Chemical Properties of Pentane, 1-bromo- (CAS 110-53-2)

InChI

InChI=1S/C5H11Br/c1-2-3-4-5-6/h2-5H2,1H3

InChI Key

YZWKKMVJZFACSU-UHFFFAOYSA-N

Formula

C5H11Br

SMILES

CCCCCBr

Molecular Weight¹

151.04

CAS

110-53-2

Other Names

• 1-Pentyl bromide
• 1-bromopentane
• PENTYLBROMIDE
• amyl bromide
• n-C5H11Br
• n-Pentyl bromide
• n-amyl bromide
• pentyl bromide

• 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).
• 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_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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• 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).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• 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).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3840		KDB
ΔcH°liquid	-3369.40 ± 1.40	kJ/mol	NIST
ΔfG°	5.54	kJ/mol	Joback Calculated Property
ΔfH°gas	-129.80 ± 1.90	kJ/mol	NIST
ΔfH°liquid	-170.40 ± 1.50	kJ/mol	NIST
ΔfusH°	13.99	kJ/mol	Joback Calculated Property
ΔvapH°	[40.90; 41.43]	kJ/mol
ΔvapH°	41.31	kJ/mol	NIST
ΔvapH°	40.90	kJ/mol	NIST
ΔvapH°	41.40 ± 0.10	kJ/mol	NIST
ΔvapH°	41.43 ± 0.02	kJ/mol	NIST
ΔvapH°	41.10 ± 0.10	kJ/mol	NIST
ΔvapH°	41.10 ± 0.10	kJ/mol	NIST
IE	[10.01; 10.10]	eV
IE	10.10 ± 0.01	eV	NIST
IE	10.01	eV	NIST
IE	10.09	eV	NIST
IE	10.10 ± 0.02	eV	NIST
log10WS	[-3.08; -3.07]
log10WS	-3.07		Aq. Solubility Prediction
log10WS	-3.08		Estimated Solubility
logPoct/wat	2.571		Crippen Calculated Property
McVol	98.810	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	3770.00	kPa	KDB
Inp	[806.50; 859.00]
Inp	809.70		NIST
Inp	807.70		NIST
Inp	840.00		NIST
Inp	Outlier 859.00		NIST
Inp	809.70		NIST
Inp	810.20		NIST
Inp	813.00		NIST
Inp	810.90		NIST
Inp	808.50		NIST
Inp	807.70		NIST
Inp	806.50		NIST
Inp	833.80		NIST
Inp	832.70		NIST
Inp	834.00		NIST
Inp	840.00		NIST
Inp	817.70		NIST
Inp	840.00		NIST
Inp	Outlier 859.00		NIST
Inp	830.00		NIST
Inp	848.00		NIST
Inp	835.00		NIST
Inp	823.00		NIST
Inp	836.00		NIST
Inp	822.00		NIST
Inp	819.00		NIST
Inp	843.60		NIST
Inp	830.00		NIST
Inp	836.00		NIST
Inp	822.00		NIST
I	[1042.00; 1091.00]
I	1068.00		NIST
I	1058.00		NIST
I	1044.00		NIST
I	Outlier 1091.00		NIST
I	1055.00		NIST
I	1052.00		NIST
I	1042.00		NIST
I	1068.00		NIST
I	1042.00		NIST
S°liquid	406.77	J/mol×K	NIST
Tboil	[391.10; 403.00]	K
Tboil	402.70	K	KDB
Tboil	403.00	K	NIST
Tboil	402.80	K	NIST
Tboil	402.90	K	NIST
Tboil	402.00 ± 0.40	K	NIST
Tboil	402.70 ± 0.40	K	NIST
Tboil	402.73 ± 0.15	K	NIST
Tboil	391.40 ± 0.50	K	NIST
Tboil	391.10 ± 0.60	K	NIST
Tboil	391.80 ± 1.50	K	NIST
Tc	564.80	K	KDB
Tfus	[178.48; 185.20]	K
Tfus	185.00	K	KDB
Tfus	180.48	K	Aq. Solubility Prediction
Tfus	185.20 ± 0.20	K	NIST
Tfus	184.80 ± 5.00	K	NIST
Tfus	Outlier 178.48 ± 0.20	K	NIST
Tfus	185.10 ± 0.20	K	NIST
Tfus	185.20 ± 0.20	K	NIST
Tfus	185.10 ± 0.20	K	NIST
Vc	0.378	m3/kmol	KDB
Zc	0.3030590		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[167.00; 219.70]	J/mol×K	[190.00; 353.15]
Cp,liquid	172.00	J/mol×K	190.00	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	170.00	J/mol×K	200.00	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	174.90	J/mol×K	206.60	NIST
Cp,liquid	169.00	J/mol×K	210.00	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	168.00	J/mol×K	220.00	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	167.00	J/mol×K	230.00	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	167.00	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	167.00	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	168.00	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	169.00	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	169.00	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	171.00	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	187.88	J/mol×K	284.15	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
Cp,liquid	188.46	J/mol×K	286.65	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
Cp,liquid	189.17	J/mol×K	289.15	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
Cp,liquid	173.00	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	171.59	J/mol×K	290.70	NIST
Cp,liquid	189.85	J/mol×K	291.65	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
Cp,liquid	190.33	J/mol×K	294.15	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
Cp,liquid	190.94	J/mol×K	296.65	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
Cp,liquid	174.00	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	219.70	J/mol×K	298.15	NIST
Cp,liquid	191.57	J/mol×K	299.15	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
