Chemical Properties of Benzene, 1,1'-tetradecylidenebis- (CAS 55268-63-8)

InChI

InChI=1S/C26H38/c1-2-3-4-5-6-7-8-9-10-11-18-23-26(24-19-14-12-15-20-24)25-21-16-13-17-22-25/h12-17,19-22,26H,2-11,18,23H2,1H3

InChI Key

RHISRDQWNQEBBY-UHFFFAOYSA-N

Formula

C26H38

SMILES

CCCCCCCCCCCCCC(c1ccccc1)c1ccccc1

Molecular Weight¹

350.58

CAS

55268-63-8

Other Names

• 1,1-Diphenyltetradecane

• ω : Acentric Factor.
• C_p,gas : Ideal gas 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_fusH° : Enthalpy of fusion at standard conditions (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).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.8943		Relay (1.0) Calculated Property
ΔfG°	390.42	kJ/mol	Joback Calculated Property
ΔfH°gas	-89.51	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	47.65	kJ/mol	Joback Calculated Property
ΔvapH°	115.16	kJ/mol	Relay (1.0) Calculated Property
IE	8.83	eV	Relay (1.0) Calculated Property
log10WS	-8.59		Relay (1.0) Calculated Property
logPoct/wat	8.520		Crippen Calculated Property
McVol	329.680	ml/mol	McGowan Calculated Property
Pc	1079.22	kPa	Joback Calculated Property
Tboil	661.84	K	Relay (1.0) Calculated Property
Tc	890.07	K	Relay (1.0) Calculated Property
Tfus	[291.10; 291.10]	K
Tfus	291.10 ± 1.00	K	NIST
Tfus	291.10 ± 0.60	K	NIST
Vc	1.238	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[442.21; 1124.18]	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			-9.02380e+01
Coefficient B			2.32192e+00
Coefficient C			-1.45620e-03
Coefficient D			3.48700e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	442.21	J/mol×K	273.00	Calculated Property
Cp,gas	564.39	J/mol×K	353.78	Calculated Property
Cp,gas	672.39	J/mol×K	434.56	Calculated Property
Cp,gas	767.33	J/mol×K	515.33	Calculated Property
Cp,gas	850.29	J/mol×K	596.11	Calculated Property
Cp,gas	922.39	J/mol×K	676.89	Calculated Property
Cp,gas	984.72	J/mol×K	757.67	Calculated Property
Cp,gas	1038.40	J/mol×K	838.44	Calculated Property
Cp,gas	1084.52	J/mol×K	919.22	Calculated Property
Cp,gas	1124.18	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0267190; 0.0000692]	Pa×s	[291.10; 738.09]	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			-1.34584e+01
Coefficient B			2.86326e+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.			291.10
Temperature range, max.			738.09
η	0.0267190	Pa×s	291.10	Calculated Property
η	0.0063714	Pa×s	340.77	Calculated Property
η	0.0021880	Pa×s	390.43	Calculated Property
η	0.0009564	Pa×s	440.10	Calculated Property
η	0.0004944	Pa×s	489.76	Calculated Property
η	0.0002886	Pa×s	539.43	Calculated Property
η	0.0001845	Pa×s	589.09	Calculated Property
η	0.0001264	Pa×s	638.76	Calculated Property
η	0.0000915	Pa×s	688.42	Calculated Property
η	0.0000692	Pa×s	738.09	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[509.82; 767.11]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.27452e+01
Coefficient B			-4.74261e+03
Coefficient C			-1.29120e+02
Temperature range, min.			509.82
Temperature range, max.			767.11
Pvap	1.33	kPa	509.82	Calculated Property
Pvap	3.18	kPa	538.41	Calculated Property
Pvap	6.78	kPa	567.00	Calculated Property
Pvap	13.17	kPa	595.58	Calculated Property
Pvap	23.69	kPa	624.17	Calculated Property
Pvap	39.97	kPa	652.76	Calculated Property
Pvap	63.88	kPa	681.35	Calculated Property
Pvap	97.49	kPa	709.93	Calculated Property
Pvap	142.99	kPa	738.52	Calculated Property
Pvap	202.66	kPa	767.11	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, 1,1'-tetradecylidenebis-.

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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