Chemical Properties of 1-Undecene (CAS 821-95-4)

InChI

InChI=1S/C11H22/c1-3-5-7-9-11-10-8-6-4-2/h3H,1,4-11H2,2H3

InChI Key

DCTOHCCUXLBQMS-UHFFFAOYSA-N

Formula

C11H22

SMILES

C=CCCCCCCCCC

Molecular Weight¹

154.29

CAS

821-95-4

Other Names

• Undec-1-ene
• Undecene-1
• n-1-Undecene
• «alpha»-Undecene

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• C_sat : Molar heat capacity at saturation pressure (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.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• 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	[0.5180; 0.5225]
ω	0.5180		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.5180		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.5225		ChemSep v8.3 pure component data Compiled value
ω	0.5180		KDB
μ	0.54	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[128.30; 129.50]	kJ/mol
ΔfG°	128.30	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	129.50	kJ/mol	KDB
ΔfH°gas	[-144.90; -144.90]	kJ/mol
ΔfH°gas	-144.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-144.90	kJ/mol	KDB
ΔfusH°	22.97	kJ/mol	Joback Calculated Property
ΔvapH°	[54.30; 55.40]	kJ/mol
ΔvapH°	54.30 ± 0.30	kJ/mol	NIST
ΔvapH°	55.40	kJ/mol	NIST
IE	9.38	eV	Relay (1.0) Calculated Property
log10WS	-5.80		Relay (1.0) Calculated Property
logPoct/wat	4.313		Crippen Calculated Property
McVol	161.550	ml/mol	McGowan Calculated Property
Pc	[1990.00; 2044.00]	kPa
Pc	1996.10	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	1992.58	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2044.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1990.00	kPa	KDB
Ptriple	4.73e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[179.50; 1100.00]
Inp	1082.00		NIST
Inp	1087.00		NIST
Inp	1090.00		NIST
Inp	1089.00		NIST
Inp	1088.00		NIST
Inp	1090.00		NIST
Inp	1094.00		NIST
Inp	1082.00		NIST
Inp	1083.00		NIST
Inp	1084.00		NIST
Inp	1082.00		NIST
Inp	1089.90		NIST
Inp	1087.00		NIST
Inp	1090.00		NIST
Inp	1088.00		NIST
Inp	1090.00		NIST
Inp	1090.50		NIST
Inp	1093.00		NIST
Inp	1092.00		NIST
Inp	1088.00		NIST
Inp	1088.00		NIST
Inp	1092.00		NIST
Inp	1093.00		NIST
Inp	1090.90		NIST
Inp	1091.40		NIST
Inp	1091.40		NIST
Inp	1086.00		NIST
Inp	1090.90		NIST
Inp	1091.40		NIST
Inp	1091.40		NIST
Inp	1089.00		NIST
Inp	1088.00		NIST
Inp	1088.79		NIST
Inp	1088.78		NIST
Inp	1088.91		NIST
Inp	1091.72		NIST
Inp	1091.85		NIST
Inp	1092.00		NIST
Inp	1088.00		NIST
Inp	1092.00		NIST
Inp	1093.00		NIST
Inp	1093.00		NIST
Inp	1092.00		NIST
Inp	1089.00		NIST
Inp	1089.00		NIST
Inp	1091.00		NIST
Inp	1092.00		NIST
Inp	1092.00		NIST
Inp	1092.00		NIST
Inp	1091.00		NIST
Inp	1089.00		NIST
Inp	1095.00		NIST
Inp	1088.60		NIST
Inp	1089.00		NIST
Inp	1088.00		NIST
Inp	1092.00		NIST
Inp	1088.00		NIST
Inp	1097.00		NIST
Inp	1100.00		NIST
Inp	1086.00		NIST
Inp	1090.00		NIST
Inp	1092.00		NIST
Inp	1090.00		NIST
Inp	1082.00		NIST
Inp	1087.00		NIST
Inp	1089.00		NIST
Inp	1088.00		NIST
Inp	1084.00		NIST
Inp	1083.00		NIST
Inp	Outlier 179.50		NIST
Inp	1087.00		NIST
Inp	Outlier 179.50		NIST
Inp	1093.00		NIST
Inp	1090.90		NIST
Inp	1088.79		NIST
Inp	1092.00		NIST
Inp	1088.00		NIST
Inp	1095.00		NIST
Ip	[1135.00; 1160.00]
Ip	1151.00		NIST
Ip	1152.00		NIST
Ip	1154.00		NIST
Ip	1148.00		NIST
Ip	1146.00		NIST
Ip	1146.00		NIST
Ip	1146.00		NIST
Ip	1147.00		NIST
Ip	1145.00		NIST
