Inp	[1042.00; 1114.00]
Inp	1094.00		NIST
Inp	1114.00		NIST
Inp	1057.00		NIST
Inp	1094.00		NIST
Inp	1042.00		NIST
Inp	1084.60		NIST
Inp	1057.70		NIST
Inp	1094.00		NIST
I	[1559.00; 1584.00]
I	1559.00		NIST
I	1584.00		NIST
I	1561.00		NIST
I	1559.00		NIST
Tboil	[466.00; 471.00]	K
Tboil	470.20	K	NIST
Tboil	466.00 ± 3.00	K	NIST
Tboil	471.00 ± 3.00	K	NIST
Tc	648.52	K	Relay (1.0) Calculated Property
Tfus	252.10 ± 0.50	K	NIST
Vc	0.374	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[189.62; 202.14]	J/mol×K	[285.15; 355.15]
Cp,liquid	189.62	J/mol×K	285.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	189.85	J/mol×K	286.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	190.08	J/mol×K	288.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	190.32	J/mol×K	289.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	190.55	J/mol×K	291.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	190.79	J/mol×K	292.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	191.03	J/mol×K	294.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	191.27	J/mol×K	295.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	191.52	J/mol×K	297.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	191.68	J/mol×K	298.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	191.20	J/mol×K	298.15	NIST
Cp,liquid	191.76	J/mol×K	298.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	192.01	J/mol×K	300.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	192.26	J/mol×K	301.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	192.51	J/mol×K	303.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	192.76	J/mol×K	304.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	193.01	J/mol×K	306.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	193.26	J/mol×K	307.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	193.52	J/mol×K	309.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	193.78	J/mol×K	310.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	194.04	J/mol×K	312.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	194.30	J/mol×K	313.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	194.56	J/mol×K	315.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	194.82	J/mol×K	316.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	195.09	J/mol×K	318.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	195.35	J/mol×K	319.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	195.62	J/mol×K	321.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	195.89	J/mol×K	322.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	196.16	J/mol×K	324.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	196.44	J/mol×K	325.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	196.71	J/mol×K	327.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	196.99	J/mol×K	328.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	197.27	J/mol×K	330.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	197.55	J/mol×K	331.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	197.83	J/mol×K	333.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	198.11	J/mol×K	334.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	198.40	J/mol×K	336.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	198.68	J/mol×K	337.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	198.97	J/mol×K	339.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	199.26	J/mol×K	340.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	199.55	J/mol×K	342.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	199.84	J/mol×K	343.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	200.14	J/mol×K	345.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	200.43	J/mol×K	346.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	200.73	J/mol×K	348.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	201.03	J/mol×K	349.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	201.33	J/mol×K	351.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	201.63	J/mol×K	352.65	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	201.93	J/mol×K	354.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
Cp,liquid	202.14	J/mol×K	355.15	Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
ΔvapH	[49.40; 51.40]	kJ/mol	[387.50; 447.50]
ΔvapH	49.40	kJ/mol	387.50	NIST
ΔvapH	51.40	kJ/mol	447.50	NIST
n0	1.51630		298.15	Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6
γ	[0.04; 0.04]	N/m	[293.15; 313.15]
γ	0.04	N/m	293.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.04	N/m	298.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.04	N/m	303.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.04	N/m	308.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.04	N/m	313.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	[337.20; 338.00]	K	[0.80; 0.80]
Tboilr	337.20	K	0.80	NIST
Tboilr	338.00	K	0.80	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[118.31; 243.83]	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			1.56340e+01
Coefficient B			4.60200e-01
Coefficient C			-3.36600e-04
Coefficient D			1.04600e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	118.31	J/mol×K	273.00	Calculated Property
Cp,gas	140.95	J/mol×K	353.78	Calculated Property
Cp,gas	160.64	J/mol×K	434.56	Calculated Property
Cp,gas	177.72	J/mol×K	515.33	Calculated Property
Cp,gas	192.51	J/mol×K	596.11	Calculated Property
Cp,gas	205.36	J/mol×K	676.89	Calculated Property
Cp,gas	216.58	J/mol×K	757.67	Calculated Property
Cp,gas	226.51	J/mol×K	838.44	Calculated Property
Cp,gas	235.49	J/mol×K	919.22	Calculated Property
Cp,gas	243.83	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0032981; 0.0003900]	Pa×s	[252.10; 440.97]	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			-1.06991e+01
Coefficient B			1.25664e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			252.10
Temperature range, max.			440.97
η	0.0032981	Pa×s	252.10	Calculated Property
η	0.0022486	Pa×s	273.09	Calculated Property
η	0.0016192	Pa×s	294.07	Calculated Property
η	0.0012181	Pa×s	315.06	Calculated Property
η	0.0009495	Pa×s	336.04	Calculated Property
η	0.0007622	Pa×s	357.03	Calculated Property
η	0.0006269	Pa×s	378.01	Calculated Property
η	0.0005263	Pa×s	399.00	Calculated Property
η	0.0004497	Pa×s	419.98	Calculated Property
η	0.0003900	Pa×s	440.97	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[353.08; 498.51]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.51599e+01
Coefficient B			-4.23974e+03
Coefficient C			-6.80070e+01
Temperature range, min.			353.08
Temperature range, max.			498.51
Pvap	1.33	kPa	353.08	Calculated Property
Pvap	2.96	kPa	369.24	Calculated Property
Pvap	6.06	kPa	385.40	Calculated Property
Pvap	11.58	kPa	401.56	Calculated Property
Pvap	20.83	kPa	417.72	Calculated Property
Pvap	35.58	kPa	433.87	Calculated Property
Pvap	58.08	kPa	450.03	Calculated Property
Pvap	91.12	kPa	466.19	Calculated Property
Pvap	138.03	kPa	482.35	Calculated Property
Pvap	202.66	kPa	498.51	Calculated Property
Pvap	[4.00; 320.55]	kPa	[375.15; 520.15]	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			9.74283e+01
Coefficient B			-1.01050e+04
Coefficient C			-1.17919e+01
Coefficient D			5.60527e-06
Coefficient E			0.00000e+00
Temperature range, min.			375.15
Temperature range, max.			520.15
Pvap	4.00	kPa	375.15	Calculated Property
Pvap	7.92	kPa	391.26	Calculated Property
Pvap	14.69	kPa	407.37	Calculated Property
Pvap	25.76	kPa	423.48	Calculated Property
Pvap	42.98	kPa	439.59	Calculated Property
Pvap	68.71	kPa	455.71	Calculated Property
Pvap	105.76	kPa	471.82	Calculated Property
Pvap	157.45	kPa	487.93	Calculated Property
Pvap	227.60	kPa	504.04	Calculated Property
Pvap	320.55	kPa	520.15	Calculated Property
Pvap	[0.13; 100.11]	kPa	[305.00; 470.70]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.52214e+01
Coefficient B			-4.58197e+03
Coefficient C			-3.90570e+01
Reference			Stull, 1947
Temperature range, min.			305.00
Temperature range, max.			470.70
Pvap	0.13	kPa	305.00	Calculated Property
Pvap	0.41	kPa	323.41	Calculated Property
Pvap	1.09	kPa	341.82	Calculated Property
Pvap	2.60	kPa	360.23	Calculated Property
Pvap	5.63	kPa	378.64	Calculated Property
Pvap	11.28	kPa	397.06	Calculated Property
Pvap	21.09	kPa	415.47	Calculated Property
Pvap	37.20	kPa	433.88	Calculated Property
Pvap	62.38	kPa	452.29	Calculated Property
Pvap	100.11	kPa	470.70	Calculated Property

