Chemical Properties of Cyclohexane, (1,1-dimethylethyl)- (CAS 3178-22-1)

InChI

InChI=1S/C10H20/c1-10(2,3)9-7-5-4-6-8-9/h9H,4-8H2,1-3H3

InChI Key

XTVMZZBLCLWBPM-UHFFFAOYSA-N

Formula

C10H20

SMILES

CC(C)(C)C1CCCCC1

Molecular Weight¹

140.27

CAS

3178-22-1

Other Names

• (1,1-Dimethylethyl)cyclohexane
• 1,1-dimethylethylcyclohexane
• 1-tert-Butylcyclohexane
• 2-cyclohexyl-2-methylpropane
• Cyclohexane, t-butyl-
• cyclohexane, tert-butyl-
• t-Butylcyclohexane
• tert-butylcyclohexane

• ω : Acentric Factor.
• 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_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).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• 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	[0.2520; 0.2991]
ω	0.2520		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2991		ChemSep v8.3 pure component data Compiled value
ω	0.2520		KDB
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
ΔfG°	56.95	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-216.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	6.08	kJ/mol	Joback Calculated Property
ΔvapH°	46.98	kJ/mol	NIST
IE	9.40	eV	Relay (1.0) Calculated Property
logPoct/wat	3.613		Crippen Calculated Property
McVol	140.900	ml/mol	McGowan Calculated Property
Pc	[2660.00; 2669.65]	kPa
Pc	2669.65	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2660.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2660.00	kPa	KDB
Ptriple	1.20e-03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[978.10; 1027.10]
Inp	1014.10		NIST
Inp	1027.10		NIST
Inp	1003.00		NIST
Inp	1012.00		NIST
Inp	1021.00		NIST
Inp	1025.00		NIST
Inp	1005.00		NIST
Inp	984.00		NIST
Inp	988.00		NIST
Inp	978.10		NIST
Inp	982.20		NIST
Inp	985.20		NIST
Inp	983.10		NIST
Inp	1014.00		NIST
Inp	1000.00		NIST
Inp	1014.10		NIST
Inp	1025.00		NIST
Inp	1014.00		NIST
Ip	[1062.00; 1088.00]
Ip	1062.00		NIST
Ip	1075.00		NIST
Ip	1088.00		NIST
Tboil	[440.20; 444.90]	K
Tboil	444.65	K	ChemSep v8.3 pure component data Compiled value
Tboil	444.70	K	KDB
Tboil	Outlier 440.20	K	NIST
Tboil	444.70	K	NIST
Tboil	444.70	K	NIST
Tboil	444.74 ± 0.03	K	NIST
Tboil	444.90 ± 0.50	K	NIST
Tboil	444.69 ± 0.20	K	NIST
Tc	[646.90; 659.26]	K
Tc	646.90	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	652.00	K	Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
Tc	659.26	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	652.00	K	ChemSep v8.3 pure component data Compiled value
Tc	659.00	K	KDB
Tc	659.00	K	NIST
Tfus	[231.95; 232.05]	K
Tfus	232.05	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	231.98	K	ChemSep v8.3 pure component data Compiled value
Tfus	232.00	K	KDB
Tfus	231.95 ± 0.20	K	NIST
Ttriple	231.98	K	ChemSep v8.3 pure component data Compiled value
UQi	5.47		ChemSep v8.3 pure component data Compiled value
URi	6.74		ChemSep v8.3 pure component data Compiled value
Vc	0.510	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2500000		ChemSep v8.3 pure component data Compiled value
Zra	0.26		ChemSep v8.3 pure component data Compiled value

