Chemical Properties of Cyclohexane, 1,4-dimethyl-, cis- (CAS 624-29-3)

InChI

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

InChI Key

QRMPKOFEUHIBNM-OCAPTIKFSA-N

Formula

C8H16

SMILES

CC1CCC(C)CC1

Molecular Weight¹

112.21

CAS

624-29-3

Other Names

• 1,4(cis)-dimethylcyclohexane
• 1,4-Dimethylcyclohexane, cis-
• 1,cis-4-Dimethylcyclohexane
• Cyclohexane, cis-1,4-dimethyl-
• cis-1,4-Dimethyl cyclohexane
• cis-1,4-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.
• 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 : 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	[0.2338; 0.2348]
ω	0.2338		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2338		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2348		ChemSep v8.3 pure component data Compiled value
ω	0.2340		KDB
AP	320.050	K	KDB
ΔcH°liquid	-5219.10 ± 1.70	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[37.95; 37.97]	kJ/mol
ΔfG°	37.95	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	37.97	kJ/mol	KDB
Δc,grossH	5219.12	kJ/mol	KDB
Δc,netH	4867.038	kJ/mol	KDB
ΔfH°gas	[-176.80; -176.65]	kJ/mol
ΔfH°gas	-176.65	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-176.80	kJ/mol	KDB
ΔfusH°	9.38	kJ/mol	Joback Calculated Property
ΔvapH°	[39.00; 3900.00]	kJ/mol
ΔvapH°	39.07	kJ/mol	NIST
ΔvapH°	39.00	kJ/mol	NIST
ΔvapH°	3900.00	kJ/mol	NIST
ΔvapH°	39.00 ± 0.10	kJ/mol	NIST
ΔvapH°	39.02	kJ/mol	NIST
IE	9.93 ± 0.05	eV	NIST
log10WS	-4.62		Relay (1.0) Calculated Property
logPoct/wat	2.833		Crippen Calculated Property
McVol	112.720	ml/mol	McGowan Calculated Property
Pc	[2900.00; 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	2900.00	kPa	KDB
Ptriple	7.04e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[761.00; 838.20]
Inp	Outlier 838.20		NIST
Inp	823.40		NIST
Inp	828.30		NIST
Inp	Outlier 837.40		NIST
Inp	813.00		NIST
Inp	804.60		NIST
Inp	804.60		NIST
Inp	809.80		NIST
Inp	805.00		NIST
Inp	804.10		NIST
Inp	804.50		NIST
Inp	810.00		NIST
Inp	809.60		NIST
Inp	811.90		NIST
Inp	815.10		NIST
Inp	815.30		NIST
Inp	810.70		NIST
Inp	810.80		NIST
Inp	813.10		NIST
Inp	813.10		NIST
Inp	822.00		NIST
Inp	829.00		NIST
Inp	833.00		NIST
Inp	836.00		NIST
Inp	805.00		NIST
Inp	810.00		NIST
Inp	805.50		NIST
Inp	801.00		NIST
Inp	820.00		NIST
Inp	804.00		NIST
Inp	810.00		NIST
Inp	820.00		NIST
Inp	821.00		NIST
Inp	801.20		NIST
Inp	802.80		NIST
Inp	Outlier 772.45		NIST
Inp	Outlier 770.01		NIST
Inp	804.70		NIST
Inp	805.30		NIST
Inp	805.70		NIST
Inp	802.20		NIST
Inp	804.70		NIST
Inp	805.30		NIST
Inp	805.70		NIST
Inp	800.00		NIST
Inp	800.00		NIST
Inp	806.00		NIST
Inp	795.00		NIST
Inp	804.00		NIST
Inp	805.20		NIST
Inp	807.20		NIST
Inp	810.10		NIST
Inp	812.40		NIST
Inp	814.30		NIST
Inp	816.00		NIST
Inp	Outlier 761.00		NIST
Inp	795.00		NIST
Inp	812.40		NIST
Inp	802.80		NIST
Inp	805.70		NIST
Inp	800.00		NIST
Inp	Outlier 838.20		NIST
Inp	804.60		NIST
Inp	804.50		NIST
Inp	815.30		NIST
Inp	822.00		NIST
Inp	810.00		NIST
S°gas	370.87	J/mol×K	NIST
S°liquid	271.12	J/mol×K	NIST
Tboil	[392.15; 397.80]	K
Tboil	397.48	K	ChemSep v8.3 pure component data Compiled value
Tboil	397.60	K	KDB
Tboil	397.70	K	NIST
Tboil	397.50	K	NIST
Tboil	397.80 ± 1.00	K	NIST
Tboil	397.00 ± 2.00	K	NIST
Tboil	397.00 ± 2.00	K	NIST
Tboil	397.70 ± 1.00	K	NIST
Tboil	397.00 ± 2.00	K	NIST
Tboil	397.73 ± 0.30	K	NIST
Tboil	Outlier 392.15 ± 0.30	K	NIST
Tboil	397.65 ± 0.50	K	NIST
Tboil	397.47 ± 0.15	K	NIST
Tboil	397.49 ± 0.30	K	NIST
Tboil	397.49 ± 0.30	K	NIST
Tboil	397.47 ± 0.25	K	NIST
Tboil	397.65 ± 0.30	K	NIST
Tboil	394.00 ± 0.50	K	NIST
Tboil	397.74 ± 0.30	K	NIST
Tboil	394.70 ± 2.00	K	NIST
Tc	[598.00; 598.15]	K
