Chemical Properties of Benzene, 1,2,4-trichloro- (CAS 120-82-1)

InChI

InChI=1S/C6H3Cl3/c7-4-1-2-5(8)6(9)3-4/h1-3H

InChI Key

PBKONEOXTCPAFI-UHFFFAOYSA-N

Formula

C6H3Cl3

SMILES

Clc1ccc(Cl)c(Cl)c1

Molecular Weight¹

181.45

CAS

120-82-1

Other Names

• 1,2,4-Trichlorobenzol
• 1,2,4-trichlorobenzene
• 1,2,5-Trichlorobenzene
• 1,3,4-Trichlorobenzene
• AS-TRICHLOROBENZENE
• Hipochem GM
• Hostetex L-PEC
• NSC 406697
• Trojchlorobenzen
• unsym-trichlorobenzene

• 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).
• 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_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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• 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	0.3581		ChemSep v8.3 pure component data Compiled value
ΔcH°liquid	[-2810.50; -2797.98]	kJ/mol
ΔcH°liquid	-2810.50 ± 1.50	kJ/mol	NIST
ΔcH°liquid	-2797.98 ± 0.44	kJ/mol	NIST
μ	1.26	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	43.05	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-11.76; 4.90]	kJ/mol
ΔfH°gas	-11.76	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	4.90 ± 1.60	kJ/mol	NIST
ΔfH°gas	-8.05	kJ/mol	NIST
ΔfH°liquid	-50.20 ± 1.50	kJ/mol	NIST
ΔfusH°	17.15	kJ/mol	Joback Calculated Property
ΔvapH°	[54.68; 57.60]	kJ/mol
ΔvapH°	Outlier 57.60	kJ/mol	NIST
ΔvapH°	55.50 ± 0.10	kJ/mol	NIST
ΔvapH°	55.10 ± 0.50	kJ/mol	NIST
ΔvapH°	54.68	kJ/mol	NIST
ΔvapH°	55.50 ± 0.10	kJ/mol	NIST
ΔvapH°	55.10 ± 0.50	kJ/mol	NIST
IE	9.04 ± 0.03	eV	NIST
log10WS	[-3.60; -3.59]
log10WS	-3.60		Aq. Solubility Prediction
log10WS	-3.59		Estimated Solubility
logPoct/wat	3.647		Crippen Calculated Property
McVol	108.360	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
NFPA Health	2		KDB
NFPA Safety	3		KDB
Pc	3720.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	0.03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[198.20; 1211.10]
Inp	1193.56		NIST
Inp	1193.67		NIST
Inp	1193.00		NIST
Inp	1189.60		NIST
Inp	1199.70		NIST
Inp	1211.10		NIST
Inp	1189.56		NIST
Inp	1164.56		NIST
Inp	1176.18		NIST
Inp	1177.00		NIST
Inp	1193.00		NIST
Inp	1177.00		NIST
Inp	1183.00		NIST
Inp	1193.00		NIST
Inp	1186.00		NIST
Inp	1177.00		NIST
Inp	1161.00		NIST
Inp	1166.00		NIST
Inp	1192.67		NIST
Inp	1193.06		NIST
Inp	1196.72		NIST
Inp	1196.78		NIST
Inp	1141.60		NIST
Inp	1158.50		NIST
Inp	1160.14		NIST
Inp	1166.23		NIST
Inp	1171.69		NIST
Inp	1168.00		NIST
Inp	1162.00		NIST
Inp	1157.00		NIST
Inp	1150.00		NIST
Inp	1152.00		NIST
Inp	1172.00		NIST
Inp	1160.00		NIST
Inp	1198.00		NIST
Inp	1142.00		NIST
Inp	1144.00		NIST
Inp	1145.00		NIST
Inp	1149.00		NIST
Inp	1170.00		NIST
Inp	1177.00		NIST
Inp	1174.00		NIST
Inp	1158.00		NIST
Inp	1145.00		NIST
Inp	1150.00		NIST
Inp	1150.00		NIST
Inp	1154.00		NIST
Inp	Outlier 199.00		NIST
Inp	Outlier 198.20		NIST
Inp	1142.00		NIST
Ip	[1630.00; 1698.00]
Ip	1665.50		NIST
Ip	1688.60		NIST
Ip	1630.00		NIST
Ip	1630.00		NIST
Ip	1653.00		NIST
Ip	1698.00		NIST
Ip	1671.43		NIST
Ip	1659.76		NIST
Ip	1658.54		NIST
Ip	1643.59		NIST
Tboil	[486.15; 486.70]	K
Tboil	486.15	K	ChemSep v8.3 pure component data Compiled value
Tboil	486.70	K	NIST
Tc	725.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	[282.20; 290.15]	K
Tfus	290.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	290.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	290.10 ± 0.02	K	NIST
Tfus	282.20 ± 4.00	K	NIST
Tfus	289.70 ± 3.00	K	NIST
Ttriple	290.15	K	ChemSep v8.3 pure component data Compiled value
UQi	3.73		ChemSep v8.3 pure component data Compiled value
URi	5.06		ChemSep v8.3 pure component data Compiled value
Vc	0.395	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2440000		ChemSep v8.3 pure component data Compiled value
Zra	0.26		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[188.00; 227.00]	J/mol×K	[290.00; 460.00]
Cp,liquid	191.00	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	194.25	J/mol×K	293.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	194.57	J/mol×K	295.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	194.90	J/mol×K	297.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	188.00	J/mol×K	297.95	NIST
Cp,liquid	194.90	J/mol×K	298.15	NIST
