Chemical Properties of Propane, 1,3-dibromo- (CAS 109-64-8)

InChI

InChI=1S/C3H6Br2/c4-2-1-3-5/h1-3H2

InChI Key

VEFLKXRACNJHOV-UHFFFAOYSA-N

Formula

C3H6Br2

SMILES

BrCCCBr

Molecular Weight¹

201.89

CAS

109-64-8

Other Names

• 1,3-dibromopropane
• CH2BrCH2CH2Br
• Dibromo-1,3 propane
• Trimethylene bromide
• trimethylene dibromide
• «alpha»,«gamma»-Dibromopropane
• «omega»,«omega»'-Dibromopropane

• 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_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (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.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.5027		Relay (1.0) Calculated Property
ΔfG°	3.02	kJ/mol	Joback Calculated Property
ΔfH°gas	-67.72	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	14.10	kJ/mol	Joback Calculated Property
ΔvapH°	[45.30; 47.60]	kJ/mol
ΔvapH°	47.46	kJ/mol	NIST
ΔvapH°	47.60	kJ/mol	NIST
ΔvapH°	47.45 ± 0.10	kJ/mol	NIST
ΔvapH°	45.30	kJ/mol	NIST
IE	[10.07; 10.26]	eV
IE	10.07 ± 0.02	eV	NIST
IE	10.10	eV	NIST
IE	10.26	eV	NIST
log10WS	-2.08		Aq. Solubility Prediction
logPoct/wat	2.166		Crippen Calculated Property
McVol	88.130	ml/mol	McGowan Calculated Property
Pc	5343.52	kPa	Joback Calculated Property
Inp	[919.00; 989.00]
Inp	971.00		NIST
Inp	989.00		NIST
Inp	936.00		NIST
Inp	955.00		NIST
Inp	919.00		NIST
Inp	963.70		NIST
Inp	937.70		NIST
I	[1419.00; 1460.00]
I	1419.00		NIST
I	1422.00		NIST
I	1460.00		NIST
I	1419.00		NIST
Tboil	[343.70; 440.50]	K
Tboil	440.05	K	KDB
Tboil	440.00	K	NIST
Tboil	440.50	K	NIST
Tboil	Outlier 343.70 ± 0.30	K	NIST
Tboil	439.90 ± 0.30	K	NIST
Tboil	440.10 ± 0.20	K	NIST
Tboil	440.10 ± 0.20	K	NIST
Tboil	437.00 ± 4.00	K	NIST
Tc	629.05	K	Relay (1.0) Calculated Property
Tfus	[237.00; 239.10]	K
Tfus	238.65	K	KDB
Tfus	239.10	K	Aq. Solubility Prediction
Tfus	238.95 ± 0.60	K	NIST
Tfus	237.00 ± 0.40	K	NIST
Tfus	238.85 ± 0.50	K	NIST
Ttriple	[238.60; 238.60]	K
Ttriple	238.60 ± 0.20	K	NIST
Ttriple	238.60 ± 0.20	K	NIST
Vc	0.321	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[123.51; 155.26]	J/mol×K	[400.56; 609.27]
Cp,gas	123.51	J/mol×K	400.56	Joback Calculated Property
Cp,gas	129.70	J/mol×K	435.34	Joback Calculated Property
Cp,gas	135.49	J/mol×K	470.13	Joback Calculated Property
Cp,gas	140.93	J/mol×K	504.91	Joback Calculated Property
Cp,gas	146.02	J/mol×K	539.70	Joback Calculated Property
Cp,gas	150.79	J/mol×K	574.48	Joback Calculated Property
Cp,gas	155.26	J/mol×K	609.27	Joback Calculated Property
Cp,liquid	[155.00; 173.00]	J/mol×K	[240.00; 360.00]
Cp,liquid	155.00	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	156.10	J/mol×K	245.70	NIST
Cp,liquid	156.00	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	158.00	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	159.00	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	160.00	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	161.00	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	162.24	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	162.41	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	162.57	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	162.74	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	162.00	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	162.92	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	163.09	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	163.26	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	163.44	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	163.62	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	159.00	J/mol×K	298.00	NIST
Cp,liquid	163.73	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	164.00	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	163.70	J/mol×K	298.15	NIST
Cp,liquid	163.79	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	164.00	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	163.97	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	164.15	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	164.34	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	164.52	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	164.71	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	164.89	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	165.08	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	166.00	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	165.27	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	165.46	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	165.65	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	165.85	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	166.04	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	166.24	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	166.43	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	167.00	J/mol×K	320.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	166.63	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	166.83	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	167.04	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	167.24	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	167.44	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	167.65	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	169.00	J/mol×K	330.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	167.86	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	168.06	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	168.27	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	168.49	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	168.70	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	168.91	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	169.13	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	170.00	J/mol×K	340.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	169.35	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	169.56	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	169.78	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	170.00	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	170.23	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	170.45	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	170.68	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	172.00	J/mol×K	350.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	170.90	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	171.13	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	171.36	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	171.51	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
Cp,liquid	173.00	J/mol×K	360.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
η	[0.0004689; 0.0030679]	Pa×s	[243.17; 400.56]
η	0.0030679	Pa×s	243.17	Joback Calculated Property
η	0.0019261	Pa×s	269.40	Joback Calculated Property
η	0.0013134	Pa×s	295.63	Joback Calculated Property
η	0.0009533	Pa×s	321.87	Joback Calculated Property
η	0.0007262	Pa×s	348.10	Joback Calculated Property
η	0.0005746	Pa×s	374.33	Joback Calculated Property
η	0.0004689	Pa×s	400.56	Joback Calculated Property
ΔfusH	[14.64; 14.64]	kJ/mol	[238.60; 238.60]
ΔfusH	14.64	kJ/mol	238.60	NIST
ΔfusH	14.64	kJ/mol	238.60	NIST
ΔfusH	14.64	kJ/mol	238.60	NIST
ΔfusH	14.64	kJ/mol	238.60	NIST
ΔvapH	[44.80; 47.89]	kJ/mol	[308.00; 439.40]
ΔvapH	47.30 ± 0.10	kJ/mol	308.00	NIST
ΔvapH	46.70 ± 0.10	kJ/mol	315.00	NIST
ΔvapH	46.10 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	45.50 ± 0.10	kJ/mol	330.00	NIST
ΔvapH	44.80 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	46.60	kJ/mol	372.00	NIST
ΔvapH	47.80	kJ/mol	419.00	NIST
ΔvapH	47.89	kJ/mol	439.40	NIST
n0	1.52040		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
ρl	[1941.18; 1980.22]	kg/m3	[292.55; 314.58]
ρl	1980.22	kg/m3	292.55	Thermodynamic and Acoustic Properties of 1,3-Dibromopropane and 1,5-Dibromopentane within the Temperature Range From 293K to 313K at Pressures up to 100MPa
ρl	1970.22	kg/m3	297.98	Thermodynamic and Acoustic Properties of 1,3-Dibromopropane and 1,5-Dibromopentane within the Temperature Range From 293K to 313K at Pressures up to 100MPa
ρl	1961.58	kg/m3	303.07	Thermodynamic and Acoustic Properties of 1,3-Dibromopropane and 1,5-Dibromopentane within the Temperature Range From 293K to 313K at Pressures up to 100MPa
ρl	1952.84	kg/m3	308.02	Thermodynamic and Acoustic Properties of 1,3-Dibromopropane and 1,5-Dibromopentane within the Temperature Range From 293K to 313K at Pressures up to 100MPa
ρl	1941.18	kg/m3	314.58	Thermodynamic and Acoustic Properties of 1,3-Dibromopropane and 1,5-Dibromopentane within the Temperature Range From 293K to 313K at Pressures up to 100MPa
ΔfusS	[61.40; 61.40]	J/mol×K	[238.60; 238.60]
ΔfusS	61.40	J/mol×K	238.60	NIST
ΔfusS	61.40	J/mol×K	238.60	NIST
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

