Chemical Properties of 1,1':3',1''-Terphenyl, 5'-phenyl- (CAS 612-71-5)

InChI

InChI=1S/C24H18/c1-4-10-19(11-5-1)22-16-23(20-12-6-2-7-13-20)18-24(17-22)21-14-8-3-9-15-21/h1-18H

InChI Key

SXWIAEOZZQADEY-UHFFFAOYSA-N

Formula

C24H18

SMILES

c1ccc(-c2cc(-c3ccccc3)cc(-c3ccccc3)c2)cc1

Molecular Weight¹

306.40

CAS

612-71-5

Other Names

• 1,1'-Biphenyl, 3,5-diphenyl-
• 1,3,5-triphenylbenzene
• 5'-Phenyl-1,1':3',1''-terphenyl
• 5'-Phenyl-m-terphenyl
• NSC 17358
• Symmetrical triphenylbenzene
• Triphenylbenzene
• benzene, 1,3,5-triphenyl-
• m-Terphenyl, 5'-phenyl-
• s-Triphenylbenzene

• 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,liquid : Liquid phase heat capacity (J/mol×K).
• C_p,solid : Solid 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°_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.
• 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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.5523		Relay (1.0) Calculated Property
ΔcH°solid	-12241.30 ± 5.30	kJ/mol	NIST
ΔfG°	581.58	kJ/mol	Joback Calculated Property
ΔfH°gas	371.80 ± 3.80	kJ/mol	NIST
ΔfH°solid	[222.00; 224.60]	kJ/mol
ΔfH°solid	222.00 ± 3.40	kJ/mol	NIST
ΔfH°solid	224.60 ± 5.40	kJ/mol	NIST
ΔfusH°	[31.10; 149.50]	kJ/mol
ΔfusH°	147.70	kJ/mol	New Knudsen effusion apparatus with simultaneous gravimetric and quartz crystal microbalance mass loss detection
ΔfusH°	147.90	kJ/mol	New Knudsen effusion apparatus with simultaneous gravimetric and quartz crystal microbalance mass loss detection
ΔfusH°	148.40	kJ/mol	New Knudsen effusion apparatus with simultaneous gravimetric and quartz crystal microbalance mass loss detection
ΔfusH°	149.50	kJ/mol	New Knudsen effusion apparatus with simultaneous gravimetric and quartz crystal microbalance mass loss detection
ΔfusH°	31.10	kJ/mol	Vapor Pressures and Vaporization Enthalpies of the n-Alkanes from C31 to C38 at T = 298.15 K by Correlation Gas Chromatography
ΔsubH°	[142.00; 152.00]	kJ/mol
ΔsubH°	149.80 ± 1.60	kJ/mol	NIST
ΔsubH°	147.80 ± 0.70	kJ/mol	NIST
ΔsubH°	150.90	kJ/mol	NIST
ΔsubH°	150.30 ± 0.90	kJ/mol	NIST
ΔsubH°	152.00 ± 0.30	kJ/mol	NIST
ΔsubH°	Outlier 142.00	kJ/mol	NIST
ΔsubH°	149.70 ± 4.10	kJ/mol	NIST
ΔvapH°	[133.40; 140.00]	kJ/mol
ΔvapH°	133.40 ± 2.00	kJ/mol	NIST
ΔvapH°	140.00	kJ/mol	NIST
IE	7.79	eV	Relay (1.0) Calculated Property
log10WS	-8.87		Relay (1.0) Calculated Property
logPoct/wat	6.688		Crippen Calculated Property
McVol	253.980	ml/mol	McGowan Calculated Property
Pc	2014.51	kPa	Joback Calculated Property
Inp	[469.48; 2891.00]
Inp	2891.00		NIST
Inp	469.48		NIST
Inp	2891.00		NIST
S°solid,1 bar	[367.40; 375.50]	J/mol×K
S°solid,1 bar	375.50	J/mol×K	NIST
S°solid,1 bar	367.40	J/mol×K	NIST
Tboil	733.20	K	NIST
Tc	1017.05	K	Relay (1.0) Calculated Property
Tfus	[444.00; 450.10]	K
Tfus	450.10 ± 4.00	K	NIST
Tfus	448.00 ± 0.30	K	NIST
Tfus	444.00 ± 1.50	K	NIST
Tfus	446.00 ± 3.00	K	NIST
Tfus	444.00 ± 1.50	K	NIST
Ttriple	[446.00; 446.00]	K
Ttriple	446.00 ± 1.00	K	NIST
Ttriple	446.00 ± 1.00	K	NIST
Vc	0.938	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[620.00; 653.00]	J/mol×K	[450.00; 480.00]
Cp,liquid	620.00	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	631.00	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
Cp,liquid	642.00	J/mol×K	470.00	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	653.00	J/mol×K	480.00	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	[357.96; 361.00]	J/mol×K	[298.10; 298.15]
Cp,solid	358.32	J/mol×K	298.10	NIST
Cp,solid	357.96	J/mol×K	298.15	Reassembling and testing of a high-precision heat capacity drop calorimeter. Heat capacity of some polyphenyls at T = 298.15 K
Cp,solid	361.00	J/mol×K	298.15	NIST
ΔfusH	[32.60; 33.40]	kJ/mol	[445.20; 446.00]
ΔfusH	32.60	kJ/mol	445.20	NIST
ΔfusH	33.40	kJ/mol	446.00	NIST
ΔfusH	33.40	kJ/mol	446.00	NIST
ΔfusH	33.40	kJ/mol	446.00	NIST
ΔfusH	33.40	kJ/mol	446.00	NIST
ΔfusH	33.40	kJ/mol	446.00	NIST
ΔfusH	33.40	kJ/mol	446.00	NIST
ΔsubH	[141.20; 164.40]	kJ/mol	[363.00; 427.00]
ΔsubH	164.40 ± 4.20	kJ/mol	363.00	NIST
ΔsubH	145.60 ± 0.90	kJ/mol	376.00	NIST
ΔsubH	142.20	kJ/mol	392.00	NIST
ΔsubH	141.20 ± 0.70	kJ/mol	418.00	NIST
ΔsubH	142.00	kJ/mol	427.00	NIST
ΔvapH	[77.50; 118.00]	kJ/mol	[477.00; 617.50]
ΔvapH	118.00	kJ/mol	477.00	NIST
ΔvapH	77.50	kJ/mol	617.50	NIST
Psub	[1.39e-04; 1.20e-03]	kPa	[407.36; 429.29]
