Chemical Properties of Cyclohexene (CAS 110-83-8)

InChI

InChI=1S/C6H10/c1-2-4-6-5-3-1/h1-2H,3-6H2

InChI Key

HGCIXCUEYOPUTN-UHFFFAOYSA-N

Formula

C6H10

SMILES

C1=CCCCC1

Molecular Weight¹

82.14

CAS

110-83-8

Other Names

• 1,2,3,4-tetrahydrobenzene
• 1-Cyclohexene
• BENZENETETRAHYDRIDE
• Benzene, tetrahydro-
• Cykloheksen
• Hexanaphthylene
• NSC 24835
• UN 2256
• benzene tetrahydride
• cyclohex-1-ene
• tetrahydrobenzene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• 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_fH°_liquid : Liquid phase 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• 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°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• 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	[0.2123; 0.2741]
ω	0.2741		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2123		ChemSep v8.3 pure component data Compiled value
PAff	784.50	kJ/mol	NIST
BasG	752.00	kJ/mol	NIST
ΔcH°liquid	[-3761.00; -3751.50]	kJ/mol
ΔcH°liquid	-3752.39 ± 0.49	kJ/mol	NIST
ΔcH°liquid	-3752.00 ± 0.50	kJ/mol	NIST
ΔcH°liquid	-3751.50 ± 0.50	kJ/mol	NIST
ΔcH°liquid	-3761.00	kJ/mol	NIST
μ	0.55	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	107.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-7.10; -4.32]	kJ/mol
ΔfH°gas	-4.52	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-4.32 ± 0.98	kJ/mol	NIST
ΔfH°gas	-4.70	kJ/mol	NIST
ΔfH°gas	-5.30	kJ/mol	NIST
ΔfH°gas	-7.10	kJ/mol	NIST
ΔfH°liquid	[-40.60; -37.80]	kJ/mol
ΔfH°liquid	-37.80 ± 8.20	kJ/mol	NIST
ΔfH°liquid	-38.20 ± 0.59	kJ/mol	NIST
ΔfH°liquid	-38.80 ± 0.59	kJ/mol	NIST
ΔfH°liquid	-40.60 ± 0.79	kJ/mol	NIST
ΔfusH°	3.28	kJ/mol	Joback Calculated Property
ΔvapH°	[30.50; 33.57]	kJ/mol
ΔvapH°	33.57	kJ/mol	NIST
ΔvapH°	33.50 ± 0.53	kJ/mol	NIST
ΔvapH°	33.50	kJ/mol	NIST
ΔvapH°	33.50 ± 0.50	kJ/mol	NIST
ΔvapH°	30.50 ± 0.30	kJ/mol	NIST
IE	[8.92; 9.57]	eV
IE	8.95 ± 0.01	eV	NIST
IE	8.94	eV	NIST
IE	8.94 ± 0.02	eV	NIST
IE	8.95	eV	NIST
IE	8.94 ± 0.01	eV	NIST
IE	Outlier 9.57 ± 0.05	eV	NIST
IE	8.99	eV	NIST
IE	8.92	eV	NIST
IE	8.95 ± 0.01	eV	NIST
IE	8.94	eV	NIST
IE	8.92 ± 0.02	eV	NIST
IE	8.95 ± 0.01	eV	NIST
IE	9.09	eV	NIST
IE	9.12	eV	NIST
IE	9.12	eV	NIST
IE	9.12	eV	NIST
IE	9.11	eV	NIST
log10WS	[-2.59; -2.59]
log10WS	-2.59		Aq. Solubility Prediction
log10WS	-2.59		Estimated Solubility
logPoct/wat	2.117		Crippen Calculated Property
McVol	80.240	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[4350.00; 4905.60]	kPa
Pc	4905.60	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4350.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	1.04e-04	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[643.00; 714.00]
Inp	Outlier 705.00		NIST
Inp	685.00		NIST
Inp	689.00		NIST
Inp	671.00		NIST
Inp	Outlier 704.40		NIST
Inp	688.00		NIST
Inp	683.00		NIST
Inp	680.50		NIST
Inp	676.80		NIST
Inp	698.00		NIST
Inp	693.00		NIST
Inp	688.00		NIST
Inp	684.00		NIST
Inp	688.00		NIST
Inp	683.00		NIST
Inp	687.50		NIST
Inp	674.00		NIST
Inp	674.00		NIST
Inp	700.00		NIST
Inp	690.00		NIST
Inp	694.00		NIST
Inp	681.00		NIST
Inp	685.10		NIST
Inp	675.90		NIST
Inp	Outlier 704.00		NIST
Inp	682.00		NIST
Inp	671.00		NIST
Inp	675.70		NIST
Inp	667.00		NIST
Inp	669.00		NIST
Inp	673.00		NIST
Inp	676.00		NIST
Inp	677.00		NIST
Inp	683.00		NIST
Inp	670.50		NIST
Inp	670.40		NIST
Inp	672.40		NIST
Inp	672.40		NIST
Inp	669.00		NIST
Inp	677.00		NIST
Inp	685.00		NIST
Inp	687.00		NIST
Inp	666.00		NIST
Inp	683.00		NIST
Inp	702.00		NIST
Inp	687.00		NIST
Inp	666.00		NIST
Inp	685.00		NIST
Inp	668.30		NIST
Inp	674.40		NIST
Inp	679.00		NIST
Inp	668.00		NIST
Inp	674.00		NIST
Inp	679.00		NIST
Inp	679.00		NIST
Inp	680.00		NIST
Inp	Outlier 707.00		NIST
Inp	667.00		NIST