Tc	598.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	598.15	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	598.15	K	ChemSep v8.3 pure component data Compiled value
Tc	598.00	K	KDB
Tfus	[185.42; 186.50]	K
Tfus	185.74	K	ChemSep v8.3 pure component data Compiled value
Tfus	185.70	K	KDB
Tfus	186.50 ± 0.50	K	NIST
Tfus	185.72 ± 0.03	K	NIST
Tfus	185.46 ± 0.20	K	NIST
Tfus	185.42 ± 0.02	K	NIST
Tfus	186.45 ± 0.70	K	NIST
Ttriple	[185.72; 195.73]	K
Ttriple	185.74	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	185.72	K	ChemSep v8.3 pure component data Compiled value
Ttriple	185.73 ± 0.02	K	NIST
Ttriple	185.72 ± 0.05	K	NIST
Ttriple	Outlier 195.73 ± 0.02	K	NIST
Ttriple	185.73 ± 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	[0.460; 0.471]	m3/kmol
Vc	0.460	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	[0.2720000; 0.2748890]
Zc	0.2720000		ChemSep v8.3 pure component data Compiled value
Zc	0.2748890		KDB
Zra	0.26		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[174.40; 213.10]	J/mol×K	[190.00; 300.00]
Cp,liquid	174.40	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
Cp,liquid	176.70	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
Cp,liquid	179.30	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	182.10	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	185.10	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	188.40	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	191.90	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	195.60	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	199.60	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	200.90	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	203.90	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	208.30	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	212.20	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	212.09	J/mol×K	298.15	NIST
Cp,liquid	213.10	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	[9.29; 9.31]	kJ/mol	[185.70; 185.73]
ΔfusH	9.29	kJ/mol	185.70	NIST
ΔfusH	9.31	kJ/mol	185.70	NIST
ΔfusH	9.31	kJ/mol	185.73	NIST
ΔfusH	9.31	kJ/mol	185.73	NIST
ΔvapH	[33.28; 37.60]	kJ/mol	[358.50; 397.60]
ΔvapH	37.60	kJ/mol	358.50	NIST
ΔvapH	33.28	kJ/mol	397.50	NIST
ΔvapH	33.77	kJ/mol	397.60	KDB
n0	1.42731		298.15	KDB
ρl	783.00	kg/m3	293.00	KDB
ΔfusS	[50.11; 50.11]	J/mol×K	[185.73; 185.73]
ΔfusS	50.11	J/mol×K	185.73	NIST
ΔfusS	50.11	J/mol×K	185.73	NIST
γ	0.02	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[116.51; 492.99]	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			1.01700e+02
Coefficient B			-8.44250e+02
Coefficient C			7.02324e+00
Coefficient D			-5.63740e-04
Coefficient E			1.57620e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	116.51	J/mol×K	200.00	Calculated Property
Cp,gas	182.88	J/mol×K	344.44	Calculated Property
Cp,gas	259.04	J/mol×K	488.89	Calculated Property
Cp,gas	322.31	J/mol×K	633.33	Calculated Property
Cp,gas	370.69	J/mol×K	777.78	Calculated Property
Cp,gas	407.20	J/mol×K	922.22	Calculated Property
Cp,gas	435.24	J/mol×K	1066.67	Calculated Property
Cp,gas	457.58	J/mol×K	1211.11	Calculated Property
Cp,gas	476.31	J/mol×K	1355.56	Calculated Property
Cp,gas	492.99	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[173.48; 270.75]	J/mol×K	[185.72; 397.47]	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			1.10770e+02
Coefficient B			1.40070e+02
Coefficient C			1.85394e+00
Coefficient D			9.13730e-03
Coefficient E			-4.83020e-06
Temperature range, min.			185.72
Temperature range, max.			397.47
Cp,liquid	173.48	J/mol×K	185.72	Calculated Property
Cp,liquid	179.06	J/mol×K	209.25	Calculated Property
Cp,liquid	186.03	J/mol×K	232.78	Calculated Property
