Chemical Properties of Benzene, hexachloro- (CAS 118-74-1)

InChI

InChI=1S/C6Cl6/c7-1-2(8)4(10)6(12)5(11)3(1)9

InChI Key

CKAPSXZOOQJIBF-UHFFFAOYSA-N

Formula

C6Cl6

SMILES

Clc1c(Cl)c(Cl)c(Cl)c(Cl)c1Cl

Molecular Weight¹

284.78

CAS

118-74-1

Other Names

• 1,2,3,4,5,6-Hexachlorobenzene
• Amatin
• Anticarie
• Benzene, 1,2,3,4,5,6-hexachloro-
• Bunt-cure
• Bunt-no-more
• Ceku C.B.
• Co-op Hexa
• Esaclorobenzene
• Granox nm
• HCB
• Hexa C.B.
• Hexachlorbenzol
• Hexcachlorbenzen
• Julin's carbon chloride
• Julin's chloride
• NSC 9243
• No Bunt
• No Bunt 40
• No Bunt 80
• No Bunt Liquid
• PENTACHLOROPHENYLCHLORIDE
• Phenyl perchloryl
• Rcra waste number U127
• Saatbeizfungizid
• Sanocid
• Sanocide
• Smut-Go
• Snieciotox
• UN 2729
• hexachlorobenzene
• pentachlorophenyl chloride
• perchlorobenzene

• ω : Acentric Factor.
• Δ_cH°_solid : Standard solid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• EA : Electron affinity (eV).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_solid : Solid 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_subH° : Enthalpy of sublimation at standard conditions (kJ/mol).
• Δ_subH : Enthalpy of sublimation 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_sub : Sublimation pressure (kPa).
• P_vap : Vapor pressure (kPa).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• 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).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.5430		KDB
ΔcH°solid	[-2375.30; -2361.09]	kJ/mol
ΔcH°solid	-2361.09	kJ/mol	NIST
ΔcH°solid	-2375.30 ± 4.20	kJ/mol	NIST
EA	[0.92; 1.00]	eV
EA	0.92 ± 0.10	eV	NIST
EA	1.00	eV	NIST
ΔfH°gas	-44.70	kJ/mol	NIST
ΔfH°solid	[-141.77; -127.60]	kJ/mol
ΔfH°solid	-141.77	kJ/mol	NIST
ΔfH°solid	-127.60 ± 4.20	kJ/mol	NIST
ΔfusH°	23.92	kJ/mol	Johari-Goldstein relaxation in orientationally disordered phase of hexa-substituted benzenes
ΔsubH°	[90.50; 96.80]	kJ/mol
ΔsubH°	96.80 ± 0.50	kJ/mol	NIST
ΔsubH°	90.50 ± 0.20	kJ/mol	NIST
ΔvapH°	[74.40; 76.80]	kJ/mol
ΔvapH°	74.40 ± 0.70	kJ/mol	NIST
ΔvapH°	76.80	kJ/mol	NIST
IE	[8.98; 9.35]	eV
IE	9.00 ± 0.10	eV	NIST
IE	8.98	eV	NIST
IE	9.00 ± 0.10	eV	NIST
IE	9.19 ± 0.03	eV	NIST
IE	9.35	eV	NIST
IE	9.31 ± 0.05	eV	NIST
IE	9.20	eV	NIST
log10WS	-7.62		Aq. Solubility Prediction
logPoct/wat	5.607		Crippen Calculated Property
McVol	145.080	ml/mol	McGowan Calculated Property
Pc	3230.00	kPa	KDB
Inp	[287.10; 1739.00]
Inp	1678.00		NIST
Inp	1678.00		NIST
Inp	1700.10		NIST
Inp	1656.00		NIST
Inp	1695.00		NIST
Inp	1656.00		NIST
Inp	1673.00		NIST
Inp	1695.00		NIST
Inp	1724.00		NIST
Inp	1700.00		NIST
Inp	1688.00		NIST
Inp	1691.00		NIST
Inp	1691.00		NIST
Inp	1693.00		NIST
Inp	1688.00		NIST
Inp	1690.00		NIST
Inp	1691.00		NIST
Inp	1693.00		NIST
Inp	1662.00		NIST
Inp	1739.00		NIST
Inp	1661.00		NIST
Inp	1699.00		NIST
Inp	1717.00		NIST
Inp	1716.00		NIST
Inp	1725.00		NIST
Inp	1728.00		NIST
Inp	1734.00		NIST
Inp	1734.00		NIST
Inp	1688.00		NIST
Inp	1680.00		NIST
Inp	1680.00		NIST
Inp	Outlier 291.00		NIST
Inp	Outlier 289.80		NIST
Inp	Outlier 288.81		NIST
Inp	Outlier 287.10		NIST
Inp	1700.00		NIST
Inp	1688.00		NIST
Inp	1717.00		NIST
Inp	1734.00		NIST
I	[2153.00; 2204.00]
I	2153.00		NIST
I	2202.30		NIST
I	2178.00		NIST
I	2204.00		NIST
I	2193.00		NIST
I	2193.00		NIST
I	2193.00		NIST
I	2153.00		NIST
S°solid,1 bar	260.24	J/mol×K	NIST
Tboil	[582.60; 597.70]	K
Tboil	582.60	K	KDB
Tboil	597.70	K	NIST
Tc	825.80	K	KDB
Tfus	[500.00; 505.00]	K
Tfus	503.00	K	KDB
Tfus	503.12	K	Aq. Solubility Prediction
Tfus	501.27 ± 0.20	K	NIST
Tfus	501.10 ± 0.20	K	NIST
Tfus	505.00 ± 0.10	K	NIST
Tfus	502.80 ± 0.50	K	NIST
Tfus	500.00 ± 2.50	K	NIST
Ttriple	502.02 ± 0.01	K	NIST
Vc	0.557	m3/kmol	KDB
Zc	0.2622620		KDB