Cp,liquid	193.00	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	194.60	J/mol×K	298.15	NIST
Cp,liquid	195.23	J/mol×K	299.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	193.00	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	195.57	J/mol×K	301.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	195.92	J/mol×K	303.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	196.27	J/mol×K	305.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	196.63	J/mol×K	307.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	196.99	J/mol×K	309.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	195.00	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	197.35	J/mol×K	311.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	197.72	J/mol×K	313.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	198.09	J/mol×K	315.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	198.47	J/mol×K	317.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	198.85	J/mol×K	319.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	197.00	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	199.23	J/mol×K	321.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	199.61	J/mol×K	323.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	200.00	J/mol×K	325.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	200.38	J/mol×K	327.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	200.77	J/mol×K	329.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	199.00	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	201.16	J/mol×K	331.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	201.55	J/mol×K	333.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	201.93	J/mol×K	335.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	202.32	J/mol×K	337.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	202.71	J/mol×K	339.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	201.00	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	203.09	J/mol×K	341.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	203.47	J/mol×K	343.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	203.85	J/mol×K	345.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	204.23	J/mol×K	347.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	204.61	J/mol×K	349.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	204.00	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	204.98	J/mol×K	351.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	205.35	J/mol×K	353.15	Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
Cp,liquid	206.00	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
Cp,liquid	208.00	J/mol×K	370.00	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	210.00	J/mol×K	380.00	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	212.00	J/mol×K	390.00	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	214.00	J/mol×K	400.00	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	216.00	J/mol×K	410.00	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	219.00	J/mol×K	420.00	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	221.00	J/mol×K	430.00	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	223.00	J/mol×K	440.00	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	225.00	J/mol×K	450.00	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	227.00	J/mol×K	460.00	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
ΔsubH	62.30	kJ/mol	288.50	NIST
ΔvapH	[47.00; 55.80]	kJ/mol	[288.50; 440.50]
ΔvapH	47.00	kJ/mol	288.50	NIST
ΔvapH	55.80	kJ/mol	290.00	NIST
ΔvapH	49.30	kJ/mol	398.50	NIST
ΔvapH	49.50	kJ/mol	440.50	NIST
n0	[1.52200; 1.54800]		[298.15; 308.15]
n0	1.54800		298.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Octanol with Chlorobenzenes
n0	1.52200		298.15	Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
n0	1.54600		303.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Octanol with Chlorobenzenes
n0	1.54300		308.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Octanol with Chlorobenzenes
ρl	1442.12	kg/m3	303.15	Effect of various substituents on benzene ring and their impact on volumetric, acoustic and transport properties of binary liquid mixtures with dimethylacetamide

