Chemical Properties of Cyclohexane, 1,2-dimethyl-, cis- (CAS 2207-01-4)

InChI

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

InChI Key

KVZJLSYJROEPSQ-OCAPTIKFSA-N

Formula

C8H16

SMILES

CC1CCCCC1C

Molecular Weight¹

112.21

CAS

2207-01-4

Other Names

• 1,2-Dimethylcyclohexane, cis
• 1,2-cis-DimethyIcyclohexane
• 1,2-cis-dimethylcyclohexane
• 1,cis-2-dimethylcyclohexane
• c-1,2-Dimethylcyclohexane
• cis-1,2-dimethylcyclohexane
• cyclohexane, 1,cis-2-dimethyl-

• 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.
• S°_gas : 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	[0.2323; 0.2363]
ω	0.2323		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2363		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2363		ChemSep v8.3 pure component data Compiled value
ω	0.2360		KDB
AP	314.850	K	KDB
ΔcH°liquid	-5222.00 ± 1.80	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[41.21; 41.24]	kJ/mol
ΔfG°	41.21	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	41.24	kJ/mol	KDB
Δc,grossH	5222.93	kJ/mol	KDB
Δc,netH	4870.846	kJ/mol	KDB
ΔfH°gas	[-172.30; -172.17]	kJ/mol
ΔfH°gas	-172.17	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-172.30	kJ/mol	KDB
ΔfusH°	9.38	kJ/mol	Joback Calculated Property
ΔvapH°	[39.40; 39.74]	kJ/mol
ΔvapH°	39.74	kJ/mol	NIST
ΔvapH°	39.40	kJ/mol	NIST
ΔvapH°	39.70	kJ/mol	NIST
ΔvapH°	39.70 ± 0.10	kJ/mol	NIST
ΔvapH°	39.71	kJ/mol	NIST
IE	[9.78; 10.08]	eV
IE	9.78 ± 0.05	eV	NIST
IE	9.90 ± 0.07	eV	NIST
IE	10.08 ± 0.02	eV	NIST
log10WS	-4.30		Estimated Solubility
logPoct/wat	2.833		Crippen Calculated Property
McVol	112.720	ml/mol	McGowan Calculated Property
Pc	[2938.43; 2964.75]	kPa
Pc	2938.43	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2964.75	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2938.43	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2940.00	kPa	KDB
Ptriple	6.41e-03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[810.00; 850.00]
Inp	837.60		NIST
Inp	843.90		NIST
Inp	826.60		NIST
Inp	826.80		NIST
Inp	826.90		NIST
Inp	827.10		NIST
Inp	826.70		NIST
Inp	822.20		NIST
Inp	828.80		NIST
Inp	840.00		NIST
Inp	828.40		NIST
Inp	828.40		NIST
Inp	832.40		NIST
Inp	829.00		NIST
Inp	826.60		NIST
Inp	827.10		NIST
Inp	834.00		NIST
Inp	844.00		NIST
Inp	829.10		NIST
Inp	834.70		NIST
Inp	840.20		NIST
Inp	834.10		NIST
Inp	835.10		NIST
Inp	839.10		NIST
Inp	836.20		NIST
Inp	829.00		NIST
Inp	835.00		NIST
Inp	826.00		NIST
Inp	831.00		NIST
Inp	833.00		NIST
Inp	836.00		NIST
Inp	840.00		NIST
Inp	830.00		NIST
Inp	826.00		NIST
Inp	Outlier 850.00		NIST
Inp	831.00		NIST
Inp	836.00		NIST
Inp	Outlier 850.00		NIST
Inp	820.00		NIST
Inp	Outlier 850.00		NIST
Inp	826.60		NIST
Inp	820.00		NIST
Inp	827.20		NIST
Inp	824.70		NIST
Inp	824.40		NIST
Inp	823.10		NIST
Inp	824.70		NIST
Inp	827.30		NIST
Inp	834.90		NIST
Inp	825.00		NIST
Inp	823.10		NIST
Inp	824.70		NIST
Inp	827.30		NIST
Inp	824.70		NIST
Inp	824.40		NIST
Inp	818.20		NIST
Inp	822.00		NIST
Inp	820.00		NIST
Inp	836.00		NIST
Inp	844.00		NIST
Inp	826.00		NIST
Inp	835.00		NIST
Inp	827.00		NIST
Inp	823.00		NIST
Inp	829.00		NIST
Inp	829.90		NIST
Inp	832.50		NIST
Inp	836.30		NIST
Inp	839.10		NIST
Inp	841.50		NIST
Inp	843.50		NIST
Inp	829.00		NIST
Inp	832.00		NIST
Inp	836.00		NIST
Inp	838.00		NIST
Inp	841.00		NIST
Inp	843.00		NIST