Cheméo can also estimate Standard Gibbs free energy of formation for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[216.40; 237.95]	J/mol×K	[612.84; 868.72]
Cp,gas	216.40	J/mol×K	612.84	Joback Calculated Property
Cp,gas	220.80	J/mol×K	655.49	Joback Calculated Property
Cp,gas	224.86	J/mol×K	698.13	Joback Calculated Property
Cp,gas	228.60	J/mol×K	740.78	Joback Calculated Property
Cp,gas	232.03	J/mol×K	783.43	Joback Calculated Property
Cp,gas	235.14	J/mol×K	826.07	Joback Calculated Property
Cp,gas	237.95	J/mol×K	868.72	Joback Calculated Property
Cp,solid	[201.29; 257.70]	J/mol×K	[298.15; 299.80]
Cp,solid	201.29	J/mol×K	298.15	NIST
Cp,solid	257.70	J/mol×K	299.80	NIST
η	[0.0002692; 0.0008967]	Pa×s	[425.92; 612.84]
η	0.0008967	Pa×s	425.92	Joback Calculated Property
η	0.0006852	Pa×s	457.07	Joback Calculated Property
η	0.0005419	Pa×s	488.23	Joback Calculated Property
η	0.0004409	Pa×s	519.38	Joback Calculated Property
η	0.0003671	Pa×s	550.53	Joback Calculated Property
η	0.0003117	Pa×s	581.69	Joback Calculated Property
η	0.0002692	Pa×s	612.84	Joback Calculated Property
ΔfusH	[23.85; 25.20]	kJ/mol	[501.87; 505.00]
ΔfusH	24.96	kJ/mol	501.87	NIST
ΔfusH	25.20	kJ/mol	502.00	NIST
ΔfusH	25.18	kJ/mol	502.02	NIST
ΔfusH	23.85	kJ/mol	505.00	NIST
ΔfusH	23.85	kJ/mol	505.00	NIST
ΔsubH	[62.70; 105.00]	kJ/mol	[278.00; 483.50]
ΔsubH	77.40 ± 0.80	kJ/mol	278.00	NIST
ΔsubH	105.00	kJ/mol	285.50	NIST
ΔsubH	101.30	kJ/mol	303.00	NIST
ΔsubH	79.50 ± 1.20	kJ/mol	324.50	NIST
ΔsubH	89.60 ± 0.20	kJ/mol	337.00	NIST
ΔsubH	94.70	kJ/mol	343.50	NIST
ΔsubH	92.00 ± 8.20	kJ/mol	383.00	NIST
ΔsubH	92.00 ± 8.20	kJ/mol	383.00	NIST
ΔsubH	62.70	kJ/mol	444.50	NIST
ΔsubH	85.50	kJ/mol	483.50	NIST
ΔvapH	[60.50; 94.30]	kJ/mol	[285.50; 582.60]
ΔvapH	81.30	kJ/mol	285.50	NIST
ΔvapH	94.30	kJ/mol	298.15	Enthalpies of Vaporization and Sublimation of the Halogen-Substituted Aromatic Hydrocarbons at 298.15 K: Application of Solution Calorimetry Approach
ΔvapH	68.60	kJ/mol	398.00	NIST
ΔvapH	60.50	kJ/mol	484.50	NIST
ΔvapH	68.70	kJ/mol	545.50	NIST
ΔvapH	63.59	kJ/mol	582.60	KDB
Psub	[1.44e-03; 0.17]	kPa	[358.00; 425.70]
Psub	1.44e-03	kPa	358.00	Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
Psub	2.16e-03	kPa	362.90	Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
Psub	3.73e-03	kPa	368.90	Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
Psub	5.19e-03	kPa	373.10	Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
Psub	7.71e-03	kPa	377.80	Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
Psub	0.01	kPa	382.90	Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
Psub	0.02	kPa	389.00	Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
Psub	0.02	kPa	392.80	Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
Psub	0.04	kPa	397.50	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.03	kPa	397.90	Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
Psub	0.05	kPa	400.40	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.04	kPa	400.80	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.05	kPa	401.20	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.05	kPa	402.00	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.06	kPa	402.80	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.05	kPa	402.80	Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
Psub	0.05	kPa	403.60	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.06	kPa	404.10	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.05	kPa	404.50	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.06	kPa	404.90	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.05	kPa	405.30	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.06	kPa	405.80	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.05	kPa	406.10	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.06	kPa	406.50	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.06	kPa	407.00	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.06	kPa	407.40	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.06	kPa	407.80	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.07	kPa	408.20	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.07	kPa	408.60	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.08	kPa	409.00	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.07	kPa	409.40	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.08	kPa	409.80	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.08	kPa	410.20	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.07	kPa	410.60	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.07	kPa	411.00	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.09	kPa	411.40	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.07	kPa	411.90	