Chemical Properties of IODOBENZENE (CAS 591-50-4)

InChI

InChI=1S/C6H5I/c7-6-4-2-1-3-5-6/h1-5H

InChI Key

SNHMUERNLJLMHN-UHFFFAOYSA-N

Formula

C6H5I

SMILES

Ic1ccccc1

Molecular Weight¹

204.01

CAS

591-50-4

Other Names

• Benzene iodide
• benzene, iodo-
• phenyl iodide

• 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_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• 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).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : 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).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2460; 0.2490]
ω	0.2460		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2466		ChemSep v8.3 pure component data Compiled value
ω	0.2490		KDB
ΔcH°liquid	[-3192.80; -3192.80]	kJ/mol
ΔcH°liquid	-3192.80 ± 4.20	kJ/mol	NIST
ΔcH°liquid	-3192.80 ± 4.20	kJ/mol	NIST
μ	[1.40; 1.70]	debye
μ	1.70	debye	ChemSep v8.3 pure component data Compiled value
μ	1.40	debye	KDB
ΔfG°	[187.90; 190.20]	kJ/mol
ΔfG°	190.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	187.90	kJ/mol	KDB
ΔfH°gas	[161.90; 165.00]	kJ/mol
ΔfH°gas	161.90 ± 1.10	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	164.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	162.70	kJ/mol	KDB
ΔfH°gas	165.00 ± 5.90	kJ/mol	NIST
ΔfH°liquid	117.00 ± 4.20	kJ/mol	NIST
ΔfusH°	9.74	kJ/mol	Joback Calculated Property
ΔvapH°	[47.40; 48.90]	kJ/mol
ΔvapH°	47.40	kJ/mol	NIST
ΔvapH°	48.90	kJ/mol	NIST
ΔvapH°	47.70 ± 4.20	kJ/mol	NIST
IE	[8.67; 9.05]	eV
IE	8.72 ± 0.04	eV	NIST
IE	8.79	eV	NIST
IE	8.75	eV	NIST
IE	8.69	eV	NIST
IE	8.79	eV	NIST
IE	8.70	eV	NIST
IE	Outlier 9.05	eV	NIST
IE	8.77 ± 0.02	eV	NIST
IE	8.67	eV	NIST
IE	8.73 ± 0.01	eV	NIST
IE	8.69	eV	NIST
IE	8.73 ± 0.03	eV	NIST
IE	8.80	eV	NIST
IE	8.67	eV	NIST
log10WS	[-3.01; -2.89]
log10WS	-2.89		Aq. Solubility Prediction
log10WS	-3.01		Estimated Solubility
logPoct/wat	2.291		Crippen Calculated Property
McVol	97.460	ml/mol	McGowan Calculated Property
Pc	[4519.10; 4520.00]	kPa
Pc	4519.10	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4519.10	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4520.00	kPa	KDB
Ptriple	1.18e-03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[1033.00; 1088.00]
Inp	1079.60		NIST
Inp	1088.00		NIST
Inp	1088.00		NIST
Inp	1075.00		NIST
Inp	1050.00		NIST
Inp	1033.00		NIST
Inp	1033.00		NIST
Inp	1033.00		NIST
Inp	1079.60		NIST
Inp	1033.00		NIST
Ip	[1569.00; 1569.00]
Ip	1569.00		NIST
Ip	1569.00		NIST
S°liquid	205.40	J/mol×K	NIST
Tboil	[460.85; 461.70]	K
Tboil	461.60	K	ChemSep v8.3 pure component data Compiled value
Tboil	461.60	K	KDB
Tboil	461.50	K	NIST
Tboil	461.60 ± 0.30	K	NIST
Tboil	461.70 ± 0.50	K	NIST
Tboil	461.70 ± 0.50	K	NIST
Tboil	461.15 ± 0.30	K	NIST
Tboil	Outlier 460.85 ± 0.50	K	NIST
Tc	[721.00; 721.15]	K
Tc	721.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	721.15	K	ChemSep v8.3 pure component data Compiled value
Tc	721.00	K	KDB
Tfus	[241.80; 242.15]	K
Tfus	242.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	241.83	K	ChemSep v8.3 pure component data Compiled value
Tfus	241.80	K	KDB
Tfus	242.05	K	Aq. Solubility Prediction
Tfus	242.15 ± 1.00	K	NIST
Tfus	241.90 ± 0.02	K	NIST
Tfus	241.80 ± 0.30	K	NIST
Ttriple	[241.80; 241.83]	K
Ttriple	241.83	K	ChemSep v8.3 pure component data Compiled value
Ttriple	241.80 ± 0.25	K	NIST