Ip	1151.20		NIST
Ip	1153.60		NIST
Ip	1148.40		NIST
Ip	1151.20		NIST
Ip	1153.60		NIST
Ip	1148.40		NIST
Ip	1147.00		NIST
Ip	1135.00		NIST
Ip	1142.00		NIST
Ip	1141.00		NIST
Ip	Outlier 1160.00		NIST
Ip	1136.00		NIST
Ip	1139.00		NIST
Ip	1139.00		NIST
Ip	1138.00		NIST
Ip	1136.00		NIST
Ip	1135.00		NIST
S°liquid	456.56	J/mol×K	NIST
Tboil	[462.00; 470.87]	K
Tboil	465.82	K	ChemSep v8.3 pure component data Compiled value
Tboil	465.80	K	KDB
Tboil	465.90	K	NIST
Tboil	462.00 ± 2.00	K	NIST
Tboil	462.00 ± 4.00	K	NIST
Tboil	465.86 ± 0.30	K	NIST
Tboil	465.50 ± 1.00	K	NIST
Tboil	465.85 ± 0.30	K	NIST
Tboil	470.87 ± 3.00	K	NIST
Tboil	470.00 ± 6.00	K	NIST
Tboil	462.00 ± 4.00	K	NIST
Tboil	466.00 ± 4.00	K	NIST
Tc	[637.00; 637.80]	K
Tc	637.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	637.04	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	637.80	K	ChemSep v8.3 pure component data Compiled value
Tc	637.00	K	KDB
Tfus	[223.70; 224.05]	K
Tfus	224.05	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	223.99	K	ChemSep v8.3 pure component data Compiled value
Tfus	224.00	K	KDB
Tfus	223.95 ± 0.50	K	NIST
Tfus	223.96 ± 0.05	K	NIST
Tfus	223.97 ± 0.03	K	NIST
Tfus	223.94 ± 0.05	K	NIST
Tfus	223.96 ± 0.03	K	NIST
Tfus	223.70 ± 2.00	K	NIST
Tfus	223.70 ± 0.50	K	NIST
Tfus	223.70 ± 1.50	K	NIST
Ttriple	[223.98; 223.99]	K
Ttriple	223.99	K	ChemSep v8.3 pure component data Compiled value
Ttriple	223.99 ± 0.01	K	NIST
Ttriple	223.98 ± 0.05	K	NIST
Ttriple	223.99 ± 0.01	K	NIST
UQi	6.34		ChemSep v8.3 pure component data Compiled value
URi	7.64		ChemSep v8.3 pure component data Compiled value
Vc	[0.626; 0.657]	m3/kmol
Vc	0.626	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.657	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.632	m3/kmol	KDB
Zc	[0.2376500; 0.2530000]
Zc	0.2530000		ChemSep v8.3 pure component data Compiled value
Zc	0.2376500		KDB
Zra	0.25		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	329.95	J/mol×K	298.15	NIST
Csat	[308.10; 335.90]	J/mol×K	[230.00; 310.00]
Csat	308.10	J/mol×K	230.00	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
Csat	308.60	J/mol×K	240.00	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
Csat	310.40	J/mol×K	250.00	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
Csat	313.30	J/mol×K	260.00	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
Csat	317.00	J/mol×K	270.00	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
Csat	318.30	J/mol×K	273.15	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
Csat	321.40	J/mol×K	280.00	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
Csat	326.20	J/mol×K	290.00	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
Csat	330.20	J/mol×K	298.15	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
Csat	331.10	J/mol×K	300.00	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
Csat	335.90	J/mol×K	310.00	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	[9.20; 16.99]	kJ/mol	[217.30; 224.00]
ΔfusH	9.20	kJ/mol	217.30	NIST
ΔfusH	16.99	kJ/mol	224.00	NIST
ΔfusH	16.99	kJ/mol	224.00	NIST
ΔvapH	[40.88; 48.20]	kJ/mol	[425.50; 465.80]
ΔvapH	48.20	kJ/mol	425.50	NIST
ΔvapH	40.88	kJ/mol	465.80	KDB
ρl	751.00	kg/m3	293.00	KDB
ΔfusS	[42.36; 75.84]	J/mol×K	[217.30; 224.00]
ΔfusS	42.36	J/mol×K	217.30	NIST
ΔfusS	75.84	J/mol×K	224.00	NIST
