Chemical Properties of TRICOSANE (CAS 638-67-5)

InChI

InChI=1S/C23H48/c1-3-5-7-9-11-13-15-17-19-21-23-22-20-18-16-14-12-10-8-6-4-2/h3-23H2,1-2H3

InChI Key

FIGVVZUWCLSUEI-UHFFFAOYSA-N

Formula

C23H48

SMILES

CCCCCCCCCCCCCCCCCCCCCCC

Molecular Weight¹

324.64

CAS

638-67-5

Other Names

• n-tricosane

• 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_fusH : Enthalpy of fusion 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_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (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).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[1.0247; 1.0262]
ω	1.0247		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	1.0262		ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	139.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-519.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	55.33	kJ/mol	Joback Calculated Property
ΔvapH°	[117.00; 120.50]	kJ/mol
ΔvapH°	117.00	kJ/mol	NIST
ΔvapH°	118.70 ± 0.10	kJ/mol	NIST
ΔvapH°	119.70 ± 2.30	kJ/mol	NIST
ΔvapH°	120.50 ± 2.00	kJ/mol	NIST
IE	9.99	eV	Relay (1.0) Calculated Property
log10WS	-9.49		Relay (1.0) Calculated Property
logPoct/wat	9.218		Crippen Calculated Property
McVol	334.930	ml/mol	McGowan Calculated Property
Pc	[900.00; 1020.00]	kPa
Pc	920.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Pc	947.39	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	Outlier 1020.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	920.00	kPa	KDB
Pc	900.00 ± 200.00	kPa	NIST
Pc	915.00 ± 40.00	kPa	NIST
Ptriple	1.87e-06	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[369.44; 388.80]
Inp	369.44		NIST
Inp	376.29		NIST
Inp	388.70		NIST
Inp	388.70		NIST
Inp	388.80		NIST
Inp	369.44		NIST
Tboil	[593.90; 653.20]	K
Tboil	653.15	K	ChemSep v8.3 pure component data Compiled value
Tboil	653.20	K	NIST
Tboil	593.90 ± 2.00	K	NIST
Tc	[789.70; 796.00]	K
Tc	791.00	K	Critical temperatures and pressures of C40, C44, and C60 normal alkanes measured by the pulse-heating technique
Tc	790.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Tc	790.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	Outlier 796.00	K	ChemSep v8.3 pure component data Compiled value
Tc	790.00	K	KDB
Tc	790.00 ± 8.00	K	NIST
Tc	789.70 ± 3.00	K	NIST
Tfus	[317.30; 322.15]	K
Tfus	322.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	320.95	K	ChemSep v8.3 pure component data Compiled value
Tfus	320.75 ± 0.15	K	NIST
Tfus	320.57 ± 0.30	K	NIST
Tfus	320.70 ± 0.30	K	NIST
Tfus	320.50 ± 0.25	K	NIST
Tfus	320.20 ± 0.60	K	NIST
Tfus	320.00 ± 2.00	K	NIST
Tfus	320.47 ± 0.40	K	NIST
Tfus	319.00 ± 2.00	K	NIST
Tfus	321.00 ± 2.00	K	NIST
Tfus	320.00 ± 2.00	K	NIST
Tfus	Outlier 317.30 ± 3.00	K	NIST
Tfus	319.00 ± 3.00	K	NIST
Tfus	321.00 ± 6.00	K	NIST
Tfus	320.50 ± 0.50	K	NIST
Tfus	320.90 ± 2.00	K	NIST
Tfus	320.90 ± 1.00	K	NIST
Ttriple	320.65	K	ChemSep v8.3 pure component data Compiled value
UQi	13.04		ChemSep v8.3 pure component data Compiled value
URi	15.96		ChemSep v8.3 pure component data Compiled value
Vc	[1.310; 1.350]	m3/kmol
Vc	1.310	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	1.350	m3/kmol	ChemSep v8.3 pure component data Compiled value
VCOSTALD	1.65	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	1.05		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	0.2080590		ChemSep v8.3 pure component data Compiled value
Zra	[0.23; 0.23]
Zra	0.23		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.23		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[734.00; 882.00]	J/mol×K	[320.00; 450.00]
Cp,liquid	734.00	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	745.00	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	757.00	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	768.00	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	772.00	J/mol×K	353.00	NIST