Datasets

Viscosity, Pa*s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.00	303.15	0.0016
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[96.56; 256.84]	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			6.31300e+01
Coefficient B			-4.26630e+02
Coefficient C			5.66124e+00
Coefficient D			-9.56960e-05
Coefficient E			1.47130e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	96.56	J/mol×K	200.00	Calculated Property
Cp,gas	143.89	J/mol×K	344.44	Calculated Property
Cp,gas	178.18	J/mol×K	488.89	Calculated Property
Cp,gas	201.91	J/mol×K	633.33	Calculated Property
Cp,gas	218.71	J/mol×K	777.78	Calculated Property
Cp,gas	230.95	J/mol×K	922.22	Calculated Property
Cp,gas	240.09	J/mol×K	1066.67	Calculated Property
Cp,gas	247.08	J/mol×K	1211.11	Calculated Property
Cp,gas	252.52	J/mol×K	1355.56	Calculated Property
Cp,gas	256.84	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[189.91; 228.43]	J/mol×K	[290.15; 486.15]	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			1.45370e+02
Coefficient B			2.34690e+02
Coefficient C			-6.28855e-01
Coefficient D			1.70120e-02
Coefficient E			-1.56750e-05
Temperature range, min.			290.15
Temperature range, max.			486.15
Cp,liquid	189.91	J/mol×K	290.15	Calculated Property
Cp,liquid	195.01	J/mol×K	311.93	Calculated Property
Cp,liquid	200.29	J/mol×K	333.71	Calculated Property
Cp,liquid	205.59	J/mol×K	355.48	Calculated Property
Cp,liquid	210.75	J/mol×K	377.26	Calculated Property
Cp,liquid	215.60	J/mol×K	399.04	Calculated Property
Cp,liquid	219.96	J/mol×K	420.82	Calculated Property
Cp,liquid	223.65	J/mol×K	442.59	Calculated Property
Cp,liquid	226.52	J/mol×K	464.37	Calculated Property
Cp,liquid	228.43	J/mol×K	486.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0032927; 0.0000408]	Pa×s	[273.15; 580.00]	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			-2.41000e+02
Coefficient B			9.89320e+03
Coefficient C			3.61150e+01
Coefficient D			-4.74580e-05
Coefficient E			2.00000e+00
Temperature range, min.			273.15
Temperature range, max.			580.00
η	0.0032927	Pa×s	273.15	Calculated Property
η	0.0016183	Pa×s	307.24	Calculated Property
η	0.0010163	Pa×s	341.34	Calculated Property
η	0.0007136	Pa×s	375.43	Calculated Property
η	0.0005158	Pa×s	409.53	Calculated Property
η	0.0003638	Pa×s	443.62	Calculated Property
η	0.0002419	Pa×s	477.72	Calculated Property
η	0.0001480	Pa×s	511.81	Calculated Property
η	0.0000821	Pa×s	545.91	Calculated Property
η	0.0000408	Pa×s	580.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[56.14; 0.00]	kJ/mol	[290.15; 725.00]	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			6.89700e+01
Coefficient B			4.02600e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.25000e+02
Temperature range, min.			290.15
Temperature range, max.			725.00
ΔvapH	56.14	kJ/mol	290.15	Calculated Property
ΔvapH	53.54	kJ/mol	338.47	Calculated Property
ΔvapH	50.74	kJ/mol	386.78	Calculated Property
ΔvapH	47.69	kJ/mol	435.10	Calculated Property
ΔvapH	44.31	kJ/mol	483.42	Calculated Property
ΔvapH	40.50	kJ/mol	531.73	Calculated Property
ΔvapH	36.07	kJ/mol	580.05	Calculated Property
ΔvapH	30.64	kJ/mol	628.37	Calculated Property
ΔvapH	23.18	kJ/mol	676.68	Calculated Property
ΔvapH	0.00	kJ/mol	725.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[353.84; 519.04]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.49608e+01
Coefficient B			-4.65563e+03
Coefficient C			-3.65540e+01
Temperature range, min.			353.84
Temperature range, max.			519.04
Pvap	1.33	kPa	353.84	Calculated Property
Pvap	2.97	kPa	372.20	Calculated Property
Pvap	6.11	kPa	390.55	Calculated Property
Pvap	11.68	kPa	408.91	Calculated Property
Pvap	21.01	kPa	427.26	Calculated Property
Pvap	35.86	kPa	445.62	Calculated Property
Pvap	58.46	kPa	463.97	Calculated Property
Pvap	91.55	kPa	482.33	Calculated Property
Pvap	138.37	kPa	500.68	Calculated Property
Pvap	202.67	kPa	519.04	Calculated Property
Pvap	[0.03; 1666.03]	kPa	[290.15; 725.00]	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			4.02963e+01
Coefficient B			-7.46065e+03
Coefficient C			-3.16487e+00
Coefficient D			-3.31643e-06
Coefficient E			2.00000e+00
Temperature range, min.			290.15
Temperature range, max.			725.00
Pvap	0.03	kPa	290.15	Calculated Property
Pvap	0.57	kPa	338.47	Calculated Property
Pvap	5.23	kPa	386.78	Calculated Property
Pvap	26.93	kPa	435.10	Calculated Property
Pvap	92.43	kPa	483.42	Calculated Property
Pvap	236.19	kPa	531.73	Calculated Property
Pvap	482.98	kPa	580.05	Calculated Property
Pvap	830.57	kPa	628.37	Calculated Property
