Chemical Properties of Bibenzyl (CAS 103-29-7)

InChI

InChI=1S/C14H14/c1-3-7-13(8-4-1)11-12-14-9-5-2-6-10-14/h1-10H,11-12H2

InChI Key

QWUWMCYKGHVNAV-UHFFFAOYSA-N

Formula

C14H14

SMILES

c1ccc(CCc2ccccc2)cc1

Molecular Weight¹

182.26

CAS

103-29-7

Other Names

• 1,1'-(1,2-Ethanediyl)bisbenzene
• 1,2-Diphenylethane(sym)
• 1,2-Diphenylethane, s
• 1,2-diphenylethane
• 2-phenylethylbenzene
• Benzene, (phenylethyl)-
• Benzene, 1,1'-(1,2-ethanediyl)bis-
• Dibenzil
• Dihydrostilbene
• NSC 30686
• dibenzyl
• ethane, 1,2-diphenyl-
• s-Diphenylethane
• sym-Diphenylethane

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• 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_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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4492		Relay (1.0) Calculated Property
PAff	801.80	kJ/mol	NIST
BasG	774.10	kJ/mol	NIST
ΔcH°liquid	-7562.60 ± 7.50	kJ/mol	NIST
ΔcH°solid	[-7594.40; -7280.00]	kJ/mol
ΔcH°solid	-7561.50 ± 1.10	kJ/mol	NIST
ΔcH°solid	-7559.60 ± 1.00	kJ/mol	NIST
ΔcH°solid	-7280.00	kJ/mol	NIST
ΔcH°solid	-7594.40	kJ/mol	NIST
ΔcH°solid	-7554.80 ± 3.00	kJ/mol	NIST
ΔfG°	291.82	kJ/mol	Joback Calculated Property
ΔfH°gas	[129.00; 135.60]	kJ/mol
ΔfH°gas	135.60 ± 1.30	kJ/mol	NIST
ΔfH°gas	129.00	kJ/mol	NIST
ΔfH°solid	[44.90; 51.50]	kJ/mol
ΔfH°solid	51.50 ± 1.30	kJ/mol	NIST
ΔfH°solid	44.90 ± 3.10	kJ/mol	NIST
ΔfusH°	20.10	kJ/mol	Joback Calculated Property
ΔsubH°	[73.20; 91.50]	kJ/mol
ΔsubH°	91.50 ± 0.70	kJ/mol	NIST
ΔsubH°	91.38 ± 0.46	kJ/mol	NIST
ΔsubH°	91.40 ± 0.50	kJ/mol	NIST
ΔsubH°	84.10	kJ/mol	NIST
ΔsubH°	73.20 ± 0.80	kJ/mol	NIST
ΔvapH°	75.85	kJ/mol	Relay (1.0) Calculated Property
IE	[8.70; 9.10]	eV
IE	9.00 ± 0.05	eV	NIST
IE	8.70 ± 0.10	eV	NIST
IE	9.10	eV	NIST
log10WS	[-4.62; -4.62]
log10WS	-4.62		Aq. Solubility Prediction
log10WS	-4.62		Estimated Solubility
logPoct/wat	3.472		Crippen Calculated Property
McVol	160.600	ml/mol	McGowan Calculated Property
Pc	2770.08	kPa	Joback Calculated Property
Inp	[258.90; 1563.00]
Inp	1496.70		NIST
Inp	1509.30		NIST
Inp	1546.30		NIST
Inp	1539.00		NIST
Inp	1541.00		NIST
Inp	1563.00		NIST
Inp	1508.80		NIST
Inp	1519.20		NIST
Inp	1524.30		NIST
Inp	1508.80		NIST
Inp	1519.20		NIST
Inp	1524.30		NIST
Inp	1528.00		NIST
Inp	1525.00		NIST
Inp	1494.00		NIST
Inp	1516.00		NIST
Inp	1489.00		NIST
Inp	1487.00		NIST
Inp	260.40		NIST
Inp	260.13		NIST
Inp	260.49		NIST
Inp	258.90		NIST
Inp	260.10		NIST
Inp	260.10		NIST
Inp	1496.70		NIST
Inp	1563.00		NIST
Inp	1525.00		NIST
Inp	1508.80		NIST
Inp	1524.30		NIST
Inp	1516.00		NIST
Inp	258.90		NIST
I	[2061.00; 2072.00]
I	2069.00		NIST
I	2072.00		NIST
I	2070.00		NIST
I	2061.00		NIST
I	2061.00		NIST
I	2061.00		NIST
I	2069.00		NIST
S°solid,1 bar	[267.39; 270.30]	J/mol×K
S°solid,1 bar	267.39	J/mol×K	NIST
S°solid,1 bar	270.30	J/mol×K	NIST
Tboil	[548.00; 568.00]	K
Tboil	557.20	K	NIST
Tboil	560.00 ± 5.00	K	NIST
Tboil	553.70 ± 1.00	K	NIST
Tboil	557.00 ± 1.00	K	NIST
Tboil	558.00 ± 3.00	K	NIST
Tboil	557.00 ± 3.00	K	NIST
Tboil	551.00 ± 5.00	K	NIST
Tboil	558.10 ± 0.50	K	NIST
Tboil	557.00 ± 3.00	K	NIST
Tboil	559.50 ± 1.50	K	NIST
Tboil	557.00 ± 3.00	K	NIST
Tboil	557.00 ± 3.00	K	NIST
Tboil	556.00 ± 3.00	K	NIST
Tboil	557.00 ± 3.00	K	NIST
Tboil	557.00 ± 3.00	K	NIST
Tboil	Outlier 548.00 ± 8.00	K	NIST
Tboil	Outlier 568.00 ± 3.00	K	NIST
Tboil	554.65 ± 1.00	K	NIST
Tboil	557.00 ± 4.00	K	NIST
Tboil	557.00 ± 4.00	K	NIST
Tboil	557.00 ± 4.00	K	NIST