Inp	673.00		NIST
Inp	677.00		NIST
Inp	681.00		NIST
Inp	689.00		NIST
Inp	677.00		NIST
Inp	681.00		NIST
Inp	695.00		NIST
Inp	667.00		NIST
Inp	673.60		NIST
Inp	673.00		NIST
Inp	667.00		NIST
Inp	687.40		NIST
Inp	701.10		NIST
Inp	677.10		NIST
Inp	676.70		NIST
Inp	678.80		NIST
Inp	677.10		NIST
Inp	676.70		NIST
Inp	678.80		NIST
Inp	667.76		NIST
Inp	667.80		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	667.00		NIST
Inp	Outlier 643.00		NIST
Inp	683.00		NIST
Inp	674.00		NIST
Inp	666.00		NIST
Inp	675.00		NIST
Inp	673.00		NIST
Inp	678.00		NIST
Inp	677.00		NIST
Inp	675.00		NIST
Inp	673.00		NIST
Inp	675.00		NIST
Inp	667.00		NIST
Inp	681.00		NIST
Inp	683.00		NIST
Inp	700.00		NIST
Inp	700.00		NIST
Inp	Outlier 714.00		NIST
Inp	687.00		NIST
Inp	657.00		NIST
Inp	681.00		NIST
Inp	675.00		NIST
Inp	665.00		NIST
Inp	681.00		NIST
Inp	703.00		NIST
Inp	661.00		NIST
Inp	667.00		NIST
Inp	681.00		NIST
Inp	Outlier 705.00		NIST
Inp	689.00		NIST
Inp	679.00		NIST
Inp	689.00		NIST
Inp	679.00		NIST
Ip	[808.00; 850.00]
Ip	822.00		NIST
Ip	850.00		NIST
Ip	832.00		NIST
Ip	841.00		NIST
Ip	825.00		NIST
Ip	850.00		NIST
Ip	849.70		NIST
Ip	832.40		NIST
Ip	840.90		NIST
Ip	849.70		NIST
Ip	832.40		NIST
Ip	840.90		NIST
Ip	808.00		NIST
Ip	808.00		NIST
Ip	808.00		NIST
Ip	811.00		NIST
Ip	808.00		NIST
S°gas	310.45	J/mol×K	NIST
S°liquid	[214.60; 216.70]	J/mol×K
S°liquid	214.60	J/mol×K	NIST
S°liquid	216.19	J/mol×K	NIST
S°liquid	216.70	J/mol×K	NIST
Tboil	[353.00; 358.00]	K
Tboil	355.97	K	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Tboil	356.15	K	Vapor Liquid Equilibrium Data for Binary Systems of N,N-Dimethylacetamide with Cyclohexene, Cyclohexane, and Benzene Separately at Atmospheric Pressure
Tboil	355.97	K	Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and Methyl Isobutyl Ketone at 100 kPa
Tboil	355.97	K	Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa
Tboil	356.12	K	ChemSep v8.3 pure component data Compiled value
Tboil	356.13	K	KDB
Tboil	356.15 ± 0.10	K	NIST
Tboil	356.20	K	NIST
Tboil	355.50 ± 0.50	K	NIST
Tboil	356.20	K	NIST
Tboil	356.16 ± 0.20	K	NIST
Tboil	356.00 ± 1.00	K	NIST
Tboil	356.15 ± 0.40	K	NIST
Tboil	356.30 ± 0.40	K	NIST
Tboil	354.15 ± 2.00	K	NIST
Tboil	356.30 ± 0.30	K	NIST
Tboil	356.13 ± 0.30	K	NIST
Tboil	Outlier 354.00 ± 5.00	K	NIST
Tboil	355.90 ± 2.00	K	NIST
Tboil	356.15 ± 0.10	K	NIST
Tboil	Outlier 354.00 ± 3.00	K	NIST
Tboil	356.90 ± 1.00	K	NIST
Tboil	Outlier 353.00 ± 4.00	K	NIST
Tboil	355.00 ± 5.00	K	NIST
Tboil	357.00 ± 4.00	K	NIST
Tboil	356.15 ± 0.30	K	NIST
Tboil	355.70 ± 0.50	K	NIST
Tboil	355.65 ± 1.00	K	NIST
Tboil	Outlier 354.00 ± 5.00	K	NIST
Tboil	356.20 ± 0.40	K	NIST
Tboil	356.10 ± 0.50	K	NIST
Tboil	356.20 ± 0.60	K	NIST
Tboil	355.00 ± 2.00	K	NIST
Tboil	356.15 ± 1.00	K	NIST
Tboil	356.12 ± 0.10	K	NIST
Tboil	355.00 ± 2.00	K	NIST
Tboil	356.40 ± 1.00	K	NIST
Tboil	355.90 ± 0.40	K	NIST
Tboil	355.50 ± 0.50	K	NIST
Tboil	357.00 ± 4.00	K	NIST
Tboil	356.00 ± 0.60	K	NIST
Tboil	356.34 ± 0.20	K	NIST
Tboil	355.30 ± 0.40	K	NIST
Tboil	357.00 ± 3.00	K	NIST
Tboil	355.85 ± 0.50	K	NIST
Tboil	357.00 ± 2.00	K	NIST
Tboil	355.85 ± 0.15	K	NIST
Tboil	356.30 ± 0.60	K	NIST
Tboil	357.00 ± 3.00	K	NIST
Tboil	Outlier 358.00 ± 3.00	K	NIST
Tboil	355.80 ± 0.30	K	NIST
Tboil	357.00 ± 3.00	K	NIST
Tboil	356.70 ± 2.00	K	NIST
Tboil	Outlier 354.00 ± 3.00	K	NIST
Tboil	356.40 ± 0.20	K	NIST
Tboil	357.00 ± 4.00	K	NIST
Tboil	356.40 ± 2.00	K	NIST
Tboil	356.00 ± 3.00	K	NIST
Tboil	Outlier 354.00 ± 4.00	K	NIST
Tboil	356.00 ± 3.00	K	NIST
Tboil	356.45 ± 1.00	K	NIST
Tboil	357.00 ± 2.00	K	NIST
Tboil	355.50 ± 2.00	K	NIST
Tc	[553.50; 560.42]	K
Tc	560.40	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	560.40	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	560.42	K	ChemSep v8.3 pure component data Compiled value