Cp,liquid	779.00	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	791.00	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	802.00	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	814.00	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	825.00	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	836.00	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	848.00	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	859.00	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	871.00	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	882.00	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
ΔfusH	[21.76; 76.70]	kJ/mol	[313.70; 320.70]
ΔfusH	21.76	kJ/mol	313.70	NIST
ΔfusH	76.70	kJ/mol	319.70	NIST
ΔfusH	52.60	kJ/mol	320.20	NIST
ΔfusH	53.97	kJ/mol	320.70	NIST
ΔfusH	53.97	kJ/mol	320.70	NIST
ΔvapH	[92.00; 123.00]	kJ/mol	[298.15; 546.50]
ΔvapH	117.00	kJ/mol	298.15	Vapor Pressures and Vaporization Enthalpies of the n-Alkanes from C21 to C30 at T = 298.15 K by Correlation Gas Chromatography
ΔvapH	110.40	kJ/mol	333.50	NIST
ΔvapH	123.00 ± 1.00	kJ/mol	393.00	NIST
ΔvapH	92.00	kJ/mol	430.00	NIST
ΔvapH	93.50	kJ/mol	437.00	NIST
ΔvapH	94.00	kJ/mol	546.50	NIST
Pvap	[0.01; 0.24]	kPa	[412.18; 461.99]
Pvap	0.01	kPa	412.18	Experimental Vapor Pressures of Six n-Alkanes (C21, C23, C25, C27, C29, C30) in the Temperature Range between 350 K and 460 K
Pvap	0.02	kPa	422.26	Experimental Vapor Pressures of Six n-Alkanes (C21, C23, C25, C27, C29, C30) in the Temperature Range between 350 K and 460 K
Pvap	0.02	kPa	422.29	Experimental Vapor Pressures of Six n-Alkanes (C21, C23, C25, C27, C29, C30) in the Temperature Range between 350 K and 460 K
Pvap	0.05	kPa	432.34	Experimental Vapor Pressures of Six n-Alkanes (C21, C23, C25, C27, C29, C30) in the Temperature Range between 350 K and 460 K
Pvap	0.08	kPa	442.33	Experimental Vapor Pressures of Six n-Alkanes (C21, C23, C25, C27, C29, C30) in the Temperature Range between 350 K and 460 K
Pvap	0.14	kPa	452.22	Experimental Vapor Pressures of Six n-Alkanes (C21, C23, C25, C27, C29, C30) in the Temperature Range between 350 K and 460 K
Pvap	0.24	kPa	461.99	Experimental Vapor Pressures of Six n-Alkanes (C21, C23, C25, C27, C29, C30) in the Temperature Range between 350 K and 460 K
ΔfusS	[69.37; 239.90]	J/mol×K	[313.70; 320.70]
ΔfusS	69.37	J/mol×K	313.70	NIST
ΔfusS	239.90	J/mol×K	319.70	NIST
ΔfusS	168.33	J/mol×K	320.70	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	472.70	K	0.40	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[494.85; 1399.06]	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			3.04710e+02
Coefficient B			-5.67010e+02
Coefficient C			7.29324e+00
Coefficient D			1.28620e-04
Coefficient E			-4.89990e-08
Temperature range, min.			273.00
Temperature range, max.			1500.00
Cp,gas	494.85	J/mol×K	273.00	Calculated Property
Cp,gas	689.42	J/mol×K	409.33	Calculated Property
Cp,gas	854.60	J/mol×K	545.67	Calculated Property
Cp,gas	987.90	J/mol×K	682.00	Calculated Property
Cp,gas	1095.32	J/mol×K	818.33	Calculated Property
Cp,gas	1182.53	J/mol×K	954.67	Calculated Property
Cp,gas	1253.83	J/mol×K	1091.00	Calculated Property
Cp,gas	1312.29	J/mol×K	1227.33	Calculated Property
Cp,gas	1360.16	J/mol×K	1363.67	Calculated Property
Cp,gas	1399.06	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[731.55; 1223.08]	J/mol×K	[320.65; 750.00]	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			-5.86550e+01
Coefficient B			-9.98450e+01
Coefficient C			6.84624e+00
Coefficient D			3.07680e-04
Coefficient E			3.77050e-07
Temperature range, min.			320.65
Temperature range, max.			750.00
Cp,liquid	731.55	J/mol×K	320.65	Calculated Property
Cp,liquid	786.64	J/mol×K	368.36	Calculated Property
Cp,liquid	838.79	J/mol×K	416.06	Calculated Property
Cp,liquid	889.71	J/mol×K	463.77	Calculated Property
Cp,liquid	940.63	J/mol×K	511.47	Calculated Property
Cp,liquid	992.49	J/mol×K	559.18	Calculated Property
