Chemical Properties of Cyclohexane, 1,3-dimethyl-, trans- (CAS 2207-03-6)

InChI

InChI=1S/C8H16/c1-7-4-3-5-8(2)6-7/h7-8H,3-6H2,1-2H3/t7-,8-/m0/s1

InChI Key

SGVUHPSBDNVHKL-YUMQZZPRSA-N

Formula

C8H16

SMILES

CC1CCCC(C)C1

Molecular Weight¹

112.21

CAS

2207-03-6

Other Names

• 1,3(trans)-dimethylcyclohexane
• 1,3-Dimethyl(trans)-cyclohexane
• 1,3-Dimethylcyclohexane, trans
• 1,trans-3-Dimethylcyclohexane
• Cyclohexane, trans-1,3-dimethyl-
• trans-1,3-Dimethyl cyclohexane
• trans-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_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).
• 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	[0.1886; 0.2356]
ω	0.2118		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.1886		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2356		ChemSep v8.3 pure component data Compiled value
ω	0.1890		KDB
AP	319.450	K	KDB
ΔcH°liquid	-5219.00 ± 1.70	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[36.32; 36.34]	kJ/mol
ΔfG°	36.32	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	36.34	kJ/mol	KDB
Δc,grossH	5219.04	kJ/mol	KDB
Δc,netH	4866.954	kJ/mol	KDB
ΔfH°gas	[-176.70; -176.56]	kJ/mol
ΔfH°gas	-176.56	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-176.70	kJ/mol	KDB
ΔfusH°	9.38	kJ/mol	Joback Calculated Property
ΔvapH°	[39.10; 39.21]	kJ/mol
ΔvapH°	39.21	kJ/mol	NIST
ΔvapH°	39.10	kJ/mol	NIST
ΔvapH°	39.20	kJ/mol	NIST
ΔvapH°	39.20 ± 0.10	kJ/mol	NIST
ΔvapH°	39.19	kJ/mol	NIST
IE	[9.52; 9.89]	eV
IE	9.53	eV	NIST
IE	9.52 ± 0.05	eV	NIST
IE	9.53	eV	NIST
IE	9.89 ± 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	[2938.43; 2970.00]	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	2970.00	kPa	KDB
Ptriple	4.22e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[783.00; 836.00]
Inp	802.60		NIST
Inp	810.80		NIST
Inp	803.90		NIST
Inp	804.10		NIST
Inp	804.20		NIST
Inp	804.30		NIST
Inp	804.10		NIST
Inp	805.60		NIST
Inp	810.80		NIST
Inp	813.00		NIST
Inp	804.90		NIST
Inp	804.60		NIST
Inp	809.80		NIST
Inp	805.40		NIST
Inp	803.90		NIST
Inp	804.30		NIST
Inp	Outlier 783.00		NIST
Inp	805.30		NIST
Inp	810.50		NIST
Inp	813.10		NIST
Inp	813.10		NIST
Inp	822.00		NIST
Inp	Outlier 829.00		NIST
Inp	Outlier 833.00		NIST
Inp	Outlier 836.00		NIST
Inp	806.00		NIST
Inp	811.00		NIST
Inp	802.00		NIST
Inp	807.00		NIST
Inp	808.00		NIST
Inp	811.00		NIST
Inp	814.00		NIST
Inp	805.50		NIST
Inp	802.00		NIST
Inp	823.00		NIST
Inp	806.00		NIST
Inp	810.00		NIST
Inp	798.00		NIST
Inp	808.84		NIST
Inp	823.00		NIST
Inp	798.70		NIST
Inp	798.00		NIST
Inp	802.80		NIST
Inp	804.10		NIST
Inp	805.30		NIST
Inp	806.20		NIST
Inp	802.20		NIST
Inp	804.10		NIST
Inp	805.30		NIST
Inp	806.20		NIST
Inp	800.00		NIST
Inp	806.00		NIST
Inp	806.00		NIST
Inp	805.60		NIST
Inp	807.60		NIST
Inp	810.60		NIST
Inp	813.00		NIST
Inp	814.90		NIST
Inp	816.60		NIST
Inp	806.00		NIST
Inp	799.00		NIST
Inp	Outlier 783.00		NIST
Inp	800.00		NIST
Ip	843.00		NIST
S°gas	376.39	J/mol×K	NIST
S°liquid	276.27	J/mol×K	NIST
Tboil	[392.00; 397.65]	K
Tboil	397.61	K	ChemSep v8.3 pure component data Compiled value
Tboil	397.60	K	KDB
Tboil	397.60	K	NIST
Tboil	393.45 ± 0.30	K	NIST
Tboil	397.65 ± 0.50	K	NIST
Tboil	397.60 ± 0.10	K	NIST
Tboil	397.60 ± 0.02	K	NIST
Tboil	397.60 ± 0.25	K	NIST
Tboil	393.85 ± 0.30	K	NIST
Tboil	396.65 ± 0.50	K	NIST
Tboil	Outlier 392.00 ± 3.00	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	[179.76; 406.83]	K
Tfus	183.07	K	ChemSep v8.3 pure component data Compiled value
Tfus	183.00	K	KDB
Tfus	406.83 ± 0.06	K	NIST
Tfus	179.76 ± 0.02	K	NIST
Tfus	196.45 ± 0.50	K	NIST
Ttriple	[183.03; 183.07]	K
Ttriple	183.07	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	183.05	K	ChemSep v8.3 pure component data Compiled value
Ttriple	183.06 ± 0.02	K	NIST
Ttriple	183.03 ± 0.05	K	NIST
Ttriple	183.06 ± 0.02	K	NIST
Ttriple	183.06 ± 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	[0.415; 0.460]	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	0.415	m3/kmol	KDB