Tboil	551.00 ± 5.00	K	NIST
Tboil	557.00 ± 4.00	K	NIST
Tboil	557.00 ± 5.00	K	NIST
Tc	784.80	K	Relay (1.0) Calculated Property
Tfus	[320.00; 330.00]	K
Tfus	324.95	K	KDB
Tfus	325.77	K	Aq. Solubility Prediction
Tfus	325.00 ± 3.00	K	NIST
Tfus	326.00 ± 4.00	K	NIST
Tfus	Outlier 330.00 ± 2.00	K	NIST
Tfus	325.20 ± 3.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.70 ± 4.00	K	NIST
Tfus	326.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	Outlier 327.00 ± 0.60	K	NIST
Tfus	324.60 ± 2.00	K	NIST
Tfus	325.90 ± 1.00	K	NIST
Tfus	324.90 ± 1.50	K	NIST
Tfus	Outlier 327.30 ± 1.50	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.40 ± 0.60	K	NIST
Tfus	Outlier 326.90 ± 1.00	K	NIST
Tfus	324.70 ± 3.00	K	NIST
Tfus	323.00 ± 3.00	K	NIST
Tfus	324.60 ± 1.00	K	NIST
Tfus	324.00 ± 3.00	K	NIST
Tfus	324.90 ± 0.80	K	NIST
Tfus	324.40 ± 1.50	K	NIST
Tfus	324.70 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.70 ± 2.00	K	NIST
Tfus	324.70 ± 2.00	K	NIST
Tfus	324.31 ± 0.20	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	323.70 ± 3.00	K	NIST
Tfus	324.90 ± 1.50	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Tfus	324.70 ± 2.00	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Tfus	325.95 ± 0.50	K	NIST
Tfus	324.00 ± 2.00	K	NIST
Tfus	324.70 ± 2.00	K	NIST
Tfus	Outlier 322.65 ± 1.00	K	NIST
Tfus	Outlier 322.70 ± 3.00	K	NIST
Tfus	325.70 ± 1.50	K	NIST
Tfus	325.90 ± 1.00	K	NIST
Tfus	324.90 ± 1.00	K	NIST
Tfus	324.00 ± 2.00	K	NIST
Tfus	325.00 ± 1.50	K	NIST
Tfus	324.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.40 ± 0.30	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.00 ± 2.00	K	NIST
Tfus	323.70 ± 3.00	K	NIST
Tfus	324.35 ± 0.40	K	NIST
Tfus	324.40 ± 0.60	K	NIST
Tfus	323.70 ± 3.00	K	NIST
Tfus	Outlier 320.00 ± 2.00	K	NIST
Tfus	Outlier 320.00 ± 5.00	K	NIST
Tfus	324.80 ± 3.00	K	NIST
Tfus	324.90 ± 2.00	K	NIST
Tfus	326.00 ± 2.00	K	NIST
Tfus	326.00 ± 1.50	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.40 ± 0.10	K	NIST
Tfus	325.15 ± 0.20	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.70 ± 2.00	K	NIST
Tfus	326.00 ± 1.50	K	NIST
Tfus	326.00 ± 1.50	K	NIST
Tfus	324.70 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.00 ± 1.50	K	NIST
Tfus	326.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	323.70 ± 2.00	K	NIST
Tfus	325.70 ± 2.00	K	NIST
Tfus	325.00 ± 1.50	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.70 ± 1.50	K	NIST
Tfus	324.70 ± 1.50	K	NIST
Tfus	326.00 ± 2.00	K	NIST
Tfus	324.40 ± 0.20	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	326.00 ± 1.50	K	NIST
Tfus	325.70 ± 1.50	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.50 ± 0.70	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.90 ± 1.50	K	NIST
Tfus	324.40 ± 0.40	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.00 ± 2.00	K	NIST
Tfus	324.00 ± 2.00	K	NIST
Tfus	326.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.70 ± 2.00	K	NIST
Tfus	326.80 ± 1.50	K	NIST
Tfus	324.00 ± 3.00	K	NIST
Tfus	325.00 ± 0.10	K	NIST
Tfus	324.45 ± 0.30	K	NIST
Tfus	323.95 ± 0.20	K	NIST
Tfus	323.70 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.00 ± 1.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	326.00 ± 3.00	K	NIST
Tfus	324.00 ± 3.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.90 ± 1.50	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 1.50	K	NIST
Tfus	324.70 ± 3.00	K	NIST