Cp,liquid	1046.03	J/mol×K	606.88	Calculated Property
Cp,liquid	1101.93	J/mol×K	654.59	Calculated Property
Cp,liquid	1160.76	J/mol×K	702.29	Calculated Property
Cp,liquid	1223.08	J/mol×K	750.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0046617; 0.0001704]	Pa×s	[320.65; 716.40]	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			-8.83940e+00
Coefficient B			1.94980e+03
Coefficient C			-4.70880e-01
Coefficient D			1.04460e-06
Coefficient E			2.00000e+00
Temperature range, min.			320.65
Temperature range, max.			716.40
η	0.0046617	Pa×s	320.65	Calculated Property
η	0.0021750	Pa×s	364.62	Calculated Property
η	0.0012014	Pa×s	408.59	Calculated Property
η	0.0007492	Pa×s	452.57	Calculated Property
η	0.0005115	Pa×s	496.54	Calculated Property
η	0.0003745	Pa×s	540.51	Calculated Property
η	0.0002898	Pa×s	584.48	Calculated Property
η	0.0002344	Pa×s	628.46	Calculated Property
η	0.0001968	Pa×s	672.43	Calculated Property
η	0.0001704	Pa×s	716.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[107.99; 0.00]	kJ/mol	[320.65; 796.00]	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			1.64340e+02
Coefficient B			1.00680e+00
Coefficient C			-5.51690e-01
Coefficient D			3.14540e-01
Coefficient E			-3.24400e-01
Critical temperature, Tc (K)			7.96000e+02
Temperature range, min.			320.65
Temperature range, max.			796.00
ΔvapH	107.99	kJ/mol	320.65	Calculated Property
ΔvapH	100.04	kJ/mol	373.47	Calculated Property
ΔvapH	92.34	kJ/mol	426.28	Calculated Property
ΔvapH	84.83	kJ/mol	479.10	Calculated Property
ΔvapH	77.45	kJ/mol	531.92	Calculated Property
ΔvapH	70.07	kJ/mol	584.73	Calculated Property
ΔvapH	62.39	kJ/mol	637.55	Calculated Property
ΔvapH	53.76	kJ/mol	690.37	Calculated Property
ΔvapH	42.12	kJ/mol	743.18	Calculated Property
ΔvapH	0.00	kJ/mol	796.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[4.71e-06; 581.37]	kPa	[320.65; 796.00]	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			-2.89881e+01
Coefficient B			-9.53411e+03
Coefficient C			8.27405e+00
Coefficient D			-1.25255e-05
Coefficient E			2.00000e+00
Temperature range, min.			320.65
Temperature range, max.			796.00
Pvap	4.71e-06	kPa	320.65	Calculated Property
Pvap	7.05e-04	kPa	373.47	Calculated Property
Pvap	0.03	kPa	426.28	Calculated Property
Pvap	0.50	kPa	479.10	Calculated Property
Pvap	4.38	kPa	531.92	Calculated Property
Pvap	23.09	kPa	584.73	Calculated Property
Pvap	81.22	kPa	637.55	Calculated Property
Pvap	204.65	kPa	690.37	Calculated Property
Pvap	389.30	kPa	743.18	Calculated Property
Pvap	581.37	kPa	796.00	Calculated Property
Pvap	[0.07; 101.34]	kPa	[440.15; 653.15]	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			3.05833e+02
Coefficient B			-2.71788e+04
Coefficient C			-4.10052e+01
Coefficient D			1.44985e-05
Coefficient E			0.00000e+00
Temperature range, min.			440.15
Temperature range, max.			653.15
Pvap	0.07	kPa	440.15	Calculated Property
Pvap	0.25	kPa	463.82	Calculated Property
Pvap	0.77	kPa	487.48	Calculated Property
Pvap	2.04	kPa	511.15	Calculated Property
Pvap	4.80	kPa	534.82	Calculated Property
Pvap	10.20	kPa	558.48	Calculated Property
Pvap	19.90	kPa	582.15	Calculated Property
Pvap	36.17	kPa	605.82	Calculated Property
Pvap	62.01	kPa	629.48	Calculated Property
Pvap	101.34	kPa	653.15	Calculated Property
Pvap	[0.13; 102.44]	kPa	[443.00; 639.70]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.97034e+01
Coefficient B			-9.67102e+03
Coefficient C			1.86400e+00
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			443.00
Temperature range, max.			639.70
Pvap	0.13	kPa	443.00	Calculated Property
Pvap	0.36	kPa	464.86	Calculated Property
Pvap	0.91	kPa	486.71	Calculated Property
Pvap	2.13	kPa	508.57	Calculated Property
Pvap	4.64	kPa	530.42	Calculated Property
Pvap	9.50	kPa	552.28	Calculated Property
Pvap	18.42	kPa	574.13	Calculated Property
Pvap	34.03	kPa	595.99	Calculated Property