γ	0.02	N/m	298.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[230.11; 647.28]	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			1.38670e+02
Coefficient B			-5.49630e+02
Coefficient C			6.49224e+00
Coefficient D			1.48610e-04
Coefficient E			-5.20260e-08
Temperature range, min.			273.00
Temperature range, max.			1500.00
Cp,gas	230.11	J/mol×K	273.00	Calculated Property
Cp,gas	320.24	J/mol×K	409.33	Calculated Property
Cp,gas	396.06	J/mol×K	545.67	Calculated Property
Cp,gas	457.13	J/mol×K	682.00	Calculated Property
Cp,gas	506.41	J/mol×K	818.33	Calculated Property
Cp,gas	546.55	J/mol×K	954.67	Calculated Property
Cp,gas	579.50	J/mol×K	1091.00	Calculated Property
Cp,gas	606.66	J/mol×K	1227.33	Calculated Property
Cp,gas	629.01	J/mol×K	1363.67	Calculated Property
Cp,gas	647.28	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[305.82; 578.32]	J/mol×K	[223.99; 591.88]	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			9.98680e+01
Coefficient B			1.44480e+02
Coefficient C			3.78224e+00
Coefficient D			4.26140e-03
Coefficient E			-1.07910e-06
Temperature range, min.			223.99
Temperature range, max.			591.88
Cp,liquid	305.82	J/mol×K	223.99	Calculated Property
Cp,liquid	317.05	J/mol×K	264.87	Calculated Property
Cp,liquid	334.22	J/mol×K	305.74	Calculated Property
Cp,liquid	356.21	J/mol×K	346.62	Calculated Property
Cp,liquid	382.56	J/mol×K	387.50	Calculated Property
Cp,liquid	413.11	J/mol×K	428.37	Calculated Property
Cp,liquid	447.86	J/mol×K	469.25	Calculated Property
Cp,liquid	486.90	J/mol×K	510.13	Calculated Property
Cp,liquid	530.34	J/mol×K	551.00	Calculated Property
Cp,liquid	578.32	J/mol×K	591.88	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0045429; 0.0001262]	Pa×s	[223.99; 523.15]	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			-4.90126e+01
Coefficient B			2.64317e+03
Coefficient C			5.95795e+00
Coefficient D			-8.45187e-06
Coefficient E			2.00000e+00
Temperature range, min.			223.99
Temperature range, max.			523.15
η	0.0045429	Pa×s	223.99	Calculated Property
η	0.0019697	Pa×s	257.23	Calculated Property
η	0.0010749	Pa×s	290.47	Calculated Property
η	0.0006776	Pa×s	323.71	Calculated Property
η	0.0004684	Pa×s	356.95	Calculated Property
η	0.0003435	Pa×s	390.19	Calculated Property
η	0.0002613	Pa×s	423.43	Calculated Property
η	0.0002033	Pa×s	456.67	Calculated Property
η	0.0001599	Pa×s	489.91	Calculated Property
η	0.0001262	Pa×s	523.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[57.93; 20.01]	kJ/mol	[223.99; 616.02]	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			2.36960e+01
Coefficient B			-6.39330e+00
Coefficient C			1.80840e+01
Coefficient D			-1.90330e+01
Coefficient E			7.47190e+00
Critical temperature, Tc (K)			6.37800e+02
Temperature range, min.			223.99
Temperature range, max.			616.02
ΔvapH	57.93	kJ/mol	223.99	Calculated Property
ΔvapH	56.72	kJ/mol	267.55	Calculated Property
ΔvapH	54.09	kJ/mol	311.11	Calculated Property
ΔvapH	50.75	kJ/mol	354.67	Calculated Property
ΔvapH	47.18	kJ/mol	398.23	Calculated Property
ΔvapH	43.54	kJ/mol	441.78	Calculated Property
ΔvapH	39.72	kJ/mol	485.34	Calculated Property
ΔvapH	35.24	kJ/mol	528.90	Calculated Property
ΔvapH	29.24	kJ/mol	572.46	Calculated Property
ΔvapH	20.01	kJ/mol	616.02	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[345.26; 495.90]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44919e+01