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[264.80; 350.30]	J/mol×K	[313.00; 420.00]
Cp,liquid	264.80	J/mol×K	313.00	NIST
Cp,liquid	269.70	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	277.80	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	285.80	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	293.90	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	301.90	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	310.00	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	318.10	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	326.10	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	334.20	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	342.20	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	350.30	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
ΔvapH	[37.01; 45.00]	kJ/mol	[328.00; 444.70]
ΔvapH	45.00 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	44.00 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	43.00 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	42.40 ± 0.10	kJ/mol	368.00	NIST
ΔvapH	42.90	kJ/mol	400.50	NIST
ΔvapH	37.01	kJ/mol	444.70	NIST
ρl	813.00	kg/m3	293.00	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[185.96; 613.98]	J/mol×K	[273.00; 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			9.53390e+01
Coefficient B			-6.01240e+02
Coefficient C			6.71524e+00
Coefficient D			-1.85210e-05
Coefficient E			-1.57400e-08
Temperature range, min.			273.00
Temperature range, max.			1500.00
Cp,gas	185.96	J/mol×K	273.00	Calculated Property
Cp,gas	283.29	J/mol×K	409.33	Calculated Property
Cp,gas	365.39	J/mol×K	545.67	Calculated Property
Cp,gas	430.20	J/mol×K	682.00	Calculated Property
Cp,gas	480.95	J/mol×K	818.33	Calculated Property
Cp,gas	520.91	J/mol×K	954.67	Calculated Property
Cp,gas	552.58	J/mol×K	1091.00	Calculated Property
Cp,gas	577.81	J/mol×K	1227.33	Calculated Property
Cp,gas	597.95	J/mol×K	1363.67	Calculated Property
Cp,gas	613.98	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[201.58; 370.68]	J/mol×K	[231.98; 444.65]	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			4.09960e+01
Coefficient B			-1.22740e+02
Coefficient C			4.93824e+00
Coefficient D			3.24880e-03
Coefficient E			-1.56110e-06
Temperature range, min.			231.98
Temperature range, max.			444.65
Cp,liquid	201.58	J/mol×K	231.98	Calculated Property
Cp,liquid	219.84	J/mol×K	255.61	Calculated Property
Cp,liquid	238.19	J/mol×K	279.24	Calculated Property
Cp,liquid	256.67	J/mol×K	302.87	Calculated Property
Cp,liquid	275.30	J/mol×K	326.50	Calculated Property
Cp,liquid	294.10	J/mol×K	350.13	Calculated Property
Cp,liquid	313.06	J/mol×K	373.76	Calculated Property
Cp,liquid	332.16	J/mol×K	397.39	Calculated Property
Cp,liquid	351.38	J/mol×K	421.02	Calculated Property
Cp,liquid	370.68	J/mol×K	444.65	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0049117; 0.0002492]	Pa×s	[231.98; 444.65]	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			-1.15490e+01
Coefficient B			1.44590e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			231.98
Temperature range, max.			444.65
η	0.0049117	Pa×s	231.98	Calculated Property
η	0.0027605	Pa×s	255.61	Calculated Property
η	0.0017104	Pa×s	279.24	Calculated Property
η	0.0011420	Pa×s	302.87	Calculated Property
η	0.0008083	Pa×s	326.50	Calculated Property
η	0.0005995	Pa×s	350.13	Calculated Property
η	0.0004618	Pa×s	373.76	Calculated Property
η	0.0003669	Pa×s	397.39	Calculated Property
η	0.0002991	Pa×s	421.02	Calculated Property
η	0.0002492	Pa×s	444.65	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[52.24; 10.87]	kJ/mol	[231.98; 629.89]	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			6.94540e+01
Coefficient B			4.09150e-01
Coefficient C			1.64940e+00
Coefficient D			-3.44940e+00