Tc	560.40	K	KDB
Tc	560.40 ± 0.10	K	NIST
Tc	560.40	K	NIST
Tc	560.40 ± 0.30	K	NIST
Tc	560.42 ± 0.02	K	NIST
Tc	Outlier 553.50 ± 0.15	K	NIST
Tfus	[168.00; 169.80]	K
Tfus	169.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	169.67	K	ChemSep v8.3 pure component data Compiled value
Tfus	169.60	K	KDB
Tfus	169.27	K	Aq. Solubility Prediction
Tfus	169.64 ± 0.06	K	NIST
Tfus	169.45 ± 0.50	K	NIST
Tfus	169.49 ± 0.20	K	NIST
Tfus	Outlier 168.00 ± 3.00	K	NIST
Tfus	169.80 ± 0.30	K	NIST
Tfus	169.00 ± 1.50	K	NIST
Tfus	169.05 ± 0.20	K	NIST
Tfus	169.10 ± 1.00	K	NIST
Tfus	169.00 ± 0.30	K	NIST
Ttriple	[169.00; 169.68]	K
Ttriple	169.68	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	169.67	K	ChemSep v8.3 pure component data Compiled value
Ttriple	169.66 ± 0.02	K	NIST
Ttriple	169.67 ± 0.05	K	NIST
Ttriple	169.00 ± 0.20	K	NIST
Ttriple	169.66 ± 0.02	K	NIST
Ttriple	169.67 ± 0.05	K	NIST
Ttriple	169.00 ± 0.20	K	NIST
UQi	3.03		ChemSep v8.3 pure component data Compiled value
URi	3.81		ChemSep v8.3 pure component data Compiled value
Vc	[0.291; 0.292]	m3/kmol
Vc	0.292	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.291	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2720000		ChemSep v8.3 pure component data Compiled value
Zra	0.27		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[133.47; 148.53]	J/mol×K	[370.00; 410.00]
Cp,gas	133.47	J/mol×K	370.00	NIST
Cp,gas	141.42	J/mol×K	390.00	NIST
Cp,gas	148.53	J/mol×K	410.00	NIST
Cp,liquid	[145.60; 152.90]	J/mol×K	[293.20; 298.15]
Cp,liquid	145.60	J/mol×K	293.20	NIST
Cp,liquid	152.90	J/mol×K	298.12	NIST
Cp,liquid	148.80	J/mol×K	298.15	NIST
Cp,liquid	148.35	J/mol×K	298.15	NIST
Cp,liquid	149.16	J/mol×K	298.15	NIST
Csat	[116.00; 149.40]	J/mol×K	[170.00; 300.00]
Csat	116.00	J/mol×K	170.00	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	117.50	J/mol×K	180.00	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	119.20	J/mol×K	190.00	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	121.10	J/mol×K	200.00	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	123.20	J/mol×K	210.00	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	125.50	J/mol×K	220.00	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	128.00	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	130.60	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	133.40	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	136.40	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	139.50	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	140.40	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	142.70	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	146.00	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	148.70	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	149.40	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
ΔfusH	[3.28; 4.23]	kJ/mol	[138.70; 169.70]
ΔfusH	4.23	kJ/mol	138.70	NIST
ΔfusH	3.28	kJ/mol	169.70	NIST
ΔfusH	3.28	kJ/mol	169.70	NIST
ΔvapH	[30.46; 33.70]	kJ/mol	[260.50; 356.20]
ΔvapH	32.60	kJ/mol	260.50	NIST
ΔvapH	32.59	kJ/mol	300.00	NIST
ΔvapH	32.70 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	33.10	kJ/mol	313.50	NIST
ΔvapH	33.70	kJ/mol	321.00	NIST
ΔvapH	32.20 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	31.70 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	32.90	kJ/mol	333.00	NIST
ΔvapH	32.60	kJ/mol	334.00	NIST
ΔvapH	32.80	kJ/mol	335.50	NIST
ΔvapH	32.70	kJ/mol	337.00	NIST
ΔvapH	31.20 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	30.70 ± 0.10	kJ/mol	353.00	NIST
ΔvapH	30.46	kJ/mol	356.20	NIST
Pvap	[19.80; 101.80]	kPa	[310.15; 356.35]