Ttriple	241.80 ± 0.25	K	NIST
UQi	3.11		ChemSep v8.3 pure component data Compiled value
URi	4.29		ChemSep v8.3 pure component data Compiled value
Vc	[0.351; 0.351]	m3/kmol
Vc	0.351	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.351	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.351	m3/kmol	KDB
Zc	[0.2646510; 0.2650000]
Zc	0.2650000		ChemSep v8.3 pure component data Compiled value
Zc	0.2646510		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[154.00; 164.00]	J/mol×K	[250.00; 320.00]
Cp,liquid	154.00	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	155.00	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	157.00	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	157.00	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	158.00	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	160.00	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	158.70	J/mol×K	298.10	NIST
Cp,liquid	161.00	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	158.40	J/mol×K	298.15	NIST
Cp,liquid	161.00	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	163.00	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	164.00	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,solid	112.10	J/mol×K	226.10	NIST
ΔfusH	[9.75; 9.75]	kJ/mol	[241.80; 241.83]
ΔfusH	9.75	kJ/mol	241.80	NIST
ΔfusH	9.75	kJ/mol	241.80	NIST
ΔfusH	9.75	kJ/mol	241.83	NIST
ΔfusH	9.75	kJ/mol	241.83	NIST
ΔvapH	[39.50; 51.40]	kJ/mol	[249.00; 570.50]
ΔvapH	43.10	kJ/mol	249.00	NIST
ΔvapH	40.00	kJ/mol	275.50	NIST
ΔvapH	51.40	kJ/mol	315.50	NIST
ΔvapH	46.00	kJ/mol	450.50	NIST
ΔvapH	39.50	kJ/mol	461.60	KDB
ΔvapH	41.10	kJ/mol	570.50	NIST
Pvap	[0.05; 0.39]	kPa	[283.80; 314.60]
Pvap	0.05	kPa	283.80	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.06	kPa	286.80	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.08	kPa	289.90	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.10	kPa	293.00	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.10	kPa	294.00	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.13	kPa	296.80	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.15	kPa	299.60	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.19	kPa	302.60	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.22	kPa	305.70	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.27	kPa	308.70	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.32	kPa	311.80	Thermochemistry of Halogen-Substituted Methylbenzenes
Pvap	0.39	kPa	314.60	Thermochemistry of Halogen-Substituted Methylbenzenes
ρl	1855.00	kg/m3	277.00	KDB
ΔfusS	[40.31; 40.31]	J/mol×K	[241.83; 241.83]
ΔfusS	40.31	J/mol×K	241.83	NIST
ΔfusS	40.31	J/mol×K	241.83	NIST
γ	0.04	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[76.13; 247.03]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			6.34420e+01
Coefficient B			-6.92720e+02
Coefficient C			6.09524e+00
Coefficient D			-4.82970e-04
Coefficient E			1.34990e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	76.13	J/mol×K	200.00	Calculated Property
Cp,gas	114.54	J/mol×K	344.44	Calculated Property
Cp,gas	151.19	J/mol×K	488.89	Calculated Property
Cp,gas	179.00	J/mol×K	633.33	Calculated Property
Cp,gas	199.17	J/mol×K	777.78	Calculated Property
Cp,gas	213.87	J/mol×K	922.22	Calculated Property
Cp,gas	224.90	J/mol×K	1066.67	Calculated Property
