Chemical Properties of Cyclohexane, 1,3-dimethyl-, cis- (CAS 638-04-0)

InChI

InChI=1S/C8H16/c1-7-4-3-5-8(2)6-7/h7-8H,3-6H2,1-2H3/t7-,8+

InChI Key

SGVUHPSBDNVHKL-OCAPTIKFSA-N

Formula

C8H16

SMILES

CC1CCCC(C)C1

Molecular Weight¹

112.21

CAS

638-04-0

Other Names

• 1,3-Dimethylcyclohexane, cis-
• 1,3-dimethyl(cis)-cyclohexane
• 1,cis-3-Dimethylcyclohexane
• Cyclohexane, cis-1,3-dimethyl-
• NSC 74159
• c-1,3-Dimethylcyclohexane
• cis-1,3-Dimethylcyclohexane

• ω : Acentric Factor.
• AP : Aniline Point (K).
• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (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).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : 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).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ : Gas thermal conductivity (W/m×K).
• λ : 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	[0.2240; 0.2414]
ω	0.2414		ChemSep v8.3 pure component data Compiled value
ω	0.2240		KDB
AP	324.850	K	KDB
ΔcH°liquid	-5211.80 ± 1.70	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[29.83; 29.85]	kJ/mol
ΔfG°	29.83	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	29.85	kJ/mol	KDB
Δc,grossH	5211.80	kJ/mol	KDB
Δc,netH	4859.716	kJ/mol	KDB
ΔfH°gas	[-184.90; -184.76]	kJ/mol
ΔfH°gas	-184.76	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-184.90	kJ/mol	KDB
ΔfusH°	9.38	kJ/mol	Joback Calculated Property
ΔvapH°	[38.10; 38.31]	kJ/mol
ΔvapH°	38.31	kJ/mol	NIST
ΔvapH°	38.10	kJ/mol	NIST
ΔvapH°	38.20	kJ/mol	NIST
ΔvapH°	38.20 ± 0.10	kJ/mol	NIST
ΔvapH°	38.22	kJ/mol	NIST
IE	9.98 ± 0.05	eV	NIST
log10WS	-4.58		Relay (1.0) Calculated Property
logPoct/wat	2.833		Crippen Calculated Property
McVol	112.720	ml/mol	McGowan Calculated Property
Pc	[2900.00; 2938.43]	kPa
Pc	2938.43	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2900.00	kPa	KDB
Ptriple	5.63e-04	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[764.00; 804.00]
Inp	Outlier 764.00		NIST
Inp	778.40		NIST
Inp	778.50		NIST
Inp	778.60		NIST
Inp	778.10		NIST
Inp	774.90		NIST
Inp	780.30		NIST
Inp	785.00		NIST
Inp	789.80		NIST
Inp	772.00		NIST
Inp	777.00		NIST
Inp	782.00		NIST
Inp	788.00		NIST
Inp	784.70		NIST
Inp	784.70		NIST
Inp	789.60		NIST
Inp	773.30		NIST
Inp	775.50		NIST
Inp	777.90		NIST
Inp	780.20		NIST
Inp	785.10		NIST
Inp	770.00		NIST
Inp	772.00		NIST
Inp	774.00		NIST
Inp	777.00		NIST
Inp	780.00		NIST
Inp	782.00		NIST
Inp	778.40		NIST
Inp	778.60		NIST
Inp	Outlier 804.00		NIST
Inp	784.90		NIST
Inp	789.70		NIST
Inp	789.70		NIST
Inp	790.10		NIST
Inp	790.80		NIST
Inp	790.80		NIST
Inp	785.00		NIST
Inp	790.00		NIST
Inp	785.00		NIST
Inp	788.00		NIST
Inp	789.00		NIST
Inp	792.00		NIST
Inp	795.00		NIST
Inp	785.00		NIST
Inp	785.00		NIST
Inp	Outlier 798.00		NIST
Inp	783.00		NIST
Inp	789.00		NIST
Inp	770.00		NIST
Inp	Outlier 798.00		NIST
Inp	769.80		NIST
Inp	778.00		NIST
Inp	776.60		NIST
Inp	772.80		NIST
Inp	774.70		NIST
Inp	776.60		NIST
Inp	783.30		NIST
Inp	775.00		NIST
Inp	772.80		NIST
Inp	774.70		NIST
Inp	776.60		NIST
Inp	770.23		NIST
Inp	771.54		NIST
Inp	771.77		NIST
Inp	772.00		NIST
Inp	767.70		NIST
Inp	770.50		NIST
Inp	772.28		NIST