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.08	kPa	412.30	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.08	kPa	412.70	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.08	kPa	413.20	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.09	kPa	413.60	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.09	kPa	414.00	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.09	kPa	414.40	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.09	kPa	414.90	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.09	kPa	415.30	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.10	kPa	415.70	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.09	kPa	416.10	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.10	kPa	416.50	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.10	kPa	417.00	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.11	kPa	417.40	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.12	kPa	417.80	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.11	kPa	418.20	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.11	kPa	418.60	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.13	kPa	419.10	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.13	kPa	419.50	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.12	kPa	419.90	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.13	kPa	420.30	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.13	kPa	420.70	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.13	kPa	421.10	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.13	kPa	421.50	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.14	kPa	421.90	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.14	kPa	422.30	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.14	kPa	422.80	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.16	kPa	423.20	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.15	kPa	423.60	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.15	kPa	424.00	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.15	kPa	424.40	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.17	kPa	424.80	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
Psub	0.17	kPa	425.70	Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
ΔfusS	50.20	J/mol×K	502.02	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[448.33; 639.86]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.18922e+01
Coefficient B			-2.91145e+03
Coefficient C			-1.97439e+02
Temperature range, min.			448.33
Temperature range, max.			639.86
Pvap	1.33	kPa	448.33	Calculated Property
Pvap	3.30	kPa	469.61	Calculated Property
Pvap	7.18	kPa	490.89	Calculated Property
Pvap	14.04	kPa	512.17	Calculated Property
Pvap	25.22	kPa	533.45	Calculated Property
Pvap	42.25	kPa	554.74	Calculated Property
Pvap	66.80	kPa	576.02	Calculated Property
Pvap	100.58	kPa	597.30	Calculated Property
Pvap	145.32	kPa	618.58	Calculated Property
Pvap	202.65	kPa	639.86	Calculated Property
Pvap	[0.13; 2564.05]	kPa	[387.15; 825.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			-1.10122e+02
Coefficient B			-1.18239e+03
Coefficient C			1.89428e+01
Coefficient D			-1.14651e-05
Temperature range, min.			387.15
Temperature range, max.			825.00
Pvap	0.13	kPa	387.15	Calculated Property
Pvap	1.11	kPa	435.80	Calculated Property
Pvap	6.49	kPa	484.45	Calculated Property
Pvap	28.16	kPa	533.10	Calculated Property
Pvap	95.18	kPa	581.75	Calculated Property
Pvap	259.28	kPa	630.40	Calculated Property
Pvap	584.14	kPa	679.05	Calculated Property
Pvap	1110.56	kPa	727.70	Calculated Property
Pvap	1810.55	kPa	776.35	Calculated Property
Pvap	2564.05	kPa	825.00	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, hexachloro-.

Mixtures

• pentachlorophenol + Benzene, hexachloro-
• Benzene, hexachloro- + Carbon Tetrachloride
• Benzene, hexachloro- + Water
• sodium chloride + Benzene, hexachloro- + Water
• potassium chloride + Benzene, hexachloro- + Water

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Vapor Pressures and Standard Molar Enthalpies, Entropies and Gibbs energies of Sublimation of two hexachloro herbicides using a TG unit
• Johari-Goldstein relaxation in orientationally disordered phase of hexa-substituted benzenes
• The Effects of Temperature and Inorganic Salts on the Aqueous Solubility of Selected Chlorobenzenes
• Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
• Determination of Henry's Law Constant Using Diffusion in Air and Water Boundary Layers
• Enthalpies of Vaporization and Sublimation of the Halogen-Substituted Aromatic Hydrocarbons at 298.15 K: Application of Solution Calorimetry Approach
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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