Cp,liquid	192.17	J/mol×K	301.65	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
Cp,liquid	193.01	J/mol×K	304.15	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
Cp,liquid	193.53	J/mol×K	306.65	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
Cp,liquid	194.17	J/mol×K	309.15	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
Cp,liquid	194.86	J/mol×K	311.65	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
Cp,liquid	195.60	J/mol×K	314.15	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
Cp,liquid	196.21	J/mol×K	316.65	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
Cp,liquid	196.98	J/mol×K	319.15	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
Cp,liquid	197.61	J/mol×K	321.65	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
Cp,liquid	198.35	J/mol×K	324.15	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
Cp,liquid	199.09	J/mol×K	326.65	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
Cp,liquid	199.80	J/mol×K	329.15	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
Cp,liquid	200.47	J/mol×K	331.65	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
Cp,liquid	201.48	J/mol×K	334.15	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
Cp,liquid	201.57	J/mol×K	336.65	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
Cp,liquid	202.76	J/mol×K	339.15	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
Cp,liquid	203.58	J/mol×K	341.65	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
Cp,liquid	204.33	J/mol×K	344.15	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
Cp,liquid	205.07	J/mol×K	346.65	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
Cp,liquid	205.89	J/mol×K	349.15	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
Cp,liquid	206.69	J/mol×K	351.65	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
Cp,liquid	207.05	J/mol×K	353.15	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
ΔfusH	[11.46; 14.37]	kJ/mol	[185.10; 185.10]
ΔfusH	11.46	kJ/mol	185.10	NIST
ΔfusH	14.37	kJ/mol	185.10	NIST
ΔfusH	14.37	kJ/mol	185.10	NIST
ΔfusH	14.36	kJ/mol	185.10	NIST
ΔfusH	11.46	kJ/mol	185.10	NIST
ΔfusH	14.36	kJ/mol	185.10	NIST
ΔvapH	[34.48; 41.00]	kJ/mol	[368.00; 402.90]
ΔvapH	41.00	kJ/mol	368.00	NIST
ΔvapH	34.48	kJ/mol	402.70	KDB
ΔvapH	35.01	kJ/mol	402.90	NIST
ρl	[1083.40; 1260.30]	kg/m3	[253.15; 393.15]
ρl	1260.30	kg/m3	253.15	Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
ρl	1249.90	kg/m3	263.15	Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
ρl	1239.60	kg/m3	273.15	Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
ρl	1214.90	kg/m3	293.15	Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
ρl	1208.50	kg/m3	298.15	Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
ρl	1177.10	kg/m3	323.15	Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
ρl	1151.00	kg/m3	343.15	Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
ρl	1124.70	kg/m3	363.15	Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
ρl	1097.40	kg/m3	383.15	Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
ρl	1083.40	kg/m3	393.15	Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
ΔfusS	[62.00; 77.61]	J/mol×K	[185.10; 185.10]
ΔfusS	62.00	J/mol×K	185.10	NIST
ΔfusS	77.61	J/mol×K	185.10	NIST
ΔfusS	77.60	J/mol×K	185.10	NIST
ΔfusS	62.00	J/mol×K	185.10	NIST
ΔfusS	77.60	J/mol×K	185.10	NIST
csound,fluid	[666.58; 1240.04]	m/s	[243.73; 423.48]
csound,fluid	1240.04	m/s	243.73	Speed of Sound, Densities, and Isentropic Compressibilities of Liquid 1-Bromoalkanes at Temperatures from (243.15 to 423.15) K
csound,fluid	1137.50	m/s	273.32	Speed of Sound, Densities, and Isentropic Compressibilities of Liquid 1-Bromoalkanes at Temperatures from (243.15 to 423.15) K
csound,fluid	1037.13	m/s	303.22	Speed of Sound, Densities, and Isentropic Compressibilities of Liquid 1-Bromoalkanes at Temperatures from (243.15 to 423.15) K
csound,fluid	972.37	m/s	323.17	Speed of Sound, Densities, and Isentropic Compressibilities of Liquid 1-Bromoalkanes at Temperatures from (243.15 to 423.15) K
csound,fluid	877.57	m/s	353.18	Speed of Sound, Densities, and Isentropic Compressibilities of Liquid 1-Bromoalkanes at Temperatures from (243.15 to 423.15) K
csound,fluid	785.49	m/s	383.23	Speed of Sound, Densities, and Isentropic Compressibilities of Liquid 1-Bromoalkanes at Temperatures from (243.15 to 423.15) K
csound,fluid	725.54	m/s	403.28	Speed of Sound, Densities, and Isentropic Compressibilities of Liquid 1-Bromoalkanes at Temperatures from (243.15 to 423.15) K
csound,fluid	666.58	m/s	423.48	Speed of Sound, Densities, and Isentropic Compressibilities of Liquid 1-Bromoalkanes at Temperatures from (243.15 to 423.15) K