Pvap	19.80	kPa	310.15	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	24.94	kPa	315.56	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	27.43	kPa	318.01	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	29.98	kPa	320.26	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	29.70	kPa	320.35	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	32.47	kPa	322.34	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	34.95	kPa	324.31	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	37.52	kPa	326.23	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	39.98	kPa	327.96	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	39.70	kPa	328.05	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	42.45	kPa	329.61	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	45.01	kPa	331.23	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	47.48	kPa	332.73	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	49.60	kPa	334.20	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	50.02	kPa	334.22	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	52.51	kPa	335.62	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	55.02	kPa	336.98	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	57.52	kPa	338.27	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	59.98	kPa	339.52	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	59.60	kPa	339.55	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	62.46	kPa	340.73	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	65.02	kPa	341.94	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	67.51	kPa	343.07	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	69.97	kPa	344.16	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	69.70	kPa	344.25	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	72.51	kPa	345.27	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	74.96	kPa	346.30	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	77.48	kPa	347.33	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	80.02	kPa	348.35	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	79.80	kPa	348.45	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	82.52	kPa	349.31	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	84.99	kPa	350.26	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	87.45	kPa	351.18	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	89.96	kPa	352.09	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	89.80	kPa	352.20	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	92.46	kPa	352.97	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	95.01	kPa	353.85	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	97.52	kPa	354.71	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	101.33	kPa	355.97	Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
Pvap	101.33	kPa	356.15	Vapor Liquid Equilibrium Data for Binary Systems of N,N-Dimethylacetamide with Cyclohexene, Cyclohexane, and Benzene Separately at Atmospheric Pressure
Pvap	101.80	kPa	356.35	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
n0	[1.44378; 1.44378]		[298.15; 298.15]
n0	1.44378		298.15	Experimental data, correlation and prediction of the extraction of benzene from cyclic hydrocarbons using [Epy][ESO4] ionic liquid
n0	1.44378		298.15	Separation of toluene from cyclic hydrocarbons using 1-butyl-3-methylimidazolium methylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
ρl	805.69	kg/m3	298.15	Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
ΔfusS	[19.35; 30.50]	J/mol×K	[138.70; 169.70]
ΔfusS	30.50	J/mol×K	138.70	NIST
ΔfusS	19.35	J/mol×K	169.70	NIST
csound,fluid	[1169.60; 1252.10]	m/s	[303.15; 318.15]
csound,fluid	1252.10	m/s	303.15	Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