Cp,gas	233.54	J/mol×K	1211.11	Calculated Property
Cp,gas	240.69	J/mol×K	1355.56	Calculated Property
Cp,gas	247.03	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[155.15; 162.91]	J/mol×K	[250.00; 350.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.39830e+02
Coefficient B			5.78690e+02
Coefficient C			-5.26246e+00
Coefficient D			3.12780e-02
Coefficient E			-3.42790e-05
Temperature range, min.			250.00
Temperature range, max.			350.00
Cp,liquid	155.15	J/mol×K	250.00	Calculated Property
Cp,liquid	156.01	J/mol×K	261.11	Calculated Property
Cp,liquid	156.91	J/mol×K	272.22	Calculated Property
Cp,liquid	157.83	J/mol×K	283.33	Calculated Property
Cp,liquid	158.76	J/mol×K	294.44	Calculated Property
Cp,liquid	159.68	J/mol×K	305.56	Calculated Property
Cp,liquid	160.57	J/mol×K	316.67	Calculated Property
Cp,liquid	161.42	J/mol×K	327.78	Calculated Property
Cp,liquid	162.21	J/mol×K	338.89	Calculated Property
Cp,liquid	162.91	J/mol×K	350.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0051078; 0.0003470]	Pa×s	[241.83; 461.60]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-5.71770e+01
Coefficient B			3.15780e+03
Coefficient C			7.15290e+00
Coefficient D			-7.09130e-06
Coefficient E			2.00000e+00
Temperature range, min.			241.83
Temperature range, max.			461.60
η	0.0051078	Pa×s	241.83	Calculated Property
η	0.0028103	Pa×s	266.25	Calculated Property
η	0.0017649	Pa×s	290.67	Calculated Property
η	0.0012193	Pa×s	315.09	Calculated Property
η	0.0009030	Pa×s	339.51	Calculated Property
η	0.0007039	Pa×s	363.92	Calculated Property
η	0.0005698	Pa×s	388.34	Calculated Property
η	0.0004743	Pa×s	412.76	Calculated Property
η	0.0004028	Pa×s	437.18	Calculated Property
η	0.0003470	Pa×s	461.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[51.63; 0.00]	kJ/mol	[241.83; 721.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			6.14882e+01
Coefficient B			4.33906e-01
Coefficient C			-1.02943e-02
Coefficient D			-1.30647e-02
Coefficient E			-3.29532e-02
Critical temperature, Tc (K)			7.21150e+02
Temperature range, min.			241.83
Temperature range, max.			721.15
ΔvapH	51.63	kJ/mol	241.83	Calculated Property
ΔvapH	49.16	kJ/mol	295.09	Calculated Property
ΔvapH	46.54	kJ/mol	348.35	Calculated Property
ΔvapH	43.74	kJ/mol	401.60	Calculated Property
ΔvapH	40.71	kJ/mol	454.86	Calculated Property
ΔvapH	37.36	kJ/mol	508.12	Calculated Property
ΔvapH	33.53	kJ/mol	561.38	Calculated Property
ΔvapH	28.87	kJ/mol	614.63	Calculated Property
ΔvapH	22.43	kJ/mol	667.89	Calculated Property
ΔvapH	0.00	kJ/mol	721.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[336.11; 492.86]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43953e+01
Coefficient B			-3.99844e+03
Coefficient C			-5.26870e+01
Temperature range, min.			336.11
Temperature range, max.			492.86
Pvap	1.33	kPa	336.11	Calculated Property
Pvap	3.02	kPa	353.53	Calculated Property
Pvap	6.24	kPa	370.94	Calculated Property
Pvap	11.98	kPa	388.36	Calculated Property
Pvap	21.57	kPa	405.78	Calculated Property
Pvap	36.73	kPa	423.19	Calculated Property
Pvap	59.62	kPa	440.61	Calculated Property
Pvap	92.84	kPa	458.03	Calculated Property
Pvap	139.40	kPa	475.44	Calculated Property
Pvap	202.66	kPa	492.86	Calculated Property
Pvap	[1.22e-03; 4521.93]	kPa	[241.83; 721.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			7.22782e+01