Inp	Outlier 810.00		NIST
Inp	829.00		NIST
Inp	828.00		NIST
Inp	836.00		NIST
Inp	836.00		NIST
S°gas	374.34	J/mol×K	NIST
Tboil	[394.00; 403.40]	K
Tboil	402.94	K	ChemSep v8.3 pure component data Compiled value
Tboil	402.90	K	KDB
Tboil	402.90	K	NIST
Tboil	402.90	K	NIST
Tboil	403.00 ± 2.00	K	NIST
Tboil	403.00 ± 2.00	K	NIST
Tboil	Outlier 398.00 ± 8.00	K	NIST
Tboil	403.00 ± 2.00	K	NIST
Tboil	402.70 ± 0.30	K	NIST
Tboil	402.88 ± 0.15	K	NIST
Tboil	402.87 ± 0.20	K	NIST
Tboil	Outlier 394.00 ± 8.00	K	NIST
Tboil	402.70 ± 2.00	K	NIST
Tboil	402.70 ± 2.00	K	NIST
Tboil	402.15 ± 0.40	K	NIST
Tboil	402.85 ± 0.50	K	NIST
Tboil	402.99 ± 0.25	K	NIST
Tboil	402.80 ± 0.15	K	NIST
Tboil	402.99 ± 0.30	K	NIST
Tboil	402.99 ± 0.30	K	NIST
Tboil	402.87 ± 0.01	K	NIST
Tboil	403.25 ± 0.30	K	NIST
Tboil	401.15 ± 1.00	K	NIST
Tboil	403.19 ± 0.50	K	NIST
Tboil	403.40 ± 0.50	K	NIST
Tboil	403.19 ± 0.50	K	NIST
Tboil	400.80 ± 3.00	K	NIST
Tboil	403.33 ± 0.20	K	NIST
Tboil	399.70 ± 2.00	K	NIST
Tc	[605.93; 607.29]	K
Tc	Outlier 607.29	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	606.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	605.93	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	606.15	K	ChemSep v8.3 pure component data Compiled value
Tc	606.00	K	KDB
Tc	606.00	K	NIST
Tfus	[213.35; 223.16]	K
Tfus	223.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	223.16	K	ChemSep v8.3 pure component data Compiled value
Tfus	223.10	K	KDB
Tfus	222.97 ± 0.50	K	NIST
Tfus	223.15 ± 0.07	K	NIST
Tfus	222.97 ± 0.20	K	NIST
Tfus	222.93 ± 0.01	K	NIST
Tfus	Outlier 213.35 ± 0.50	K	NIST
Tfus	222.95 ± 0.30	K	NIST
Ttriple	[223.16; 223.29]	K
Ttriple	223.29	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	223.16	K	ChemSep v8.3 pure component data Compiled value
Ttriple	223.28 ± 0.01	K	NIST
Ttriple	223.27 ± 0.05	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	[0.422; 0.471]	m3/kmol
Vc	0.422	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.460	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.471	m3/kmol	KDB
Zc	[0.2680000; 0.2750020]
Zc	0.2680000		ChemSep v8.3 pure component data Compiled value
Zc	0.2750020		KDB
Zra	0.27		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[182.60; 211.10]	J/mol×K	[230.00; 300.00]
Cp,liquid	182.60	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	186.10	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	189.90	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	193.70	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	197.80	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	199.10	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	202.10	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	206.50	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	210.20	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
Cp,liquid	211.10	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
ΔfusH	1.64	kJ/mol	223.30	NIST
ΔvapH	[33.47; 38.00]	kJ/mol	[363.50; 402.90]
ΔvapH	38.00	kJ/mol	363.50	NIST
ΔvapH	35.50 ± 0.10	kJ/mol	370.00	NIST
ΔvapH	34.50 ± 0.10	kJ/mol	387.00	NIST
ΔvapH	33.64	kJ/mol	402.90	KDB
ΔvapH	33.47	kJ/mol	402.90	NIST
n0	1.43358		298.15	KDB
ρl	796.00	kg/m3	293.00	KDB
γ	0.03	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[114.65; 493.66]	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			9.92100e+01