Inp	771.53		NIST
Inp	774.44		NIST
Inp	776.29		NIST
Inp	770.00		NIST
Inp	785.32		NIST
Inp	790.00		NIST
Inp	778.00		NIST
Inp	773.00		NIST
Inp	778.00		NIST
Inp	773.00		NIST
Inp	773.00		NIST
Inp	784.40		NIST
Inp	786.00		NIST
Inp	788.50		NIST
Inp	790.50		NIST
Inp	792.20		NIST
Inp	793.70		NIST
Inp	785.00		NIST
Inp	Outlier 764.00		NIST
Inp	785.32		NIST
Inp	790.00		NIST
Inp	769.80		NIST
Inp	770.00		NIST
Inp	785.00		NIST
I	[810.00; 810.00]
I	810.00		NIST
I	810.00		NIST
S°gas	371.20	J/mol×K	NIST
S°liquid	272.63	J/mol×K	NIST
Tboil	[392.15; 398.10]	K
Tboil	393.24	K	ChemSep v8.3 pure component data Compiled value
Tboil	393.30	K	KDB
Tboil	393.20	K	NIST
Tboil	393.30	K	NIST
Tboil	393.50 ± 0.30	K	NIST
Tboil	393.70 ± 0.50	K	NIST
Tboil	393.00 ± 2.00	K	NIST
Tboil	393.56 ± 0.30	K	NIST
Tboil	393.20 ± 1.00	K	NIST
Tboil	392.15 ± 0.50	K	NIST
Tboil	393.65 ± 0.50	K	NIST
Tboil	393.85 ± 0.60	K	NIST
Tboil	393.15 ± 0.10	K	NIST
Tboil	394.15 ± 0.60	K	NIST
Tboil	393.75 ± 0.50	K	NIST
Tboil	393.23 ± 0.02	K	NIST
Tboil	393.45 ± 0.30	K	NIST
Tboil	393.24 ± 0.20	K	NIST
Tboil	Outlier 397.85 ± 0.30	K	NIST
Tboil	392.65 ± 0.50	K	NIST
Tboil	392.70 ± 2.00	K	NIST
Tboil	392.65 ± 0.50	K	NIST
Tboil	Outlier 398.10 ± 2.00	K	NIST
Tboil	393.15 ± 0.70	K	NIST
Tboil	393.55 ± 0.30	K	NIST
Tboil	394.70 ± 2.00	K	NIST
Tc	[586.10; 591.15]	K
Tc	586.10	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	591.15	K	ChemSep v8.3 pure component data Compiled value
Tc	591.00	K	KDB
Tc	591.00	K	NIST
Tfus	[177.95; 197.61]	K
Tfus	197.61	K	ChemSep v8.3 pure component data Compiled value
Tfus	197.60	K	KDB
Tfus	196.09 ± 0.02	K	NIST
Tfus	177.95 ± 0.20	K	NIST
Tfus	194.15 ± 3.00	K	NIST
Ttriple	[197.58; 197.59]	K
Ttriple	197.58	K	ChemSep v8.3 pure component data Compiled value
Ttriple	197.59 ± 0.02	K	NIST
Ttriple	197.58 ± 0.05	K	NIST
Ttriple	197.59 ± 0.03	K	NIST
Ttriple	197.59 ± 0.02	K	NIST
UQi	4.31		ChemSep v8.3 pure component data Compiled value
URi	5.39		ChemSep v8.3 pure component data Compiled value
Vc	[0.449; 0.450]	m3/kmol
Vc	0.450	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.449	m3/kmol	KDB
Zc	[0.2649250; 0.2690000]
Zc	0.2690000		ChemSep v8.3 pure component data Compiled value
Zc	0.2649250		KDB
Zra	0.27		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[173.40; 210.30]	J/mol×K	[210.00; 300.00]
Cp,liquid	173.40	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
Cp,liquid	176.80	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
Cp,liquid	180.30	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
Cp,liquid	184.10	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
Cp,liquid	188.00	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
Cp,liquid	192.10	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
Cp,liquid	196.40	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
Cp,liquid	197.70	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
Cp,liquid	200.80	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
Cp,liquid	205.50	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
Cp,liquid	209.40	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
Cp,liquid	209.37	J/mol×K	298.15	NIST