Coefficient E			1.95730e+00
Critical temperature, Tc (K)			6.52000e+02
Temperature range, min.			231.98
Temperature range, max.			629.89
ΔvapH	52.24	kJ/mol	231.98	Calculated Property
ΔvapH	48.88	kJ/mol	276.19	Calculated Property
ΔvapH	45.70	kJ/mol	320.40	Calculated Property
ΔvapH	42.65	kJ/mol	364.62	Calculated Property
ΔvapH	39.60	kJ/mol	408.83	Calculated Property
ΔvapH	36.31	kJ/mol	453.04	Calculated Property
ΔvapH	32.45	kJ/mol	497.25	Calculated Property
ΔvapH	27.55	kJ/mol	541.47	Calculated Property
ΔvapH	20.87	kJ/mol	585.68	Calculated Property
ΔvapH	10.87	kJ/mol	629.89	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[321.45; 476.05]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.32339e+01
Coefficient B			-3.15642e+03
Coefficient C			-7.76360e+01
Temperature range, min.			321.45
Temperature range, max.			476.05
Pvap	1.33	kPa	321.45	Calculated Property
Pvap	3.13	kPa	338.63	Calculated Property
Pvap	6.60	kPa	355.81	Calculated Property
Pvap	12.77	kPa	372.98	Calculated Property
Pvap	22.97	kPa	390.16	Calculated Property
Pvap	38.87	kPa	407.34	Calculated Property
Pvap	62.45	kPa	424.52	Calculated Property
Pvap	95.95	kPa	441.69	Calculated Property
Pvap	141.80	kPa	458.87	Calculated Property
Pvap	202.63	kPa	476.05	Calculated Property
Pvap	[8.85e-04; 2660.00]	kPa	[231.98; 632.18]	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			1.16259e+02
Coefficient B			-9.67556e+03
Coefficient C			-1.50819e+01
Coefficient D			1.05041e-05
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 652 K.
Temperature range, min.			231.98
Temperature range, max.			632.18
Pvap	8.85e-04	kPa	231.98	Calculated Property
Pvap	0.07	kPa	276.45	Calculated Property
Pvap	1.16	kPa	320.91	Calculated Property
Pvap	8.87	kPa	365.38	Calculated Property
Pvap	39.89	kPa	409.85	Calculated Property
Pvap	127.35	kPa	454.32	Calculated Property
Pvap	324.56	kPa	498.78	Calculated Property
Pvap	712.70	kPa	543.25	Calculated Property
Pvap	1419.83	kPa	587.72	Calculated Property
Pvap	2660.00	kPa	632.18	Calculated Property
Pvap	[0.05; 2616.37]	kPa	[273.15; 659.00]	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			8.63471e+01
Coefficient B			-8.58272e+03
Coefficient C			-1.03859e+01
Coefficient D			4.50963e-06
Coefficient E			0.00000e+00
Temperature range, min.			273.15
Temperature range, max.			659.00
Pvap	0.05	kPa	273.15	Calculated Property
Pvap	0.87	kPa	316.02	Calculated Property
Pvap	6.77	kPa	358.89	Calculated Property
Pvap	31.18	kPa	401.77	Calculated Property
Pvap	100.51	kPa	444.64	Calculated Property
Pvap	252.65	kPa	487.51	Calculated Property
Pvap	531.90	kPa	530.38	Calculated Property
Pvap	985.09	kPa	573.26	Calculated Property
Pvap	1661.41	kPa	616.13	Calculated Property
Pvap	2616.37	kPa	659.00	Calculated Property
Pvap	[6.39; 104.00]	kPa	[357.18; 445.82]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37681e+01
Coefficient B			-3.45415e+03
Coefficient C			-6.72270e+01
Reference			Forziati, Norris, et al., 1949
Temperature range, min.			357.18
Temperature range, max.			445.82
Pvap	6.39	kPa	357.18	Calculated Property
Pvap	9.46	kPa	367.03	Calculated Property
Pvap	13.64	kPa	376.88	Calculated Property
Pvap	19.24	kPa	386.73	Calculated Property
Pvap	26.58	kPa	396.58	Calculated Property
Pvap	36.04	kPa	406.42	Calculated Property
Pvap	48.04	kPa	416.27	Calculated Property
Pvap	63.03	kPa	426.12	Calculated Property
Pvap	81.51	kPa	435.97	Calculated Property
Pvap	104.00	kPa	445.82	Calculated Property
Pvap	[6.39; 104.00]	kPa	[357.18; 445.82]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37681e+01
Coefficient B			-3.45415e+03
Coefficient C			-6.72270e+01
Reference			Forziati, Norris, et al., 1949, 2
Temperature range, min.			357.18
Temperature range, max.			445.82
Pvap	6.39	kPa	357.18	Calculated Property
Pvap	9.46	kPa	367.03	Calculated Property