Coefficient B			-8.18530e+03
Coefficient C			-8.26360e+00
Coefficient D			3.59630e-06
Coefficient E			2.00000e+00
Temperature range, min.			241.83
Temperature range, max.			721.15
Pvap	1.22e-03	kPa	241.83	Calculated Property
Pvap	0.12	kPa	295.09	Calculated Property
Pvap	2.34	kPa	348.35	Calculated Property
Pvap	18.78	kPa	401.60	Calculated Property
Pvap	85.97	kPa	454.86	Calculated Property
Pvap	273.03	kPa	508.12	Calculated Property
Pvap	677.90	kPa	561.38	Calculated Property
Pvap	1420.39	kPa	614.63	Calculated Property
Pvap	2642.71	kPa	667.89	Calculated Property
Pvap	4521.93	kPa	721.15	Calculated Property
Pvap	[1.16e-03; 4473.13]	kPa	[241.83; 721.15]	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			7.00267e+01
Coefficient B			-8.12638e+03
Coefficient C			-7.90248e+00
Coefficient D			3.17808e-06
Coefficient E			0.00000e+00
Temperature range, min.			241.83
Temperature range, max.			721.15
Pvap	1.16e-03	kPa	241.83	Calculated Property
Pvap	0.11	kPa	295.09	Calculated Property
Pvap	2.29	kPa	348.35	Calculated Property
Pvap	18.64	kPa	401.60	Calculated Property
Pvap	86.10	kPa	454.86	Calculated Property
Pvap	274.81	kPa	508.12	Calculated Property
Pvap	683.12	kPa	561.38	Calculated Property
Pvap	1427.65	kPa	614.63	Calculated Property
Pvap	2639.80	kPa	667.89	Calculated Property
Pvap	4473.13	kPa	721.15	Calculated Property
Pvap	[0.19; 102.18]	kPa	[302.40; 461.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46702e+01
Coefficient B			-4.15263e+03
Coefficient C			-4.79330e+01
Reference			Young, 1889
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			302.40
Temperature range, max.			461.40
Pvap	0.19	kPa	302.40	Calculated Property
Pvap	0.55	kPa	320.07	Calculated Property
Pvap	1.41	kPa	337.73	Calculated Property
Pvap	3.20	kPa	355.40	Calculated Property
Pvap	6.67	kPa	373.07	Calculated Property
Pvap	12.89	kPa	390.73	Calculated Property
Pvap	23.34	kPa	408.40	Calculated Property
Pvap	39.98	kPa	426.07	Calculated Property
Pvap	65.27	kPa	443.73	Calculated Property
Pvap	102.18	kPa	461.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1900.19; 581.61]	kg/m3	[241.83; 721.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			1.53435e+02
Coefficient B			2.63810e-01
Coefficient C			7.21150e+02
Coefficient D			2.89500e-01
Temperature range, min.			241.83
Temperature range, max.			721.15
ρl	1900.19	kg/m3	241.83	Calculated Property
ρl	1826.25	kg/m3	295.09	Calculated Property
ρl	1748.71	kg/m3	348.35	Calculated Property
ρl	1666.68	kg/m3	401.60	Calculated Property
ρl	1578.86	kg/m3	454.86	Calculated Property
ρl	1483.24	kg/m3	508.12	Calculated Property
ρl	1376.33	kg/m3	561.38	Calculated Property
ρl	1251.09	kg/m3	614.63	Calculated Property
ρl	1088.45	kg/m3	667.89	Calculated Property
ρl	581.61	kg/m3	721.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.02]	N/m	[242.15; 461.15]	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			7.21947e-02
Coefficient B			-1.12300e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			242.15
Temperature range, max.			461.15
γ	0.05	N/m	242.15	Calculated Property
γ	0.04	N/m	266.48	Calculated Property
γ	0.04	N/m	290.82	Calculated Property
γ	0.04	N/m	315.15	Calculated Property
γ	0.03	N/m	339.48	Calculated Property
γ	0.03	N/m	363.82	Calculated Property
γ	0.03	N/m	388.15	Calculated Property
γ	0.03	N/m	412.48	Calculated Property