Cp,liquid	210.30	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	[10.82; 10.82]	kJ/mol	[197.59; 197.60]
ΔfusH	10.82	kJ/mol	197.59	NIST
ΔfusH	10.82	kJ/mol	197.59	NIST
ΔfusH	10.82	kJ/mol	197.60	NIST
ΔfusH	10.82	kJ/mol	197.60	NIST
ΔvapH	[32.80; 37.70]	kJ/mol	[357.00; 393.30]
ΔvapH	36.80	kJ/mol	357.00	NIST
ΔvapH	37.70	kJ/mol	357.00	NIST
ΔvapH	34.90 ± 0.10	kJ/mol	363.00	NIST
ΔvapH	33.30 ± 0.10	kJ/mol	385.00	NIST
ΔvapH	32.80	kJ/mol	393.30	KDB
ΔvapH	32.91	kJ/mol	393.30	NIST
n0	1.42063		298.15	KDB
ρl	766.00	kg/m3	293.00	KDB
ΔfusS	[54.77; 54.77]	J/mol×K	[197.59; 197.59]
ΔfusS	54.77	J/mol×K	197.59	NIST
ΔfusS	54.77	J/mol×K	197.59	NIST
γ	0.02	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[115.87; 496.11]	J/mol×K	[200.00; 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			1.00690e+02
Coefficient B			-8.36690e+02
Coefficient C			7.00024e+00
Coefficient D			-5.12060e-04
Coefficient E			1.35820e-07
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	115.87	J/mol×K	200.00	Calculated Property
Cp,gas	183.03	J/mol×K	344.44	Calculated Property
Cp,gas	260.02	J/mol×K	488.89	Calculated Property
Cp,gas	324.17	J/mol×K	633.33	Calculated Property
Cp,gas	373.40	J/mol×K	777.78	Calculated Property
Cp,gas	410.60	J/mol×K	922.22	Calculated Property
Cp,gas	439.07	J/mol×K	1066.67	Calculated Property
Cp,gas	461.54	J/mol×K	1211.11	Calculated Property
Cp,gas	480.04	J/mol×K	1355.56	Calculated Property
Cp,gas	496.11	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[169.53; 263.99]	J/mol×K	[197.58; 393.24]	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			9.16380e+01
Coefficient B			6.75100e+01
Coefficient C			2.77354e+00
Coefficient D			6.95350e-03
Coefficient E			-3.42780e-06
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			197.58
Temperature range, max.			393.24
Cp,liquid	169.53	J/mol×K	197.58	Calculated Property
Cp,liquid	176.54	J/mol×K	219.32	Calculated Property
Cp,liquid	184.45	J/mol×K	241.06	Calculated Property
Cp,liquid	193.24	J/mol×K	262.80	Calculated Property
Cp,liquid	202.89	J/mol×K	284.54	Calculated Property
Cp,liquid	213.41	J/mol×K	306.28	Calculated Property
Cp,liquid	224.78	J/mol×K	328.02	Calculated Property
Cp,liquid	237.01	J/mol×K	349.76	Calculated Property
Cp,liquid	250.08	J/mol×K	371.50	Calculated Property
Cp,liquid	263.99	J/mol×K	393.24	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0055586; 0.0002965]	Pa×s	[197.58; 393.24]	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			-1.90680e+01
Coefficient B			1.35830e+03
Coefficient C			1.35260e+00
Coefficient D			-3.82020e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			197.58
Temperature range, max.			393.24
η	0.0055586	Pa×s	197.58	Calculated Property
η	0.0031282	Pa×s	219.32	Calculated Property
η	0.0019572	Pa×s	241.06	Calculated Property
η	0.0013236	Pa×s	262.80	Calculated Property
η	0.0009489	Pa×s	284.54	Calculated Property
η	0.0007112	Pa×s	306.28	Calculated Property
η	0.0005517	Pa×s	328.02	Calculated Property
η	0.0004398	Pa×s	349.76	Calculated Property
η	0.0003580	Pa×s	371.50	Calculated Property