Tfus	323.70 ± 3.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.65 ± 1.00	K	NIST
Tfus	326.60 ± 1.50	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	323.00 ± 3.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.00 ± 3.00	K	NIST
Tfus	324.00 ± 3.00	K	NIST
Tfus	324.00 ± 3.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.70 ± 3.00	K	NIST
Tfus	324.70 ± 3.00	K	NIST
Tfus	324.00 ± 3.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.50 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.70 ± 2.00	K	NIST
Tfus	325.00 ± 1.50	K	NIST
Tfus	324.00 ± 2.00	K	NIST
Tfus	325.70 ± 1.50	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.70 ± 1.50	K	NIST
Tfus	324.00 ± 2.00	K	NIST
Tfus	324.00 ± 1.00	K	NIST
Tfus	324.40 ± 1.50	K	NIST
Tfus	325.36 ± 1.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.00 ± 3.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.90 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.00 ± 3.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.90 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.15 ± 2.00	K	NIST
Tfus	324.70 ± 3.00	K	NIST
Tfus	325.00 ± 1.50	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	324.00 ± 3.00	K	NIST
Tfus	326.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 1.00	K	NIST
Tfus	324.90 ± 2.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	326.00 ± 3.00	K	NIST
Tfus	324.55 ± 0.60	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	326.00 ± 3.00	K	NIST
Tfus	326.00 ± 3.00	K	NIST
Tfus	325.40 ± 1.50	K	NIST
Tfus	324.70 ± 1.50	K	NIST
Tfus	326.20 ± 3.00	K	NIST
Tfus	325.50 ± 1.00	K	NIST
Tfus	325.00 ± 2.00	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Tfus	325.90 ± 2.00	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Tfus	323.00 ± 3.00	K	NIST
Tfus	324.00 ± 3.10	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Tfus	323.00 ± 3.00	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Tfus	325.00 ± 3.00	K	NIST
Ttriple	[324.34; 324.34]	K
Ttriple	324.34 ± 0.01	K	NIST
Ttriple	324.34 ± 0.01	K	NIST
Vc	0.616	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[372.43; 460.43]	J/mol×K	[573.28; 812.95]
Cp,gas	372.43	J/mol×K	573.28	Joback Calculated Property
Cp,gas	390.19	J/mol×K	613.23	Joback Calculated Property
Cp,gas	406.61	J/mol×K	653.17	Joback Calculated Property
Cp,gas	421.76	J/mol×K	693.12	Joback Calculated Property
Cp,gas	435.73	J/mol×K	733.06	Joback Calculated Property
Cp,gas	448.59	J/mol×K	773.01	Joback Calculated Property
Cp,gas	460.43	J/mol×K	812.95	Joback Calculated Property
Cp,liquid	[315.40; 385.50]	J/mol×K	[330.00; 470.00]
Cp,liquid	315.40	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	321.40	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	327.30	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	333.00	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	338.50	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	343.90	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	349.20	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	354.30	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	359.20	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	364.00	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	368.60	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	373.10	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	377.40	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	381.50	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	385.50	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,solid	[251.00; 320.10]	J/mol×K	[293.60; 330.00]