Pvap	60.20	kPa	617.84	Calculated Property
Pvap	102.44	kPa	639.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[806.54; 383.66]	kg/m3	[273.15; 770.98]	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			1.58632e+01
Coefficient B			1.29220e-01
Coefficient C			8.18250e+02
Coefficient D			2.05310e-01
Temperature range, min.			273.15
Temperature range, max.			770.98
ρl	806.54	kg/m3	273.15	Calculated Property
ρl	774.21	kg/m3	328.46	Calculated Property
ρl	740.33	kg/m3	383.78	Calculated Property
ρl	704.54	kg/m3	439.09	Calculated Property
ρl	666.40	kg/m3	494.41	Calculated Property
ρl	625.20	kg/m3	549.72	Calculated Property
ρl	579.85	kg/m3	605.04	Calculated Property
ρl	528.44	kg/m3	660.35	Calculated Property
ρl	466.96	kg/m3	715.67	Calculated Property
ρl	383.66	kg/m3	770.98	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 2.79e-04]	N/m	[320.65; 796.00]	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			-3.25200e-02
Coefficient B			-8.69480e+01
Coefficient C			-1.77970e+00
Coefficient D			-2.65250e-03
Coefficient E			9.20070e-07
Temperature range, min.			320.65
Temperature range, max.			796.00
γ	0.03	N/m	320.65	Calculated Property
γ	0.02	N/m	373.47	Calculated Property
γ	0.02	N/m	426.28	Calculated Property
γ	0.02	N/m	479.10	Calculated Property
γ	0.01	N/m	531.92	Calculated Property
γ	0.01	N/m	584.73	Calculated Property
γ	0.01	N/m	637.55	Calculated Property
γ	0.00	N/m	690.37	Calculated Property
γ	0.00	N/m	743.18	Calculated Property
γ	2.79e-04	N/m	796.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.06]	W/m×K	[320.65; 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			-2.32830e+02
Coefficient B			1.05660e+00
Coefficient C			-5.27470e+09
Coefficient D			-9.86040e+10
Temperature range, min.			320.65
Temperature range, max.			1000.00
λgas	0.01	W/m×K	320.65	Calculated Property
λgas	0.01	W/m×K	396.13	Calculated Property
λgas	0.01	W/m×K	471.62	Calculated Property
λgas	0.02	W/m×K	547.10	Calculated Property
λgas	0.02	W/m×K	622.58	Calculated Property
λgas	0.03	W/m×K	698.07	Calculated Property
λgas	0.04	W/m×K	773.55	Calculated Property
λgas	0.05	W/m×K	849.03	Calculated Property
λgas	0.05	W/m×K	924.52	Calculated Property
λgas	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.08]	W/m×K	[320.65; 653.35]	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			-1.82180e-01
Coefficient B			1.91470e-01
Coefficient C			-9.49060e-01
Coefficient D			-3.56420e-04
Coefficient E			-3.50250e-07
Temperature range, min.			320.65
Temperature range, max.			653.35
λliquid	0.15	W/m×K	320.65	Calculated Property
λliquid	0.14	W/m×K	357.62	Calculated Property
λliquid	0.14	W/m×K	394.58	Calculated Property
λliquid	0.13	W/m×K	431.55	Calculated Property
λliquid	0.12	W/m×K	468.52	Calculated Property
λliquid	0.11	W/m×K	505.48	Calculated Property
λliquid	0.11	W/m×K	542.45	Calculated Property
λliquid	0.10	W/m×K	579.42	Calculated Property
λliquid	0.09	W/m×K	616.38	Calculated Property
λliquid	0.08	W/m×K	653.35	Calculated Property

Similar Compounds

Find more compounds similar to TRICOSANE.

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).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 ChEDL chemicals 1.5.2, from Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkanes. J. Chem. Eng. Data 1995, 40, 531-546.
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• 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
• Critical temperatures and pressures of C40, C44, and C60 normal alkanes measured by the pulse-heating technique
• Vapor Pressures and Vaporization Enthalpies of the n-Alkanes from C21 to C30 at T = 298.15 K by Correlation Gas Chromatography
• Experimental Vapor Pressures of Six n-Alkanes (C21, C23, C25, C27, C29, C30) in the Temperature Range between 350 K and 460 K
• Joback Method
• KDB
• 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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