Coefficient B			-3.90995e+03
Coefficient C			-6.99970e+01
Temperature range, min.			345.26
Temperature range, max.			495.90
Pvap	1.33	kPa	345.26	Calculated Property
Pvap	3.01	kPa	362.00	Calculated Property
Pvap	6.22	kPa	378.74	Calculated Property
Pvap	11.93	kPa	395.47	Calculated Property
Pvap	21.46	kPa	412.21	Calculated Property
Pvap	36.57	kPa	428.95	Calculated Property
Pvap	59.41	kPa	445.69	Calculated Property
Pvap	92.61	kPa	462.42	Calculated Property
Pvap	139.20	kPa	479.16	Calculated Property
Pvap	202.65	kPa	495.90	Calculated Property
Pvap	[3.98e-05; 1935.56]	kPa	[223.99; 637.80]	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			8.67402e+01
Coefficient B			-9.30649e+03
Coefficient C			-1.02614e+01
Coefficient D			4.14983e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 637.9 K.
Temperature range, min.			223.99
Temperature range, max.			637.80
Pvap	3.98e-05	kPa	223.99	Calculated Property
Pvap	7.62e-03	kPa	269.97	Calculated Property
Pvap	0.26	kPa	315.95	Calculated Property
Pvap	3.05	kPa	361.93	Calculated Property
Pvap	18.79	kPa	407.91	Calculated Property
Pvap	74.68	kPa	453.88	Calculated Property
Pvap	219.43	kPa	499.86	Calculated Property
Pvap	521.07	kPa	545.84	Calculated Property
Pvap	1061.75	kPa	591.82	Calculated Property
Pvap	1935.56	kPa	637.80	Calculated Property
Pvap	[1.83e-05; 2036.33]	kPa	[223.99; 638.00]	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			1.36979e+02
Coefficient B			-1.16219e+04
Coefficient C			-1.78317e+01
Coefficient D			9.87600e-06
Coefficient E			0.00000e+00
Temperature range, min.			223.99
Temperature range, max.			638.00
Pvap	1.83e-05	kPa	223.99	Calculated Property
Pvap	5.65e-03	kPa	269.99	Calculated Property
Pvap	0.23	kPa	315.99	Calculated Property
Pvap	3.03	kPa	361.99	Calculated Property
Pvap	19.03	kPa	407.99	Calculated Property
Pvap	75.09	kPa	454.00	Calculated Property
Pvap	218.40	kPa	500.00	Calculated Property
Pvap	518.24	kPa	546.00	Calculated Property
Pvap	1073.88	kPa	592.00	Calculated Property
Pvap	2036.33	kPa	638.00	Calculated Property
Pvap	[6.40; 104.02]	kPa	[379.02; 466.89]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40262e+01
Coefficient B			-3.59772e+03
Coefficient C			-8.34070e+01
Reference			Forziati, Camin, et al., 1950, 2
Temperature range, min.			379.02
Temperature range, max.			466.89
Pvap	6.40	kPa	379.02	Calculated Property
Pvap	9.44	kPa	388.78	Calculated Property
Pvap	13.60	kPa	398.55	Calculated Property
Pvap	19.16	kPa	408.31	Calculated Property
Pvap	26.47	kPa	418.07	Calculated Property
Pvap	35.90	kPa	427.84	Calculated Property
Pvap	47.88	kPa	437.60	Calculated Property
Pvap	62.88	kPa	447.36	Calculated Property
Pvap	81.41	kPa	457.13	Calculated Property
Pvap	104.02	kPa	466.89	Calculated Property
Pvap	[6.40; 104.02]	kPa	[379.02; 466.89]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40262e+01
Coefficient B			-3.59772e+03
Coefficient C			-8.34070e+01
Reference			Forziati, Camin, et al., 1950
Temperature range, min.			379.02
Temperature range, max.			466.89
Pvap	6.40	kPa	379.02	Calculated Property
Pvap	9.44	kPa	388.78	Calculated Property
Pvap	13.60	kPa	398.55	Calculated Property
Pvap	19.16	kPa	408.31	Calculated Property
Pvap	26.47	kPa	418.07	Calculated Property
Pvap	35.90	kPa	427.84	Calculated Property
Pvap	47.88	kPa	437.60	Calculated Property