γ	0.02	N/m	436.82	Calculated Property
γ	0.02	N/m	461.15	Calculated Property
γ	[0.05; 7.67e-06]	N/m	[241.83; 716.84]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-1.07720e-02
Coefficient B			6.58410e+01
Coefficient C			-3.14090e+00
Coefficient D			1.00090e-03
Coefficient E			-4.27850e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 721.15 K.
Temperature range, min.			241.83
Temperature range, max.			716.84
γ	0.05	N/m	241.83	Calculated Property
γ	0.04	N/m	294.61	Calculated Property
γ	0.03	N/m	347.39	Calculated Property
γ	0.03	N/m	400.17	Calculated Property
γ	0.02	N/m	452.94	Calculated Property
γ	0.02	N/m	505.72	Calculated Property
γ	0.01	N/m	558.50	Calculated Property
γ	0.01	N/m	611.28	Calculated Property
γ	0.00	N/m	664.06	Calculated Property
γ	7.67e-06	N/m	716.84	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.04]	W/m×K	[241.83; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			2.68780e-04
Coefficient B			7.89110e-01
Coefficient C			3.73970e+02
Coefficient D			1.87720e+05
Temperature range, min.			241.83
Temperature range, max.			1000.00
λgas	0.00	W/m×K	241.83	Calculated Property
λgas	0.01	W/m×K	326.07	Calculated Property
λgas	0.01	W/m×K	410.31	Calculated Property
λgas	0.01	W/m×K	494.55	Calculated Property
λgas	0.02	W/m×K	578.79	Calculated Property
λgas	0.02	W/m×K	663.04	Calculated Property
λgas	0.03	W/m×K	747.28	Calculated Property
λgas	0.03	W/m×K	831.52	Calculated Property
λgas	0.04	W/m×K	915.76	Calculated Property
λgas	0.04	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.11; 0.08]	W/m×K	[216.35; 461.60]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			7.79230e-02
Coefficient B			1.28480e+03
Coefficient C			-1.70820e+01
Coefficient D			5.03620e-02
Coefficient E			-6.77900e-05
Temperature range, min.			216.35
Temperature range, max.			461.60
λliquid	0.11	W/m×K	216.35	Calculated Property
λliquid	0.11	W/m×K	243.60	Calculated Property
λliquid	0.10	W/m×K	270.85	Calculated Property
λliquid	0.10	W/m×K	298.10	Calculated Property
λliquid	0.10	W/m×K	325.35	Calculated Property
λliquid	0.09	W/m×K	352.60	Calculated Property
λliquid	0.09	W/m×K	379.85	Calculated Property
λliquid	0.09	W/m×K	407.10	Calculated Property
λliquid	0.08	W/m×K	434.35	Calculated Property
λliquid	0.08	W/m×K	461.60	Calculated Property

Similar Compounds

Find more compounds similar to IODOBENZENE.

Mixtures

• IODOBENZENE + 1,2-Ethanediol
• IODOBENZENE + Carbon dioxide

Sources

• KDB Vapor Pressure Data
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• 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.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
• Phase behavior of ionic liquids 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imides with halogenated benzenes
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Solubilities of 4-Phenyltoluene, Phenylboric Acid, Biphenyl, and Iodobenzene in Carbon Dioxide from Measurements of the Relative Permittivity
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Thermochemistry of Halogen-Substituted Methylbenzenes
• Liquid-Liquid Equilibria in Binary Mixtures Containing Chlorobenzene, Bromobenzene, and Iodobenzene with Ionic Liquid 1-Ethyl-3-methylimidazolim Bis(trifluoromethylsulfonyl)imide
• 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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