Chemical Properties of Benzene, 1,1',1'',1'''-(1,6-hexanediylidene)tetrakis- (CAS 2819-41-2)

InChI

InChI=1S/C30H30/c1-5-15-25(16-6-1)29(26-17-7-2-8-18-26)23-13-14-24-30(27-19-9-3-10-20-27)28-21-11-4-12-22-28/h1-12,15-22,29-30H,13-14,23-24H2

InChI Key

WUHPEKSUKIJIJF-UHFFFAOYSA-N

Formula

C30H30

SMILES

c1ccc(C(CCCCC(c2ccccc2)c2ccccc2)c2ccccc2)cc1

Molecular Weight¹

390.56

CAS

2819-41-2

Other Names

• 1,1,6,6-Tetraphenylhexane
• Hexane, 1,1,6,6-tetraphenyl-

• 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	0.7097		Relay (1.0) Calculated Property
ΔfG°	646.48	kJ/mol	Joback Calculated Property
ΔfH°gas	301.61	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	42.57	kJ/mol	Joback Calculated Property
ΔvapH°	142.43	kJ/mol	Relay (1.0) Calculated Property
IE	8.30	eV	Relay (1.0) Calculated Property
log10WS	-8.84		Relay (1.0) Calculated Property
logPoct/wat	8.211		Crippen Calculated Property
McVol	338.520	ml/mol	McGowan Calculated Property
Pc	1314.65	kPa	Joback Calculated Property
Tboil	732.14	K	Relay (1.0) Calculated Property
Tc	1049.97	K	Relay (1.0) Calculated Property
Tfus	[397.65; 397.70]	K
Tfus	397.65 ± 0.50	K	NIST
Tfus	397.70 ± 2.00	K	NIST
Vc	1.222	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[412.24; 1094.03]	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			-1.63366e+02
Coefficient B			2.55000e+00
Coefficient C			-1.73940e-03
Coefficient D			4.46800e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	412.24	J/mol×K	273.00	Calculated Property
Cp,gas	540.85	J/mol×K	353.78	Calculated Property
Cp,gas	652.95	J/mol×K	434.56	Calculated Property
Cp,gas	749.95	J/mol×K	515.33	Calculated Property
Cp,gas	833.27	J/mol×K	596.11	Calculated Property
Cp,gas	904.31	J/mol×K	676.89	Calculated Property
Cp,gas	964.50	J/mol×K	757.67	Calculated Property
Cp,gas	1015.24	J/mol×K	838.44	Calculated Property
Cp,gas	1057.95	J/mol×K	919.22	Calculated Property
Cp,gas	1094.03	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0035596; 0.0000362]	Pa×s	[397.67; 875.05]	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			-1.40484e+01
Coefficient B			3.34456e+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.			397.67
Temperature range, max.			875.05
η	0.0035596	Pa×s	397.67	Calculated Property
η	0.0013230	Pa×s	450.72	Calculated Property
η	0.0006057	Pa×s	503.76	Calculated Property
η	0.0003218	Pa×s	556.80	Calculated Property
η	0.0001908	Pa×s	609.84	Calculated Property
η	0.0001231	Pa×s	662.88	Calculated Property
η	0.0000847	Pa×s	715.92	Calculated Property
η	0.0000613	Pa×s	768.97	Calculated Property
η	0.0000463	Pa×s	822.01	Calculated Property
η	0.0000362	Pa×s	875.05	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[579.14; 754.19]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			2.16429e+01
Coefficient B			-1.21519e+04
Coefficient C			-1.01080e+01
Temperature range, min.			579.14
Temperature range, max.			754.19
Pvap	1.33	kPa	579.14	Calculated Property
Pvap	2.70	kPa	598.59	Calculated Property
Pvap	5.23	kPa	618.04	Calculated Property
Pvap	9.71	kPa	637.49	Calculated Property
Pvap	17.39	kPa	656.94	Calculated Property
Pvap	30.10	kPa	676.39	Calculated Property
Pvap	50.49	kPa	695.84	Calculated Property
Pvap	82.31	kPa	715.29	Calculated Property
Pvap	130.72	kPa	734.74	Calculated Property
Pvap	202.64	kPa	754.19	Calculated Property

Similar Compounds

Find more compounds similar to Benzene, 1,1',1'',1'''-(1,6-hexanediylidene)tetrakis-.

Sources

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

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
These property values are available through the Cheméo API. A free account gives you an access key.