Cp,solid	251.00	J/mol×K	293.60	NIST
Cp,solid	251.90	J/mol×K	298.10	NIST
Cp,solid	253.76	J/mol×K	298.15	NIST
Cp,solid	253.60	J/mol×K	298.50	NIST
Cp,solid	257.00	J/mol×K	303.00	NIST
Cp,solid	320.10	J/mol×K	330.00	NIST
η	[0.0001781; 0.0026164]	Pa×s	[300.38; 573.28]
η	0.0026164	Pa×s	300.38	Joback Calculated Property
η	0.0012455	Pa×s	345.86	Joback Calculated Property
η	0.0007045	Pa×s	391.35	Joback Calculated Property
η	0.0004487	Pa×s	436.83	Joback Calculated Property
η	0.0003112	Pa×s	482.31	Joback Calculated Property
η	0.0002299	Pa×s	527.80	Joback Calculated Property
η	0.0001781	Pa×s	573.28	Joback Calculated Property
ΔfusH	[2.25; 23.01]	kJ/mol	[273.20; 324.40]
ΔfusH	2.25	kJ/mol	273.20	NIST
ΔfusH	22.73	kJ/mol	324.30	NIST
ΔfusH	22.57	kJ/mol	324.30	NIST
ΔfusH	22.73	kJ/mol	324.30	NIST
ΔfusH	23.01	kJ/mol	324.40	NIST
ΔsubH	[72.40; 92.90]	kJ/mol	[295.50; 326.20]
ΔsubH	91.20 ± 0.40	kJ/mol	295.50	NIST
ΔsubH	84.10 ± 0.40	kJ/mol	296.50	NIST
ΔsubH	84.10 ± 0.40	kJ/mol	296.50	NIST
ΔsubH	72.40 ± 1.30	kJ/mol	303.50	NIST
ΔsubH	92.90	kJ/mol	308.00	NIST
ΔsubH	83.97 ± 0.46	kJ/mol	326.20	NIST
ΔvapH	[57.00; 67.53]	kJ/mol	[324.40; 458.00]
ΔvapH	67.53 ± 0.10	kJ/mol	324.40	NIST
ΔvapH	67.53 ± 0.10	kJ/mol	324.40	NIST
ΔvapH	66.20 ± 0.20	kJ/mol	340.00	NIST
ΔvapH	66.20 ± 0.20	kJ/mol	340.00	NIST
ΔvapH	64.10	kJ/mol	373.00	NIST
ΔvapH	67.40	kJ/mol	398.00	NIST
ΔvapH	57.00	kJ/mol	458.00	NIST
ΔfusS	[8.23; 70.90]	J/mol×K	[273.20; 324.40]
ΔfusS	8.23	J/mol×K	273.20	NIST
ΔfusS	70.09	J/mol×K	324.30	NIST
ΔfusS	70.90	J/mol×K	324.40	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[410.70; 591.81]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.46161e+01
Coefficient B			-4.80619e+03
Coefficient C			-7.52760e+01
Temperature range, min.			410.70
Temperature range, max.			591.81
Pvap	1.33	kPa	410.70	Calculated Property
Pvap	3.00	kPa	430.82	Calculated Property
Pvap	6.19	kPa	450.95	Calculated Property
Pvap	11.86	kPa	471.07	Calculated Property
Pvap	21.34	kPa	491.19	Calculated Property
Pvap	36.37	kPa	511.32	Calculated Property
Pvap	59.15	kPa	531.44	Calculated Property
Pvap	92.32	kPa	551.56	Calculated Property
Pvap	138.97	kPa	571.69	Calculated Property
Pvap	202.65	kPa	591.81	Calculated Property
Pvap	[9.53e-03; 2719.16]	kPa	[324.34; 780.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.13283e+02
Coefficient B			-1.22009e+04
Coefficient C			-1.39952e+01
Coefficient D			5.69580e-06
Temperature range, min.			324.34
Temperature range, max.			780.00
Pvap	9.53e-03	kPa	324.34	Calculated Property
Pvap	0.25	kPa	374.97	Calculated Property
Pvap	2.53	kPa	425.60	Calculated Property
Pvap	14.32	kPa	476.23	Calculated Property
Pvap	54.56	kPa	526.86	Calculated Property
Pvap	158.20	kPa	577.48	Calculated Property
Pvap	379.31	kPa	628.11	Calculated Property
Pvap	795.72	kPa	678.74	Calculated Property
Pvap	1519.68	kPa	729.37	Calculated Property
Pvap	2719.16	kPa	780.00	Calculated Property

Similar Compounds

Find more compounds similar to Bibenzyl.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Modified solution calorimetry approach for determination of vaporization and sublimation enthalpies of branched-chain aliphatic and alkyl aromatic compounds at T = 298.15 K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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