Pvap	62.88	kPa	447.36	Calculated Property
Pvap	81.41	kPa	457.13	Calculated Property
Pvap	104.02	kPa	466.89	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[799.01; 234.62]	kg/m3	[223.99; 637.80]	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			5.86327e+01
Coefficient B			2.49910e-01
Coefficient C			6.37800e+02
Coefficient D			2.85710e-01
Temperature range, min.			223.99
Temperature range, max.			637.80
ρl	799.01	kg/m3	223.99	Calculated Property
ρl	767.26	kg/m3	269.97	Calculated Property
ρl	733.97	kg/m3	315.95	Calculated Property
ρl	698.77	kg/m3	361.93	Calculated Property
ρl	661.12	kg/m3	407.91	Calculated Property
ρl	620.14	kg/m3	453.88	Calculated Property
ρl	574.36	kg/m3	499.86	Calculated Property
ρl	520.77	kg/m3	545.84	Calculated Property
ρl	451.27	kg/m3	591.82	Calculated Property
ρl	234.62	kg/m3	637.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 6.49e-04]	N/m	[223.99; 616.02]	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			-7.73970e-03
Coefficient B			7.89440e+01
Coefficient C			-3.63550e+00
Coefficient D			1.49240e-03
Coefficient E			-5.77860e-06
Temperature range, min.			223.99
Temperature range, max.			616.02
γ	0.03	N/m	223.99	Calculated Property
γ	0.03	N/m	267.55	Calculated Property
γ	0.02	N/m	311.11	Calculated Property
γ	0.02	N/m	354.67	Calculated Property
γ	0.02	N/m	398.23	Calculated Property
γ	0.01	N/m	441.78	Calculated Property
γ	0.01	N/m	485.34	Calculated Property
γ	0.01	N/m	528.90	Calculated Property
γ	0.00	N/m	572.46	Calculated Property
γ	6.49e-04	N/m	616.02	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.09]	W/m×K	[223.99; 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			1.83350e-05
Coefficient B			1.30310e+00
Coefficient C			7.09580e+02
Coefficient D			-2.80460e+03
Temperature range, min.			223.99
Temperature range, max.			1000.00
λgas	0.01	W/m×K	223.99	Calculated Property
λgas	0.01	W/m×K	310.21	Calculated Property
λgas	0.02	W/m×K	396.44	Calculated Property
λgas	0.02	W/m×K	482.66	Calculated Property
λgas	0.03	W/m×K	568.88	Calculated Property
λgas	0.04	W/m×K	655.11	Calculated Property
λgas	0.05	W/m×K	741.33	Calculated Property
λgas	0.06	W/m×K	827.55	Calculated Property
λgas	0.07	W/m×K	913.78	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.09]	W/m×K	[223.99; 465.82]	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			6.78470e-02
Coefficient B			-2.50410e+02
Coefficient C			4.02010e-01
Coefficient D			-8.28280e-03
Coefficient E			1.40580e-06
Temperature range, min.			223.99
Temperature range, max.			465.82
λliquid	0.15	W/m×K	223.99	Calculated Property
λliquid	0.14	W/m×K	250.86	Calculated Property
λliquid	0.14	W/m×K	277.73	Calculated Property
λliquid	0.13	W/m×K	304.60	Calculated Property
λliquid	0.12	W/m×K	331.47	Calculated Property
λliquid	0.11	W/m×K	358.34	Calculated Property
λliquid	0.11	W/m×K	385.21	Calculated Property
λliquid	0.10	W/m×K	412.08	Calculated Property
λliquid	0.10	W/m×K	438.95	Calculated Property
λliquid	0.09	W/m×K	465.82	Calculated Property

Similar Compounds

Find more compounds similar to 1-Undecene.

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.
• 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
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• 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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