η	0.0002965	Pa×s	393.24	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[43.98; 0.00]	kJ/mol	[197.58; 591.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			6.83450e+01
Coefficient B			2.09840e+00
Coefficient C			-4.31870e+00
Coefficient D			4.40540e+00
Coefficient E			-1.70470e+00
Critical temperature, Tc (K)			5.91150e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			197.58
Temperature range, max.			591.15
ΔvapH	43.98	kJ/mol	197.58	Calculated Property
ΔvapH	41.44	kJ/mol	241.31	Calculated Property
ΔvapH	39.08	kJ/mol	285.04	Calculated Property
ΔvapH	36.69	kJ/mol	328.77	Calculated Property
ΔvapH	34.08	kJ/mol	372.50	Calculated Property
ΔvapH	31.10	kJ/mol	416.23	Calculated Property
ΔvapH	27.61	kJ/mol	459.96	Calculated Property
ΔvapH	23.33	kJ/mol	503.69	Calculated Property
ΔvapH	17.50	kJ/mol	547.42	Calculated Property
ΔvapH	0.00	kJ/mol	591.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[283.11; 420.90]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38755e+01
Coefficient B			-3.19163e+03
Coefficient C			-4.82270e+01
Temperature range, min.			283.11
Temperature range, max.			420.90
Pvap	1.33	kPa	283.11	Calculated Property
Pvap	3.06	kPa	298.42	Calculated Property
Pvap	6.39	kPa	313.73	Calculated Property
Pvap	12.30	kPa	329.04	Calculated Property
Pvap	22.14	kPa	344.35	Calculated Property
Pvap	37.61	kPa	359.66	Calculated Property
Pvap	60.80	kPa	374.97	Calculated Property
Pvap	94.13	kPa	390.28	Calculated Property
Pvap	140.40	kPa	405.59	Calculated Property
Pvap	202.63	kPa	420.90	Calculated Property
Pvap	[5.53e-04; 2939.75]	kPa	[197.58; 591.15]	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			7.33962e+01
Coefficient B			-6.95290e+03
Coefficient C			-8.68380e+00
Coefficient D			5.07100e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			197.58
Temperature range, max.			591.15
Pvap	5.53e-04	kPa	197.58	Calculated Property
Pvap	0.06	kPa	241.31	Calculated Property
Pvap	1.39	kPa	285.04	Calculated Property
Pvap	11.83	kPa	328.77	Calculated Property
Pvap	55.94	kPa	372.50	Calculated Property
Pvap	180.59	kPa	416.23	Calculated Property
Pvap	450.87	kPa	459.96	Calculated Property
Pvap	942.55	kPa	503.69	Calculated Property
Pvap	1739.60	kPa	547.42	Calculated Property
Pvap	2939.75	kPa	591.15	Calculated Property
Pvap	[5.63e-04; 2938.63]	kPa	[197.58; 591.15]	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			7.27551e+01
Coefficient B			-6.92278e+03
Coefficient C			-8.58765e+00
Coefficient D			5.00269e-06
Coefficient E			0.00000e+00
Temperature range, min.			197.58
Temperature range, max.			591.15
Pvap	5.63e-04	kPa	197.58	Calculated Property
Pvap	0.06	kPa	241.31	Calculated Property
Pvap	1.39	kPa	285.04	Calculated Property
Pvap	11.83	kPa	328.77	Calculated Property
Pvap	55.91	kPa	372.50	Calculated Property
Pvap	180.47	kPa	416.23	Calculated Property
Pvap	450.62	kPa	459.96	Calculated Property
Pvap	942.18	kPa	503.69	Calculated Property
Pvap	1739.08	kPa	547.42	Calculated Property
Pvap	2938.63	kPa	591.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[839.83; 247.74]	kg/m3	[197.58; 591.15]	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			6.30029e+01
Coefficient B			2.54310e-01
Coefficient C			5.91150e+02