csound,fluid	1224.80	m/s	308.15	Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
csound,fluid	1196.60	m/s	313.15	Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
csound,fluid	1169.60	m/s	318.15	Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
λliquid	[0.12; 0.14]	W/m×K	[257.22; 328.22]
λliquid	0.14	W/m×K	257.22	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.14	W/m×K	257.42	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.14	W/m×K	257.57	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	275.37	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	275.58	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	275.73	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	295.57	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	295.77	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	295.92	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	296.28	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	296.49	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	296.65	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	311.67	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	311.89	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	312.04	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	327.85	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	328.07	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	328.22	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[55.72; 322.91]	J/mol×K	[150.00; 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			4.89190e+01
Coefficient B			-6.44330e+02
Coefficient C			6.25224e+00
Coefficient D			-2.75800e-04
Coefficient E			9.07170e-08
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	55.72	J/mol×K	150.00	Calculated Property
Cp,gas	105.17	J/mol×K	300.00	Calculated Property
Cp,gas	160.49	J/mol×K	450.00	Calculated Property
Cp,gas	204.25	J/mol×K	600.00	Calculated Property
Cp,gas	237.08	J/mol×K	750.00	Calculated Property
Cp,gas	261.98	J/mol×K	900.00	Calculated Property
Cp,gas	281.45	J/mol×K	1050.00	Calculated Property
Cp,gas	297.30	J/mol×K	1200.00	Calculated Property
Cp,gas	310.82	J/mol×K	1350.00	Calculated Property
Cp,gas	322.91	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[115.37; 170.56]	J/mol×K	[169.67; 356.12]	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			9.77380e+01
Coefficient B			2.33630e+00
Coefficient C			8.54845e-01
Coefficient D			1.37720e-02
Coefficient E			-1.16530e-05
Temperature range, min.			169.67
Temperature range, max.			356.12
Cp,liquid	115.37	J/mol×K	169.67	Calculated Property
Cp,liquid	119.21	J/mol×K	190.39	Calculated Property
Cp,liquid	123.63	J/mol×K	211.10	Calculated Property
Cp,liquid	128.66	J/mol×K	231.82	Calculated Property
Cp,liquid	134.29	J/mol×K	252.54	Calculated Property
Cp,liquid	140.54	J/mol×K	273.25	Calculated Property
Cp,liquid	147.35	J/mol×K	293.97	Calculated Property
Cp,liquid	154.69	J/mol×K	314.69	Calculated Property
Cp,liquid	162.46	J/mol×K	335.40	Calculated Property
Cp,liquid	170.56	J/mol×K	356.12	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0040160; 0.0001718]	Pa×s	[200.00; 448.34]	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			-1.19010e+01
Coefficient B			1.15930e+03
Coefficient C			1.12280e-01
Coefficient D			-1.96510e-07
Coefficient E			2.00000e+00
Temperature range, min.			200.00
Temperature range, max.			448.34
η	0.0040160	Pa×s	200.00	Calculated Property
η	0.0020132	Pa×s	227.59	Calculated Property
η	0.0011725	Pa×s	255.19	Calculated Property
η	0.0007592	Pa×s	282.78	Calculated Property
η	0.0005311	Pa×s	310.37	Calculated Property
η	0.0003939	Pa×s	337.96	Calculated Property
η	0.0003056	Pa×s	365.56	Calculated Property