Coefficient B			-8.35350e+02
Coefficient C			7.01724e+00
Coefficient D			-5.47540e-04
Coefficient E			1.50430e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	114.65	J/mol×K	200.00	Calculated Property
Cp,gas	182.41	J/mol×K	344.44	Calculated Property
Cp,gas	259.48	J/mol×K	488.89	Calculated Property
Cp,gas	323.25	J/mol×K	633.33	Calculated Property
Cp,gas	371.91	J/mol×K	777.78	Calculated Property
Cp,gas	408.55	J/mol×K	922.22	Calculated Property
Cp,gas	436.59	J/mol×K	1066.67	Calculated Property
Cp,gas	458.82	J/mol×K	1211.11	Calculated Property
Cp,gas	477.33	J/mol×K	1355.56	Calculated Property
Cp,gas	493.66	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[180.28; 268.69]	J/mol×K	[223.16; 402.94]	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			1.11710e+02
Coefficient B			5.26250e+01
Coefficient C			2.46514e+00
Coefficient D			7.75530e-03
Coefficient E			-4.09320e-06
Temperature range, min.			223.16
Temperature range, max.			402.94
Cp,liquid	180.28	J/mol×K	223.16	Calculated Property
Cp,liquid	187.29	J/mol×K	243.14	Calculated Property
Cp,liquid	195.00	J/mol×K	263.11	Calculated Property
Cp,liquid	203.40	J/mol×K	283.09	Calculated Property
Cp,liquid	212.51	J/mol×K	303.06	Calculated Property
Cp,liquid	222.34	J/mol×K	323.04	Calculated Property
Cp,liquid	232.87	J/mol×K	343.01	Calculated Property
Cp,liquid	244.12	J/mol×K	362.99	Calculated Property
Cp,liquid	256.06	J/mol×K	382.96	Calculated Property
Cp,liquid	268.69	J/mol×K	402.94	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0053086; 0.0001659]	Pa×s	[223.16; 472.00]	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			-1.23120e+01
Coefficient B			1.46530e+03
Coefficient C			9.79550e-02
Coefficient D			-4.47920e-07
Coefficient E			2.00000e+00
Temperature range, min.			223.16
Temperature range, max.			472.00
η	0.0053086	Pa×s	223.16	Calculated Property
η	0.0025884	Pa×s	250.81	Calculated Property
η	0.0014545	Pa×s	278.46	Calculated Property
η	0.0009061	Pa×s	306.11	Calculated Property
η	0.0006098	Pa×s	333.76	Calculated Property
η	0.0004355	Pa×s	361.40	Calculated Property
η	0.0003258	Pa×s	389.05	Calculated Property
η	0.0002529	Pa×s	416.70	Calculated Property
η	0.0002023	Pa×s	444.35	Calculated Property
η	0.0001659	Pa×s	472.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[43.76; 0.00]	kJ/mol	[223.16; 606.15]	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			6.62470e+01
Coefficient B			1.82400e+00
Coefficient C			-3.74400e+00
Coefficient D			3.95020e+00
Coefficient E			-1.56330e+00
Critical temperature, Tc (K)			6.06150e+02
Temperature range, min.			223.16
Temperature range, max.			606.15
ΔvapH	43.76	kJ/mol	223.16	Calculated Property
ΔvapH	41.51	kJ/mol	265.71	Calculated Property
ΔvapH	39.27	kJ/mol	308.27	Calculated Property
ΔvapH	36.89	kJ/mol	350.82	Calculated Property
ΔvapH	34.23	kJ/mol	393.38	Calculated Property
ΔvapH	31.19	kJ/mol	435.93	Calculated Property
ΔvapH	27.64	kJ/mol	478.49	Calculated Property
ΔvapH	23.33	kJ/mol	521.04	Calculated Property
ΔvapH	17.49	kJ/mol	563.60	Calculated Property
ΔvapH	0.00	kJ/mol	606.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[290.58; 431.66]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37858e+01
Coefficient B			-3.21239e+03
Coefficient C			-5.25890e+01
Temperature range, min.			290.58