Coefficient D			2.81960e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			197.58
Temperature range, max.			591.15
ρl	839.83	kg/m3	197.58	Calculated Property
ρl	807.00	kg/m3	241.31	Calculated Property
ρl	772.54	kg/m3	285.04	Calculated Property
ρl	736.06	kg/m3	328.77	Calculated Property
ρl	696.98	kg/m3	372.50	Calculated Property
ρl	654.37	kg/m3	416.23	Calculated Property
ρl	606.68	kg/m3	459.96	Calculated Property
ρl	550.73	kg/m3	503.69	Calculated Property
ρl	477.91	kg/m3	547.42	Calculated Property
ρl	247.74	kg/m3	591.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 2.11e-06]	N/m	[197.58; 587.61]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-8.18160e-03
Coefficient B			5.87390e+01
Coefficient C			-3.50090e+00
Coefficient D			1.25720e-03
Coefficient E			-6.20770e-06
Comment			ChemSep eq 16, SurfaceTension, ChemSep Tmax 591.15 K
Temperature range, min.			197.58
Temperature range, max.			587.61
γ	0.03	N/m	197.58	Calculated Property
γ	0.03	N/m	240.92	Calculated Property
γ	0.02	N/m	284.25	Calculated Property
γ	0.02	N/m	327.59	Calculated Property
γ	0.02	N/m	370.93	Calculated Property
γ	0.01	N/m	414.26	Calculated Property
γ	0.01	N/m	457.60	Calculated Property
γ	0.01	N/m	500.94	Calculated Property
γ	0.00	N/m	544.27	Calculated Property
γ	2.11e-06	N/m	587.61	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.00; 0.09]	W/m×K	[197.58; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K
Coefficient A			1.51950e-02
Coefficient B			3.52060e-01
Coefficient C			-4.61670e+01
Coefficient D			8.70770e+05
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			197.58
Temperature range, max.			1000.00
λ	0.00	W/m×K	197.58	Calculated Property
λ	0.01	W/m×K	286.74	Calculated Property
λ	0.02	W/m×K	375.90	Calculated Property
λ	0.03	W/m×K	465.05	Calculated Property
λ	0.04	W/m×K	554.21	Calculated Property
λ	0.05	W/m×K	643.37	Calculated Property
λ	0.06	W/m×K	732.53	Calculated Property
λ	0.07	W/m×K	821.68	Calculated Property
λ	0.08	W/m×K	910.84	Calculated Property
λ	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ	[0.13; 0.09]	W/m×K	[197.58; 393.24]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K
Coefficient A			-4.19800e-02
Coefficient B			-3.86820e+00
Coefficient C			-1.52840e+00
Coefficient D			-7.40680e-04
Coefficient E			-1.10560e-06
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			197.58
Temperature range, max.			393.24
λ	0.13	W/m×K	197.58	Calculated Property
λ	0.13	W/m×K	219.32	Calculated Property
λ	0.13	W/m×K	241.06	Calculated Property
λ	0.12	W/m×K	262.80	Calculated Property
λ	0.12	W/m×K	284.54	Calculated Property
λ	0.11	W/m×K	306.28	Calculated Property
λ	0.11	W/m×K	328.02	Calculated Property
λ	0.10	W/m×K	349.76	Calculated Property
λ	0.10	W/m×K	371.50	Calculated Property
λ	0.09	W/m×K	393.24	Calculated Property

Similar Compounds

Find more compounds similar to Cyclohexane, 1,3-dimethyl-, cis-.

Sources

• KDB Vapor Pressure Data
• 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
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• 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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