Pvap	1244.28	kPa	676.68	Calculated Property
Pvap	1666.03	kPa	725.00	Calculated Property
Pvap	[0.03; 3719.15]	kPa	[290.15; 725.00]	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			3.43692e+01
Coefficient B			-6.72270e+03
Coefficient C			-2.58415e+00
Coefficient D			2.74692e-07
Coefficient E			0.00000e+00
Temperature range, min.			290.15
Temperature range, max.			725.00
Pvap	0.03	kPa	290.15	Calculated Property
Pvap	0.60	kPa	338.47	Calculated Property
Pvap	5.12	kPa	386.78	Calculated Property
Pvap	26.31	kPa	435.10	Calculated Property
Pvap	95.05	kPa	483.42	Calculated Property
Pvap	266.50	kPa	531.73	Calculated Property
Pvap	619.26	kPa	580.05	Calculated Property
Pvap	1247.60	kPa	628.37	Calculated Property
Pvap	2250.21	kPa	676.68	Calculated Property
Pvap	3719.15	kPa	725.00	Calculated Property
Pvap	[0.13; 100.77]	kPa	[311.60; 486.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.52892e+01
Coefficient B			-4.86072e+03
Coefficient C			-3.07210e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			311.60
Temperature range, max.			486.00
Pvap	0.13	kPa	311.60	Calculated Property
Pvap	0.41	kPa	330.98	Calculated Property
Pvap	1.09	kPa	350.36	Calculated Property
Pvap	2.59	kPa	369.73	Calculated Property
Pvap	5.62	kPa	389.11	Calculated Property
Pvap	11.27	kPa	408.49	Calculated Property
Pvap	21.12	kPa	427.87	Calculated Property
Pvap	37.32	kPa	447.24	Calculated Property
Pvap	62.69	kPa	466.62	Calculated Property
Pvap	100.77	kPa	486.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1457.82; 443.65]	kg/m3	[290.15; 725.00]	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			1.11976e+02
Coefficient B			2.52400e-01
Coefficient C			7.25000e+02
Coefficient D			2.85700e-01
Temperature range, min.			290.15
Temperature range, max.			725.00
ρl	1457.82	kg/m3	290.15	Calculated Property
ρl	1401.55	kg/m3	338.47	Calculated Property
ρl	1342.48	kg/m3	386.78	Calculated Property
ρl	1279.94	kg/m3	435.10	Calculated Property
ρl	1212.93	kg/m3	483.42	Calculated Property
ρl	1139.87	kg/m3	531.73	Calculated Property
ρl	1058.08	kg/m3	580.05	Calculated Property
ρl	962.12	kg/m3	628.37	Calculated Property
ρl	837.20	kg/m3	676.68	Calculated Property
ρl	443.65	kg/m3	725.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 2.34e-05]	N/m	[290.15; 720.22]	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			-9.90860e-03
Coefficient B			2.12190e+02
Coefficient C			-4.13940e+00
Coefficient D			3.73520e-03
Coefficient E			-6.66530e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 725 K.
Temperature range, min.			290.15
Temperature range, max.			720.22
γ	0.05	N/m	290.15	Calculated Property
γ	0.04	N/m	337.94	Calculated Property
γ	0.03	N/m	385.72	Calculated Property
γ	0.03	N/m	433.51	Calculated Property
γ	0.02	N/m	481.29	Calculated Property
γ	0.02	N/m	529.08	Calculated Property
γ	0.01	N/m	576.86	Calculated Property
γ	0.01	N/m	624.65	Calculated Property
γ	0.00	N/m	672.43	Calculated Property
γ	2.34e-05	N/m	720.22	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.06]	W/m×K	[290.15; 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			-7.43070e+02
Coefficient B			7.41590e-01
Coefficient C			-2.17460e+09
Coefficient D			-6.45020e+10
Temperature range, min.			290.15
Temperature range, max.			1000.00
λgas	0.01	W/m×K	290.15	Calculated Property
λgas	0.01	W/m×K	369.02	Calculated Property
λgas	0.01	W/m×K	447.89	Calculated Property
λgas	0.02	W/m×K	526.77	Calculated Property
λgas	0.02	W/m×K	605.64	Calculated Property
λgas	0.03	W/m×K	684.51	Calculated Property
λgas	0.03	W/m×K	763.38	Calculated Property
λgas	0.04	W/m×K	842.26	Calculated Property
λgas	0.05	W/m×K	921.13	Calculated Property
λgas	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.11; 0.09]	W/m×K	[285.15; 486.15]	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			7.01050e-02
Coefficient B			-2.90720e+02
Coefficient C			-2.03660e-01
Coefficient D			-7.44150e-03
Coefficient E			2.47790e-06
Temperature range, min.			285.15
Temperature range, max.			486.15
λliquid	0.11	W/m×K	285.15	Calculated Property
λliquid	0.11	W/m×K	307.48	Calculated Property
λliquid	0.11	W/m×K	329.82	Calculated Property
λliquid	0.11	W/m×K	352.15	Calculated Property
λliquid	0.10	W/m×K	374.48	Calculated Property
λliquid	0.10	W/m×K	396.82	Calculated Property
λliquid	0.10	W/m×K	419.15	Calculated Property
λliquid	0.10	W/m×K	441.48	Calculated Property
λliquid	0.09	W/m×K	463.82	Calculated Property
λliquid	0.09	W/m×K	486.15	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, 1,2,4-trichloro-.