Temperature range, max.			431.66
Pvap	1.33	kPa	290.58	Calculated Property
Pvap	3.07	kPa	306.26	Calculated Property
Pvap	6.42	kPa	321.93	Calculated Property
Pvap	12.37	kPa	337.61	Calculated Property
Pvap	22.25	kPa	353.28	Calculated Property
Pvap	37.78	kPa	368.96	Calculated Property
Pvap	61.02	kPa	384.63	Calculated Property
Pvap	94.39	kPa	400.31	Calculated Property
Pvap	140.60	kPa	415.98	Calculated Property
Pvap	202.65	kPa	431.66	Calculated Property
Pvap	[6.32e-03; 2939.89]	kPa	[223.16; 606.15]	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			7.27672e+01
Coefficient B			-7.11060e+03
Coefficient C			-8.54220e+00
Coefficient D			4.57410e-06
Coefficient E			2.00000e+00
Temperature range, min.			223.16
Temperature range, max.			606.15
Pvap	6.32e-03	kPa	223.16	Calculated Property
Pvap	0.26	kPa	265.71	Calculated Property
Pvap	3.26	kPa	308.27	Calculated Property
Pvap	20.13	kPa	350.82	Calculated Property
Pvap	78.38	kPa	393.38	Calculated Property
Pvap	223.66	kPa	435.93	Calculated Property
Pvap	514.47	kPa	478.49	Calculated Property
Pvap	1015.96	kPa	521.04	Calculated Property
Pvap	1798.12	kPa	563.60	Calculated Property
Pvap	2939.89	kPa	606.15	Calculated Property
Pvap	[6.40e-03; 2931.71]	kPa	[223.16; 606.15]	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			7.35050e+01
Coefficient B			-7.12649e+03
Coefficient C			-8.66492e+00
Coefficient D			4.76986e-06
Coefficient E			0.00000e+00
Temperature range, min.			223.16
Temperature range, max.			606.15
Pvap	6.40e-03	kPa	223.16	Calculated Property
Pvap	0.26	kPa	265.71	Calculated Property
Pvap	3.26	kPa	308.27	Calculated Property
Pvap	20.08	kPa	350.82	Calculated Property
Pvap	77.95	kPa	393.38	Calculated Property
Pvap	222.04	kPa	435.93	Calculated Property
Pvap	510.44	kPa	478.49	Calculated Property
Pvap	1008.59	kPa	521.04	Calculated Property
Pvap	1788.12	kPa	563.60	Calculated Property
Pvap	2931.71	kPa	606.15	Calculated Property
Pvap	[6.35; 103.90]	kPa	[322.33; 403.83]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37385e+01
Coefficient B			-3.15345e+03
Coefficient C			-5.71100e+01
Reference			Williamham, Taylor, et al., 1945
Temperature range, min.			322.33
Temperature range, max.			403.83
Pvap	6.35	kPa	322.33	Calculated Property
Pvap	9.40	kPa	331.39	Calculated Property
Pvap	13.58	kPa	340.44	Calculated Property
Pvap	19.17	kPa	349.50	Calculated Property
Pvap	26.50	kPa	358.55	Calculated Property
Pvap	35.96	kPa	367.61	Calculated Property
Pvap	47.95	kPa	376.66	Calculated Property
Pvap	62.94	kPa	385.72	Calculated Property
Pvap	81.41	kPa	394.77	Calculated Property
Pvap	103.90	kPa	403.83	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[850.13; 241.65]	kg/m3	[223.16; 606.15]	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			5.83539e+01
Coefficient B			2.41480e-01
Coefficient C			6.06150e+02
Coefficient D			2.65500e-01
Temperature range, min.			223.16
Temperature range, max.			606.15
ρl	850.13	kg/m3	223.16	Calculated Property
ρl	817.84	kg/m3	265.71	Calculated Property
ρl	783.84	kg/m3	308.27	Calculated Property
ρl	747.71	kg/m3	350.82	Calculated Property
ρl	708.85	kg/m3	393.38	Calculated Property
ρl	666.30	kg/m3	435.93	Calculated Property
ρl	618.41	kg/m3	478.49	Calculated Property
ρl	561.86	kg/m3	521.04	Calculated Property
ρl	487.57	kg/m3	563.60	Calculated Property