Cp,liquid	194.29	J/mol×K	256.30	Calculated Property
Cp,liquid	203.82	J/mol×K	279.83	Calculated Property
Cp,liquid	214.63	J/mol×K	303.36	Calculated Property
Cp,liquid	226.72	J/mol×K	326.89	Calculated Property
Cp,liquid	240.11	J/mol×K	350.41	Calculated Property
Cp,liquid	254.79	J/mol×K	373.94	Calculated Property
Cp,liquid	270.75	J/mol×K	397.47	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0080570; 0.0001600]	Pa×s	[185.72; 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			-2.07040e+01
Coefficient B			1.39140e+03
Coefficient C			1.63780e+00
Coefficient D			-4.79530e-06
Coefficient E			2.00000e+00
Temperature range, min.			185.72
Temperature range, max.			472.00
η	0.0080570	Pa×s	185.72	Calculated Property
η	0.0032819	Pa×s	217.53	Calculated Property
η	0.0016900	Pa×s	249.34	Calculated Property
η	0.0010091	Pa×s	281.15	Calculated Property
η	0.0006643	Pa×s	312.96	Calculated Property
η	0.0004672	Pa×s	344.76	Calculated Property
η	0.0003439	Pa×s	376.57	Calculated Property
η	0.0002613	Pa×s	408.38	Calculated Property
η	0.0002029	Pa×s	440.19	Calculated Property
η	0.0001600	Pa×s	472.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[45.43; 12.84]	kJ/mol	[185.72; 576.44]	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			7.15140e+01
Coefficient B			2.37240e+00
Coefficient C			-5.20210e+00
Coefficient D			5.47510e+00
Coefficient E			-2.15210e+00
Critical temperature, Tc (K)			5.98150e+02
Temperature range, min.			185.72
Temperature range, max.			576.44
ΔvapH	45.43	kJ/mol	185.72	Calculated Property
ΔvapH	42.82	kJ/mol	229.13	Calculated Property
ΔvapH	40.49	kJ/mol	272.55	Calculated Property
ΔvapH	38.19	kJ/mol	315.96	Calculated Property
ΔvapH	35.70	kJ/mol	359.37	Calculated Property
ΔvapH	32.86	kJ/mol	402.79	Calculated Property
ΔvapH	29.54	kJ/mol	446.20	Calculated Property
ΔvapH	25.58	kJ/mol	489.61	Calculated Property
ΔvapH	20.59	kJ/mol	533.03	Calculated Property
ΔvapH	12.84	kJ/mol	576.44	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[285.84; 425.21]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38911e+01
Coefficient B			-3.23780e+03
Coefficient C			-4.78270e+01
Temperature range, min.			285.84
Temperature range, max.			425.21
Pvap	1.33	kPa	285.84	Calculated Property
Pvap	3.06	kPa	301.33	Calculated Property
Pvap	6.39	kPa	316.81	Calculated Property
Pvap	12.30	kPa	332.30	Calculated Property
Pvap	22.13	kPa	347.78	Calculated Property
Pvap	37.59	kPa	363.27	Calculated Property
Pvap	60.77	kPa	378.75	Calculated Property
Pvap	94.11	kPa	394.24	Calculated Property
Pvap	140.38	kPa	409.72	Calculated Property
Pvap	202.65	kPa	425.21	Calculated Property
Pvap	[6.82e-05; 2939.97]	kPa	[185.72; 598.15]	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			7.22552e+01
Coefficient B			-7.00460e+03
Coefficient C			-8.47790e+00
Coefficient D			4.60530e-06
Coefficient E			2.00000e+00
Temperature range, min.			185.72
Temperature range, max.			598.15
Pvap	6.82e-05	kPa	185.72	Calculated Property
Pvap	0.02	kPa	231.55	Calculated Property
Pvap	0.72	kPa	277.37	Calculated Property
Pvap	7.97	kPa	323.20	Calculated Property
Pvap	44.22	kPa	369.02	Calculated Property
Pvap	157.44	kPa	414.85	Calculated Property
Pvap	417.85	kPa	460.67	Calculated Property
Pvap	907.72	kPa	506.50	Calculated Property
Pvap	1715.57	kPa	552.32	Calculated Property
Pvap	2939.97	kPa	598.15	Calculated Property
Pvap	[7.04e-05; 2941.05]	kPa	[185.72; 598.15]	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			7.15606e+01
Coefficient B			-6.96889e+03
Coefficient C			-8.37542e+00
Coefficient D			4.54960e-06
Coefficient E			0.00000e+00
Temperature range, min.			185.72
Temperature range, max.			598.15
Pvap	7.04e-05	kPa	185.72	Calculated Property