Mixtures

• Benzene, 1,2,4-trichloro- + Dimethyl Sulfoxide
• Benzene, 1,2,4-trichloro- + N,N-Dimethylacetamide
• Benzene, 1,2,4-trichloro- + Tetrahydrofuran
• n-Hexane + Benzene, 1,2,4-trichloro- + Furfural
• Benzene, 1,2,4-trichloro- + Furfural + Hexadecane
• Benzene, 1,2,4-trichloro- + Water
• Benzene, 1,2,4-trichloro- + 2-Octanol

Sources

• KDB Vapor Pressure Data
• 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).
• 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
• Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Octanol with Chlorobenzenes
• Densities and ultrasonic studies for binary mixtures of tetrahydrofuran with chlorobenzenes, chlorotoluenes and nitrotoluenes at 298.15 K
• Effect of various substituents on benzene ring and their impact on volumetric, acoustic and transport properties of binary liquid mixtures with dimethylacetamide
• Volumetric, ultrasonic and viscometric studies of binary mixtures of dimethyl sulphoxide with chloro and nitro substituted aromatic hydrocarbons at T = 303.15 K
• Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
• Mutual Solubilities for Water-o-Nitrotoluene System and Distribution Coefficients for Furfural and Acetic Acid in Water-o-Nitrotoluene System
• Determination of Henry's Law Constant Using Diffusion in Air and Water Boundary Layers
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Heat Capacities and Densities of Some Liquid Chloro-, Bromo-, and Bromochloro-Substituted Benzenes
• 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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