Psub	1.40e-04	kPa	407.36	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.41e-04	kPa	407.36	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.39e-04	kPa	407.36	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.44e-04	kPa	408.04	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	1.49e-04	kPa	408.05	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	1.54e-04	kPa	408.16	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	1.66e-04	kPa	409.30	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.64e-04	kPa	409.30	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.73e-04	kPa	409.30	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.10e-04	kPa	411.30	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.06e-04	kPa	411.30	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.15e-04	kPa	411.30	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.38e-04	kPa	413.04	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	2.47e-04	kPa	413.05	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	2.53e-04	kPa	413.16	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	2.56e-04	kPa	413.23	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.51e-04	kPa	413.23	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	2.51e-04	kPa	413.23	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.17e-04	kPa	415.35	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.16e-04	kPa	415.35	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.16e-04	kPa	415.35	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.61e-04	kPa	416.86	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.48e-04	kPa	416.86	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.70e-04	kPa	417.22	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.71e-04	kPa	417.22	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	3.88e-04	kPa	418.03	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	4.03e-04	kPa	418.05	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	4.16e-04	kPa	418.15	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	4.70e-04	kPa	419.24	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	4.54e-04	kPa	419.24	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	5.63e-04	kPa	421.36	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	5.42e-04	kPa	421.36	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	5.68e-04	kPa	421.36	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	6.22e-04	kPa	423.03	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	6.34e-04	kPa	423.03	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	6.48e-04	kPa	423.04	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	6.72e-04	kPa	423.16	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	6.72e-04	kPa	423.29	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	6.68e-04	kPa	423.29	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	6.49e-04	kPa	423.29	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	7.84e-04	kPa	425.26	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	7.96e-04	kPa	425.26	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	9.84e-04	kPa	427.36	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	9.66e-04	kPa	427.36	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.00e-03	kPa	427.36	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	9.83e-04	kPa	428.03	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	1.03e-03	kPa	428.04	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	1.08e-03	kPa	428.16	Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
Psub	1.20e-03	kPa	429.29	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.17e-03	kPa	429.29	The design, construction, and testing of a new Knudsen effusion apparatus
Psub	1.20e-03	kPa	429.29	The design, construction, and testing of a new Knudsen effusion apparatus
Pvap	[5.47e-10; 0.19]	kPa	[298.15; 510.00]
Pvap	5.47e-10	kPa	298.15	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	7.65e-10	kPa	300.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	4.30e-09	kPa	310.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	2.12e-08	kPa	320.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	9.25e-08	kPa	330.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	3.62e-07	kPa	340.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	1.28e-06	kPa	350.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	4.16e-06	kPa	360.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	1.24e-05	kPa	370.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	3.44e-05	kPa	380.