Pvap	13.64	kPa	376.88	Calculated Property
Pvap	19.24	kPa	386.73	Calculated Property
Pvap	26.58	kPa	396.58	Calculated Property
Pvap	36.04	kPa	406.42	Calculated Property
Pvap	48.04	kPa	416.27	Calculated Property
Pvap	63.03	kPa	426.12	Calculated Property
Pvap	81.51	kPa	435.97	Calculated Property
Pvap	104.00	kPa	445.82	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[862.45; 424.47]	kg/m3	[231.98; 629.89]	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			7.34824e+01
Coefficient B			2.67050e-01
Coefficient C			6.52000e+02
Coefficient D			3.29130e-01
Temperature range, min.			231.98
Temperature range, max.			629.89
ρl	862.45	kg/m3	231.98	Calculated Property
ρl	827.75	kg/m3	276.19	Calculated Property
ρl	791.77	kg/m3	320.40	Calculated Property
ρl	754.19	kg/m3	364.62	Calculated Property
ρl	714.58	kg/m3	408.83	Calculated Property
ρl	672.30	kg/m3	453.04	Calculated Property
ρl	626.28	kg/m3	497.25	Calculated Property
ρl	574.54	kg/m3	541.47	Calculated Property
ρl	512.68	kg/m3	585.68	Calculated Property
ρl	424.47	kg/m3	629.89	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 4.84e-04]	N/m	[231.98; 629.89]	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			-8.90590e-02
Coefficient B			-2.46970e+01
Coefficient C			-1.67640e+00
Coefficient D			-1.56120e-03
Coefficient E			7.20730e-07
Temperature range, min.			231.98
Temperature range, max.			629.89
γ	0.03	N/m	231.98	Calculated Property
γ	0.03	N/m	276.19	Calculated Property
γ	0.02	N/m	320.40	Calculated Property
γ	0.02	N/m	364.62	Calculated Property
γ	0.02	N/m	408.83	Calculated Property
γ	0.01	N/m	453.04	Calculated Property
γ	0.01	N/m	497.25	Calculated Property
γ	0.01	N/m	541.47	Calculated Property
γ	0.00	N/m	585.68	Calculated Property
γ	4.84e-04	N/m	629.89	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.09]	W/m×K	[231.98; 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			7.76070e-02
Coefficient B			1.40040e-01
Coefficient C			-9.19400e+01
Coefficient D			1.37250e+06
Temperature range, min.			231.98
Temperature range, max.			1000.00
λgas	0.01	W/m×K	231.98	Calculated Property
λgas	0.01	W/m×K	317.32	Calculated Property
λgas	0.02	W/m×K	402.65	Calculated Property
λgas	0.03	W/m×K	487.99	Calculated Property
λgas	0.04	W/m×K	573.32	Calculated Property
λgas	0.05	W/m×K	658.66	Calculated Property
λgas	0.06	W/m×K	743.99	Calculated Property
λgas	0.07	W/m×K	829.33	Calculated Property
λgas	0.08	W/m×K	914.66	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.12; 0.09]	W/m×K	[231.98; 444.65]	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			5.44050e-02
Coefficient B			-2.03550e+02
Coefficient C			-5.04950e-01
Coefficient D			-6.58180e-03
Coefficient E			2.90950e-06
Temperature range, min.			231.98
Temperature range, max.			444.65
λliquid	0.12	W/m×K	231.98	Calculated Property
λliquid	0.12	W/m×K	255.61	Calculated Property
λliquid	0.11	W/m×K	279.24	Calculated Property
λliquid	0.11	W/m×K	302.87	Calculated Property
λliquid	0.11	W/m×K	326.50	Calculated Property
λliquid	0.10	W/m×K	350.13	Calculated Property
λliquid	0.10	W/m×K	373.76	Calculated Property
λliquid	0.10	W/m×K	397.39	Calculated Property
λliquid	0.09	W/m×K	421.02	Calculated Property
λliquid	0.09	W/m×K	444.65	Calculated Property

Similar Compounds

Find more compounds similar to Cyclohexane, (1,1-dimethylethyl)-.

Mixtures

• 9H-Fluoren-9-one + Cyclohexane, (1,1-dimethylethyl)-

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).
• Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
• Cheméo Relay (1.0)
• 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
• Crippen Method
• Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
• Joback Method
• KDB
• 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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