ρl	241.65	kg/m3	606.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 1.55e-05]	N/m	[223.16; 599.26]	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			-1.10150e-01
Coefficient B			-2.48560e+01
Coefficient C			-1.51820e+00
Coefficient D			-1.58990e-03
Coefficient E			8.53960e-07
Comment			Range stopped where the equation turns negative; ChemSep gives it to 606.15 K.
Temperature range, min.			223.16
Temperature range, max.			599.26
γ	0.03	N/m	223.16	Calculated Property
γ	0.03	N/m	264.95	Calculated Property
γ	0.02	N/m	306.74	Calculated Property
γ	0.02	N/m	348.53	Calculated Property
γ	0.02	N/m	390.31	Calculated Property
γ	0.01	N/m	432.10	Calculated Property
γ	0.01	N/m	473.89	Calculated Property
γ	0.01	N/m	515.68	Calculated Property
γ	0.00	N/m	557.47	Calculated Property
γ	1.55e-05	N/m	599.26	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.09]	W/m×K	[223.16; 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			1.58240e-02
Coefficient B			3.45160e-01
Coefficient C			-2.53880e+01
Coefficient D			8.92770e+05
Temperature range, min.			223.16
Temperature range, max.			1000.00
λgas	0.01	W/m×K	223.16	Calculated Property
λgas	0.01	W/m×K	309.48	Calculated Property
λgas	0.02	W/m×K	395.79	Calculated Property
λgas	0.03	W/m×K	482.11	Calculated Property
λgas	0.04	W/m×K	568.42	Calculated Property
λgas	0.05	W/m×K	654.74	Calculated Property
λgas	0.06	W/m×K	741.05	Calculated Property
λgas	0.07	W/m×K	827.37	Calculated Property
λgas	0.08	W/m×K	913.68	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.13; 0.10]	W/m×K	[223.16; 402.94]	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			-1.32340e-02
Coefficient B			-3.13660e+01
Coefficient C			-1.38920e+00
Coefficient D			-1.60870e-03
Coefficient E			-6.16200e-07
Temperature range, min.			223.16
Temperature range, max.			402.94
λliquid	0.13	W/m×K	223.16	Calculated Property
λliquid	0.13	W/m×K	243.14	Calculated Property
λliquid	0.13	W/m×K	263.11	Calculated Property
λliquid	0.12	W/m×K	283.09	Calculated Property
λliquid	0.12	W/m×K	303.06	Calculated Property
λliquid	0.11	W/m×K	323.04	Calculated Property
λliquid	0.11	W/m×K	343.01	Calculated Property
λliquid	0.10	W/m×K	362.99	Calculated Property
λliquid	0.10	W/m×K	382.96	Calculated Property
λliquid	0.10	W/m×K	402.94	Calculated Property

Similar Compounds

Find more compounds similar to Cyclohexane, 1,2-dimethyl-, cis-.

Mixtures

• Cyclohexane, 1,2-dimethyl-, cis- + Cyclohexane, 1,2-dimethyl-, trans- + Water
• Cyclohexane, 1,2-dimethyl-, cis- + Cyclohexane, 1,2-dimethyl-, trans- + 1,2-Ethanediol

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.
• 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
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Solubilities of Alkylcyclohexanes in Water from 30 C to 180 C
• Apparatus for the Determination of Water Solubility in Hydrocarbon: Toluene and Alkylcyclohexanes (C6 to C8) from 30 C to 180 C
• Liquid Liquid Equilibria at Three Temperatures (between 280.15 K and 333.15 K) of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Cyclohexane, para-Xylene, trans- and cis-Dimethylcyclohexane, and trans- and cis-Decahydronaphthalene
• Joback Method
• KDB
• 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

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