Similar Compounds

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

Mixtures

• Formic acid, butyl ester + Butane, 1,4-dibromo-
• Acetic acid, butyl ester + Butane, 1,4-dibromo-
• Propanoic acid, butyl ester + Butane, 1,4-dibromo-
• Butanoic acid, butyl ester + Butane, 1,4-dibromo-
• Ethyl formate + Butane, 1,4-dibromo-
• Ethyl Acetate + Butane, 1,4-dibromo-
• Propanoic acid, ethyl ester + Butane, 1,4-dibromo-
• Butanoic acid, ethyl ester + Butane, 1,4-dibromo-
• Pentanoic acid, ethyl ester + Butane, 1,4-dibromo-
• Methyl formate + Butane, 1,4-dibromo-
• Acetic acid, methyl ester + Butane, 1,4-dibromo-
• Methyl propionate + Butane, 1,4-dibromo-
• Butanoic acid, methyl ester + Butane, 1,4-dibromo-
• Methyl valerate + Butane, 1,4-dibromo-

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6
• Thermodynamic study of (alkyl esters + alpha,omega-alkyl dihalides) IV: Hex and Vex for 25 binary mixtures {xC(u-1)H(2u-1)CO2CH3 + (1-x)alpha,omega-BrCH2(CH2)(v-2)CH2Br}, where u = 1 to 5, alpha = 1 and v = omega = 2 to 6
• Thermodynamic study of (alkyl esters + alpha,beta-alkyl dihalides) VI.H and V for 20 binary mixtures {xCu-1H2u-1CO2(CH2)3CH3 + (1 - x)alpha,omega-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, alpha = 1, and v = omega = 2 to 6
• The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
• Heat Capacity of alpha,omega-Bromochloroalkanes and ?,?-Dibromoalkanes: Their Dependence on the Hydrocarbon Chain Length and Temperature (285.15 to 355.15) K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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