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 294.08]	kPa	[330.28; 467.14]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.61869e+01
Coefficient B			-4.23517e+03
Coefficient C			-6.39080e+01
Temperature range, min.			330.28
Temperature range, max.			467.14
Pvap	1.33	kPa	330.28	Calculated Property
Pvap	3.15	kPa	345.49	Calculated Property
Pvap	6.80	kPa	360.69	Calculated Property
Pvap	13.63	kPa	375.90	Calculated Property
Pvap	25.62	kPa	391.11	Calculated Property
Pvap	45.51	kPa	406.31	Calculated Property
Pvap	77.01	kPa	421.52	Calculated Property
Pvap	124.84	kPa	436.73	Calculated Property
Pvap	194.85	kPa	451.93	Calculated Property
Pvap	294.08	kPa	467.14	Calculated Property
Pvap	[0.15; 102.57]	kPa	[283.15; 441.15]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			3.97029e+01
Coefficient B			-6.17431e+03
Coefficient C			-3.53806e+00
Coefficient D			2.40591e-06
Temperature range, min.			283.15
Temperature range, max.			441.15
Pvap	0.15	kPa	283.15	Calculated Property
Pvap	0.45	kPa	300.71	Calculated Property
Pvap	1.17	kPa	318.26	Calculated Property
Pvap	2.74	kPa	335.82	Calculated Property
Pvap	5.88	kPa	353.37	Calculated Property
Pvap	11.67	kPa	370.93	Calculated Property
Pvap	21.71	kPa	388.48	Calculated Property
Pvap	38.17	kPa	406.04	Calculated Property
Pvap	63.92	kPa	423.59	Calculated Property
Pvap	102.57	kPa	441.15	Calculated Property

Similar Compounds

Find more compounds similar to Propane, 1,3-dibromo-.

Mixtures

• Formic acid, butyl ester + Propane, 1,3-dibromo-
• Propane, 1,3-dibromo- + Acetic acid, butyl ester
• Propanoic acid, butyl ester + Propane, 1,3-dibromo-
• Butanoic acid, butyl ester + Propane, 1,3-dibromo-
• Ethyl formate + Propane, 1,3-dibromo-
• Propane, 1,3-dibromo- + Ethyl Acetate
• Propanoic acid, ethyl ester + Propane, 1,3-dibromo-
• Propane, 1,3-dibromo- + Butanoic acid, ethyl ester
• Pentanoic acid, ethyl ester + Propane, 1,3-dibromo-
• Propane, 1,3-dibromo- + Methyl formate
• Propane, 1,3-dibromo- + Acetic acid, methyl ester
• Propane, 1,3-dibromo- + Methyl propionate
• Butanoic acid, methyl ester + Propane, 1,3-dibromo-
• Propane, 1,3-dibromo- + Methyl valerate

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Thermodynamic and Acoustic Properties of 1,3-Dibromopropane and 1,5-Dibromopentane within the Temperature Range From 293K to 313K at Pressures up to 100MPa
• 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
• Aqueous Solubility Prediction Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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