η	0.0002456	Pa×s	393.15	Calculated Property
η	0.0002031	Pa×s	420.74	Calculated Property
η	0.0001718	Pa×s	448.34	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[40.16; 0.30]	kJ/mol	[169.67; 560.40]	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			5.79440e+01
Coefficient B			1.58758e+00
Coefficient C			-2.22547e+00
Coefficient D			1.10963e+00
Coefficient E			4.15890e-02
Critical temperature, Tc (K)			5.60420e+02
Temperature range, min.			169.67
Temperature range, max.			560.40
ΔvapH	40.16	kJ/mol	169.67	Calculated Property
ΔvapH	37.60	kJ/mol	213.08	Calculated Property
ΔvapH	35.40	kJ/mol	256.50	Calculated Property
ΔvapH	33.36	kJ/mol	299.91	Calculated Property
ΔvapH	31.28	kJ/mol	343.33	Calculated Property
ΔvapH	28.90	kJ/mol	386.74	Calculated Property
ΔvapH	25.90	kJ/mol	430.16	Calculated Property
ΔvapH	21.79	kJ/mol	473.57	Calculated Property
ΔvapH	15.66	kJ/mol	516.99	Calculated Property
ΔvapH	0.30	kJ/mol	560.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[258.08; 380.72]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41558e+01
Coefficient B			-2.99426e+03
Coefficient C			-4.21740e+01
Temperature range, min.			258.08
Temperature range, max.			380.72
Pvap	1.33	kPa	258.08	Calculated Property
Pvap	3.04	kPa	271.71	Calculated Property
Pvap	6.31	kPa	285.33	Calculated Property
Pvap	12.13	kPa	298.96	Calculated Property
Pvap	21.82	kPa	312.59	Calculated Property
Pvap	37.12	kPa	326.21	Calculated Property
Pvap	60.14	kPa	339.84	Calculated Property
Pvap	93.42	kPa	353.47	Calculated Property
Pvap	139.83	kPa	367.09	Calculated Property
Pvap	202.63	kPa	380.72	Calculated Property
Pvap	[1.19e-04; 4319.17]	kPa	[169.67; 560.40]	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			7.51442e+01
Coefficient B			-6.38870e+03
Coefficient C			-9.10350e+00
Coefficient D			7.13170e-06
Coefficient E			2.00000e+00
Temperature range, min.			169.67
Temperature range, max.			560.40
Pvap	1.19e-04	kPa	169.67	Calculated Property
Pvap	0.04	kPa	213.08	Calculated Property
Pvap	1.23	kPa	256.50	Calculated Property
Pvap	12.96	kPa	299.91	Calculated Property
Pvap	68.32	kPa	343.33	Calculated Property
Pvap	233.97	kPa	386.74	Calculated Property
Pvap	605.98	kPa	430.16	Calculated Property
Pvap	1303.60	kPa	473.57	Calculated Property
Pvap	2474.91	kPa	516.99	Calculated Property
Pvap	4319.17	kPa	560.40	Calculated Property
Pvap	[9.03e-05; 4391.33]	kPa	[169.67; 560.40]	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			8.66975e+01
Coefficient B			-6.84280e+03
Coefficient C			-1.08968e+01
Coefficient D			9.11435e-06
Coefficient E			0.00000e+00
Temperature range, min.			169.67
Temperature range, max.			560.40
Pvap	9.03e-05	kPa	169.67	Calculated Property
Pvap	0.03	kPa	213.08	Calculated Property
Pvap	1.19	kPa	256.50	Calculated Property
Pvap	12.83	kPa	299.91	Calculated Property
Pvap	67.91	kPa	343.33	Calculated Property
Pvap	232.04	kPa	386.74	Calculated Property
Pvap	599.80	kPa	430.16	Calculated Property
Pvap	1293.07	kPa	473.57	Calculated Property
Pvap	2475.87	kPa	516.99	Calculated Property
Pvap	4391.33	kPa	560.40	Calculated Property
Pvap	[19.88; 129.63]	kPa	[310.02; 364.53]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38093e+01
Coefficient B			-2.81353e+03
Coefficient C			-4.99800e+01
Reference			Meyer and Hotz, 1973
Comment			NIST log10(P/bar) coefficients: A=3.9973 ± 0.0018, B=1221.9 ± 1.0, C=-49.98 ± 0.12
Temperature range, min.			310.02
Temperature range, max.			364.53
Pvap	19.88	kPa	310.02	Calculated Property
Pvap	25.43	kPa	316.08	Calculated Property
Pvap	32.18	kPa	322.13	Calculated Property
Pvap	40.30	kPa	328.19	Calculated Property
Pvap	49.99	kPa	334.25	Calculated Property
Pvap	61.45	kPa	340.30	Calculated Property