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	8.89e-05	kPa	390.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	2.16e-04	kPa	400.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	4.94e-04	kPa	410.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	1.07e-03	kPa	420.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	2.22e-03	kPa	430.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	4.39e-03	kPa	440.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	8.31e-03	kPa	450.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.02	kPa	460.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.03	kPa	470.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.05	kPa	480.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.08	kPa	490.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.12	kPa	500.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
Pvap	0.19	kPa	510.00	Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
ΔfusS	[75.10; 75.10]	J/mol×K	[446.00; 446.00]
ΔfusS	75.10	J/mol×K	446.00	NIST
ΔfusS	75.10	J/mol×K	446.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[290.69; 777.33]	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			-1.25950e+02
Coefficient B			1.84920e+00
Coefficient C			-1.27252e-03
Coefficient D			3.26600e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	290.69	J/mol×K	273.00	Calculated Property
Cp,gas	383.45	J/mol×K	353.78	Calculated Property
Cp,gas	464.13	J/mol×K	434.56	Calculated Property
Cp,gas	533.76	J/mol×K	515.33	Calculated Property
Cp,gas	593.37	J/mol×K	596.11	Calculated Property
Cp,gas	644.00	J/mol×K	676.89	Calculated Property
Cp,gas	686.68	J/mol×K	757.67	Calculated Property
Cp,gas	722.44	J/mol×K	838.44	Calculated Property
Cp,gas	752.31	J/mol×K	919.22	Calculated Property
Cp,gas	777.33	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0010986; 0.0000827]	Pa×s	[446.42; 802.62]	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			-1.26411e+01
Coefficient B			2.60144e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			446.42
Temperature range, max.			802.62
η	0.0010986	Pa×s	446.42	Calculated Property
η	0.0006835	Pa×s	486.00	Calculated Property
η	0.0004567	Pa×s	525.58	Calculated Property
η	0.0003230	Pa×s	565.15	Calculated Property
η	0.0002389	Pa×s	604.73	Calculated Property
η	0.0001835	Pa×s	644.31	Calculated Property
η	0.0001452	Pa×s	683.89	Calculated Property
η	0.0001179	Pa×s	723.46	Calculated Property
η	0.0000979	Pa×s	763.04	Calculated Property
η	0.0000827	Pa×s	802.62	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[6.76e-03; 0.12]	kPa	[453.99; 499.99]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			6.45707e+00
Coefficient B			-1.57576e+03
Coefficient C			-3.16422e+02
Reference			Malaspina, Bardi, et al., 1974
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			453.99
Temperature range, max.			499.99
Pvap	6.76e-03	kPa	453.99	Calculated Property
Pvap	0.01	kPa	459.10	Calculated Property
Pvap	0.01	kPa	464.21	Calculated Property
Pvap	0.02	kPa	469.32	Calculated Property
Pvap	0.03	kPa	474.43	Calculated Property
Pvap	0.04	kPa	479.55	Calculated Property
Pvap	0.05	kPa	484.66	Calculated Property
Pvap	0.07	kPa	489.77	Calculated Property
Pvap	0.09	kPa	494.88	Calculated Property
Pvap	0.12	kPa	499.99	Calculated Property

Similar Compounds

Find more compounds similar to 1,1':3',1''-Terphenyl, 5'-phenyl-.

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• The design, construction, and testing of a new Knudsen effusion apparatus
• Thermodynamic study of 1,2,3-triphenylbenzene and 1,3,5-triphenylbenzene
• New Knudsen effusion apparatus with simultaneous gravimetric and quartz crystal microbalance mass loss detection
• Reassembling and testing of a high-precision heat capacity drop calorimeter. Heat capacity of some polyphenyls at T = 298.15 K
• Development of the Knudsen effusion methodology for vapour pressure measurements of low volatile liquids and solids based on a quartz crystal microbalance
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Vapor Pressures and Vaporization Enthalpies of the n-Alkanes from C31 to C38 at T = 298.15 K by Correlation Gas Chromatography
• Hypothetical Thermodynamic Properties. Subcooled Vaporization Enthalpies and Vapor Pressures of Polyaromatic Hydrocarbons
• Joback Method
• McGowan Method
• NIST Webbook
• 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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