Pressure Dependent Properties

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[125.54; 286.35]	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			6.53400e+00
Coefficient B			5.17020e-01
Coefficient C			-3.19600e-04
Coefficient D			8.24000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	125.54	J/mol×K	273.00	Calculated Property
Cp,gas	153.09	J/mol×K	353.78	Calculated Property
Cp,gas	177.62	J/mol×K	434.56	Calculated Property
Cp,gas	199.37	J/mol×K	515.33	Calculated Property
Cp,gas	218.62	J/mol×K	596.11	Calculated Property
Cp,gas	235.62	J/mol×K	676.89	Calculated Property
Cp,gas	250.63	J/mol×K	757.67	Calculated Property
Cp,gas	263.92	J/mol×K	838.44	Calculated Property
Cp,gas	275.74	J/mol×K	919.22	Calculated Property
Cp,gas	286.35	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0070358; 0.0003220]	Pa×s	[184.41; 395.36]	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			-1.07374e+01
Coefficient B			1.06602e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			184.41
Temperature range, max.			395.36
η	0.0070358	Pa×s	184.41	Calculated Property
η	0.0036661	Pa×s	207.85	Calculated Property
η	0.0021801	Pa×s	231.29	Calculated Property
η	0.0014266	Pa×s	254.73	Calculated Property
η	0.0010027	Pa×s	278.17	Calculated Property
η	0.0007444	Pa×s	301.61	Calculated Property
η	0.0005769	Pa×s	325.04	Calculated Property
η	0.0004627	Pa×s	348.48	Calculated Property
η	0.0003816	Pa×s	371.92	Calculated Property
η	0.0003220	Pa×s	395.36	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[300.87; 421.19]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.74893e+01
Coefficient B			-5.01695e+03
Coefficient C			-9.21200e+00
Temperature range, min.			300.87
Temperature range, max.			421.19
Pvap	1.33	kPa	300.87	Calculated Property
Pvap	2.83	kPa	314.24	Calculated Property
Pvap	5.65	kPa	327.61	Calculated Property
Pvap	10.67	kPa	340.98	Calculated Property
Pvap	19.16	kPa	354.35	Calculated Property
Pvap	32.95	kPa	367.71	Calculated Property
Pvap	54.50	kPa	381.08	Calculated Property
Pvap	87.04	kPa	394.45	Calculated Property
Pvap	134.72	kPa	407.82	Calculated Property
Pvap	202.67	kPa	421.19	Calculated Property
Pvap	[1.31; 3920.12]	kPa	[294.15; 564.76]	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			2.04728e+02
Coefficient B			-1.21476e+04
Coefficient C			-2.91790e+01
Coefficient D			3.11793e-05
Coefficient E			0.00000e+00
Temperature range, min.			294.15
Temperature range, max.			564.76
Pvap	1.31	kPa	294.15	Calculated Property
Pvap	6.31	kPa	324.22	Calculated Property
Pvap	21.55	kPa	354.29	Calculated Property
Pvap	58.46	kPa	384.35	Calculated Property
Pvap	135.98	kPa	414.42	Calculated Property
Pvap	286.23	kPa	444.49	Calculated Property
Pvap	566.82	kPa	474.56	Calculated Property
Pvap	1086.48	kPa	504.62	Calculated Property
Pvap	2058.97	kPa	534.69	Calculated Property
Pvap	3920.12	kPa	564.76	Calculated Property

Similar Compounds

Find more compounds similar to Pentane, 1-bromo-.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• 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
• Density of Some 1-Bromoalkanes within the Temperature Range from (243.15 to 423.15) K
• Speed of Sound, Densities, and Isentropic Compressibilities of Liquid 1-Bromoalkanes at Temperatures from (243.15 to 423.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility 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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