Pvap	74.91	kPa	346.36	Calculated Property
Pvap	90.60	kPa	352.42	Calculated Property
Pvap	108.75	kPa	358.47	Calculated Property
Pvap	129.63	kPa	364.53	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[915.97; 286.94]	kg/m3	[169.67; 560.40]	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			6.62899e+01
Coefficient B			2.52530e-01
Coefficient C			5.60420e+02
Coefficient D			2.67380e-01
Temperature range, min.			169.67
Temperature range, max.			560.40
ρl	915.97	kg/m3	169.67	Calculated Property
ρl	881.16	kg/m3	213.08	Calculated Property
ρl	844.52	kg/m3	256.50	Calculated Property
ρl	805.60	kg/m3	299.91	Calculated Property
ρl	763.75	kg/m3	343.33	Calculated Property
ρl	717.95	kg/m3	386.74	Calculated Property
ρl	666.42	kg/m3	430.16	Calculated Property
ρl	605.59	kg/m3	473.57	Calculated Property
ρl	525.75	kg/m3	516.99	Calculated Property
ρl	286.94	kg/m3	560.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[169.65; 356.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			6.26362e-02
Coefficient B			-1.22300e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			169.65
Temperature range, max.			356.15
γ	0.04	N/m	169.65	Calculated Property
γ	0.04	N/m	190.37	Calculated Property
γ	0.04	N/m	211.09	Calculated Property
γ	0.03	N/m	231.82	Calculated Property
γ	0.03	N/m	252.54	Calculated Property
γ	0.03	N/m	273.26	Calculated Property
γ	0.03	N/m	293.98	Calculated Property
γ	0.02	N/m	314.71	Calculated Property
γ	0.02	N/m	335.43	Calculated Property
γ	0.02	N/m	356.15	Calculated Property
γ	[0.04; 1.69e-05]	N/m	[169.67; 556.10]	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			-1.12450e-02
Coefficient B			3.11130e+01
Coefficient C			-2.98800e+00
Coefficient D			2.99970e-04
Coefficient E			-5.56540e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 560.4 K.
Temperature range, min.			169.67
Temperature range, max.			556.10
γ	0.04	N/m	169.67	Calculated Property
γ	0.04	N/m	212.61	Calculated Property
γ	0.03	N/m	255.54	Calculated Property
γ	0.03	N/m	298.48	Calculated Property
γ	0.02	N/m	341.42	Calculated Property
γ	0.02	N/m	384.35	Calculated Property
γ	0.01	N/m	427.29	Calculated Property
γ	0.01	N/m	470.23	Calculated Property
γ	0.00	N/m	513.17	Calculated Property
γ	1.69e-05	N/m	556.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.10]	W/m×K	[169.67; 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			9.43360e-05
Coefficient B			1.07830e+00
Coefficient C			5.68300e+02
Coefficient D			3.44710e+04
Temperature range, min.			169.67
Temperature range, max.			1000.00
λgas	0.00	W/m×K	169.67	Calculated Property
λgas	0.01	W/m×K	261.93	Calculated Property
λgas	0.02	W/m×K	354.19	Calculated Property
λgas	0.03	W/m×K	446.45	Calculated Property
λgas	0.04	W/m×K	538.71	Calculated Property
λgas	0.05	W/m×K	630.96	Calculated Property
λgas	0.06	W/m×K	723.22	Calculated Property
λgas	0.07	W/m×K	815.48	Calculated Property
λgas	0.09	W/m×K	907.74	Calculated Property
λgas	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.12]	W/m×K	[169.67; 383.15]	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			1.11740e-01
Coefficient B			8.16810e+02
Coefficient C			-1.43730e+01
Coefficient D			5.59870e-02
Coefficient E			-1.01040e-04
Temperature range, min.			169.67
Temperature range, max.			383.15
λliquid	0.16	W/m×K	169.67	Calculated Property
λliquid	0.16	W/m×K	193.39	Calculated Property
λliquid	0.15	W/m×K	217.11	Calculated Property
λliquid	0.15	W/m×K	240.83	Calculated Property
λliquid	0.14	W/m×K	264.55	Calculated Property
λliquid	0.13	W/m×K	288.27	Calculated Property
λliquid	0.13	W/m×K	311.99	Calculated Property
λliquid	0.12	W/m×K	335.71	Calculated Property
λliquid	0.12	W/m×K	359.43	Calculated Property
λliquid	0.12	W/m×K	383.15	Calculated Property