Pvap	0.02	kPa	231.55	Calculated Property
Pvap	0.72	kPa	277.37	Calculated Property
Pvap	7.99	kPa	323.20	Calculated Property
Pvap	44.23	kPa	369.02	Calculated Property
Pvap	157.37	kPa	414.85	Calculated Property
Pvap	417.65	kPa	460.67	Calculated Property
Pvap	907.51	kPa	506.50	Calculated Property
Pvap	1715.72	kPa	552.32	Calculated Property
Pvap	2941.05	kPa	598.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[866.61; 427.35]	kg/m3	[185.72; 576.44]	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			5.98497e+01
Coefficient B			2.45330e-01
Coefficient C			5.98150e+02
Coefficient D			2.77100e-01
Temperature range, min.			185.72
Temperature range, max.			576.44
ρl	866.61	kg/m3	185.72	Calculated Property
ρl	833.90	kg/m3	229.13	Calculated Property
ρl	799.69	kg/m3	272.55	Calculated Property
ρl	763.61	kg/m3	315.96	Calculated Property
ρl	725.20	kg/m3	359.37	Calculated Property
ρl	683.70	kg/m3	402.79	Calculated Property
ρl	637.91	kg/m3	446.20	Calculated Property
ρl	585.60	kg/m3	489.61	Calculated Property
ρl	521.68	kg/m3	533.03	Calculated Property
ρl	427.35	kg/m3	576.44	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 9.18e-04]	N/m	[185.72; 576.44]	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			-1.30740e-02
Coefficient B			2.42990e+01
Coefficient C			-3.00070e+00
Coefficient D			-1.83310e-04
Coefficient E			-3.62660e-06
Temperature range, min.			185.72
Temperature range, max.			576.44
γ	0.04	N/m	185.72	Calculated Property
γ	0.03	N/m	229.13	Calculated Property
γ	0.03	N/m	272.55	Calculated Property
γ	0.02	N/m	315.96	Calculated Property
γ	0.02	N/m	359.37	Calculated Property
γ	0.01	N/m	402.79	Calculated Property
γ	0.01	N/m	446.20	Calculated Property
γ	0.01	N/m	489.61	Calculated Property
γ	0.00	N/m	533.03	Calculated Property
γ	9.18e-04	N/m	576.44	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.09]	W/m×K	[185.72; 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			1.67470e-02
Coefficient B			3.40720e-01
Coefficient C			-1.79650e+00
Coefficient D			8.98230e+05
Temperature range, min.			185.72
Temperature range, max.			1000.00
λgas	0.00	W/m×K	185.72	Calculated Property
λgas	0.01	W/m×K	276.20	Calculated Property
λgas	0.02	W/m×K	366.67	Calculated Property
λgas	0.03	W/m×K	457.15	Calculated Property
λgas	0.04	W/m×K	547.62	Calculated Property
λgas	0.05	W/m×K	638.10	Calculated Property
λgas	0.06	W/m×K	728.57	Calculated Property
λgas	0.07	W/m×K	819.05	Calculated Property
λgas	0.08	W/m×K	909.52	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.09]	W/m×K	[185.72; 397.47]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			-6.35270e-02
Coefficient B			3.30260e+00
Coefficient C			-1.49410e+00
Coefficient D			-4.36200e-04
Coefficient E			-1.16630e-06
Temperature range, min.			185.72
Temperature range, max.			397.47
λliquid	0.14	W/m×K	185.72	Calculated Property
λliquid	0.13	W/m×K	209.25	Calculated Property
λliquid	0.13	W/m×K	232.78	Calculated Property
λliquid	0.12	W/m×K	256.30	Calculated Property
λliquid	0.12	W/m×K	279.83	Calculated Property
λliquid	0.12	W/m×K	303.36	Calculated Property
λliquid	0.11	W/m×K	326.89	Calculated Property
λliquid	0.10	W/m×K	350.41	Calculated Property
λliquid	0.10	W/m×K	373.94	Calculated Property
λliquid	0.09	W/m×K	397.47	Calculated Property

Similar Compounds

Find more compounds similar to Cyclohexane, 1,4-dimethyl-, cis-.

Sources

• KDB Vapor Pressure Data
• 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.
• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Crippen Method
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• 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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