Similar Compounds

Find more compounds similar to Cyclohexene.

Mixtures

• Acetonitrile + Cyclohexene + Water
• Dimethyl Sulfoxide + Cyclohexene
• 2-Pyrrolidinone, 1-methyl- + Cyclohexene
• Cyclohexene + Cyclohexane
• Pyridine + Cyclohexene
• Benzene + Cyclohexene
• Morpholine + Cyclohexene
• Morpholine + Cyclohexene + Cyclohexane
• Acetic acid, pentyl ester + Cyclohexene
• Ethanol, 2-methoxy- + Cyclohexene
• Carbon dioxide + Cyclohexene
• Diethyl carbonate + Cyclohexene
• Diethyl carbonate + Cyclohexene + Cyclohexane
• Cyclohexanol + Cyclohexene
• Cyclohexanol + Cyclohexene + Water
• 2-Propanol + Cyclohexene + Water
• Ethanol, 2-methoxy- + Cyclohexene + Cyclohexane
• N,N-Dimethylacetamide + Cyclohexene
• Cyclohexanol + Cyclohexene + Isophorone
• Glycerin + Cyclohexene

Find more mixtures with Cyclohexene.

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).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 6. Unsaturated Aliphatic Hydrocarbons. J. Chem. Eng. Data 1996, 41, 645-656.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• 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.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• 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
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
• Isobaric vapor-liquid equilibria for binary and ternary mixtures with cyclohexane, cyclohexene, and morpholine at 100 kPa
• Phase equilibria for benzene-cyclohexene and activity coefficients at infinite dilution for the ternary systems with ionic liquids
• Experimental data, correlation and prediction of the extraction of benzene from cyclic hydrocarbons using [Epy][ESO4] ionic liquid
• Liquid liquid and liquid liquid equilibrium for ternary system water acetonitrile cyclohexene at 298.15 K
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• Separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [EMIM]-based ionic liquids
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Ternary LLE measurements for the separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [DCA]-based ionic liquids
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
• Separation of toluene from cyclic hydrocarbons using 1-butyl-3-methylimidazolium methylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Bis(trifluoromethylsulfonyl)imide, or dicyanamide-based ionic liquids in the liquid liquid extraction of hex-1-ene from hexane and cyclohexene from cyclohexane
• Liquid-liquid separation of hex-1-ene from hexane and cyclohexene from cyclohexane with ionic liquids
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Liquid-liquid separation of hexane/hex-1-ene and cyclohexane/cyclohexene by dicyanamide-based ionic liquids
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Imidazolium and pyridinium-based ionic liquids for the cyclohexane/cyclohexene separation by liquid-liquid extraction
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
• Vapor Liquid Equilibrium Data for Binary Systems of N,N-Dimethylacetamide with Cyclohexene, Cyclohexane, and Benzene Separately at Atmospheric Pressure
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Vapor Liquid Equilibrium Measurements for Carbon Dioxide + Cyclohexene + Squalane at High Pressures Using a Synthetic Method
• Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
• Vapor-Liquid Phase Equilibrium of a Cyclohexene + Water + Cyclohexanol + Isophorone Quaternary System at 500 kPa
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Partition Coefficients of Organic Solutes between Supercritical Carbon Dioxide and Water: Experimental Measurements and Empirical Correlations
• Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
• VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
• 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
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Physical Properties (Density, Viscosity, Surface Tension, Interfacial Tension, and Contact Angle) of the System Isopropyl Alcohol + Cyclohexene + Water
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and Methyl Isobutyl Ketone at 100 kPa
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
• Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
• Liquid-Liquid Equilibrium for the System Water + Cyclohexene + Cyclohexanol over the Temperature Range of (303.2 to 403.2) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• 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

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.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.