Zc	[0.2481930; 0.2720000]
Zc	0.2720000		ChemSep v8.3 pure component data Compiled value
Zc	0.2481930		KDB
Zra	0.26		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[172.60; 213.70]	J/mol×K	[190.00; 300.00]
Cp,liquid	172.60	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	175.30	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	178.20	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
Cp,liquid	181.40	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	184.70	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	188.30	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	192.00	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	195.90	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	200.10	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	201.40	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
Cp,liquid	204.40	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	209.00	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
Cp,liquid	212.80	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	212.84	J/mol×K	298.15	NIST
Cp,liquid	213.70	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	[9.87; 9.87]	kJ/mol	[183.06; 183.10]
ΔfusH	9.87	kJ/mol	183.06	NIST
ΔfusH	9.87	kJ/mol	183.06	NIST
ΔfusH	9.87	kJ/mol	183.10	NIST
ΔfusH	9.87	kJ/mol	183.10	NIST
ΔvapH	[33.39; 37.90]	kJ/mol	[354.00; 397.60]
ΔvapH	37.40	kJ/mol	354.00	NIST
ΔvapH	37.90	kJ/mol	357.00	NIST
ΔvapH	33.85	kJ/mol	397.60	KDB
ΔvapH	33.39	kJ/mol	397.60	NIST
n0	1.42843		298.15	KDB
ρl	785.00	kg/m3	293.00	KDB
ΔfusS	[53.89; 53.89]	J/mol×K	[183.06; 183.06]
ΔfusS	53.89	J/mol×K	183.06	NIST
ΔfusS	53.89	J/mol×K	183.06	NIST
γ	0.02	N/m	298.20	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	[170.72; 270.29]	J/mol×K	[183.05; 397.61]	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			1.21960e+02
Coefficient B			7.66430e+01
Coefficient C			1.90984e+00
Coefficient D			9.56020e-03
Coefficient E			-5.72050e-06
Temperature range, min.			183.05
Temperature range, max.			397.61
Cp,liquid	170.72	J/mol×K	183.05	Calculated Property
Cp,liquid	177.29	J/mol×K	206.89	Calculated Property
Cp,liquid	184.97	J/mol×K	230.73	Calculated Property
Cp,liquid	193.76	J/mol×K	254.57	Calculated Property
Cp,liquid	203.69	J/mol×K	278.41	Calculated Property
Cp,liquid	214.76	J/mol×K	302.25	Calculated Property
Cp,liquid	226.97	J/mol×K	326.09	Calculated Property
Cp,liquid	240.33	J/mol×K	349.93	Calculated Property
Cp,liquid	254.79	J/mol×K	373.77	Calculated Property
Cp,liquid	270.29	J/mol×K	397.61	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0057962; 0.0001514]	Pa×s	[183.07; 478.40]	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			-1.08540e+01
Coefficient B			1.07440e+03
Coefficient C			-3.20300e-02
Coefficient D			4.56100e-08
Coefficient E			2.00000e+00
Temperature range, min.			183.07
Temperature range, max.			478.40
η	0.0057962	Pa×s	183.07	Calculated Property
η	0.0023643	Pa×s	215.88	Calculated Property
η	0.0012214	Pa×s	248.70	Calculated Property
η	0.0007358	Pa×s	281.51	Calculated Property
η	0.0004927	Pa×s	314.33	Calculated Property
η	0.0003559	Pa×s	347.14	Calculated Property
η	0.0002719	Pa×s	379.96	Calculated Property
η	0.0002169	Pa×s	412.77	Calculated Property
η	0.0001788	Pa×s	445.59	Calculated Property
η	0.0001514	Pa×s	478.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[45.85; 1.22]	kJ/mol	[183.05; 598.00]	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			6.93820e+01
Coefficient B			2.11840e+00
Coefficient C			-4.47660e+00
Coefficient D			4.67760e+00
Coefficient E			-1.83180e+00
Critical temperature, Tc (K)			5.98150e+02
Temperature range, min.			183.05
Temperature range, max.			598.00
ΔvapH	45.85	kJ/mol	183.05	Calculated Property
ΔvapH	43.07	kJ/mol	229.16	Calculated Property
ΔvapH	40.57	kJ/mol	275.26	Calculated Property
ΔvapH	38.05	kJ/mol	321.37	Calculated Property
ΔvapH	35.31	kJ/mol	367.47	Calculated Property
ΔvapH	32.16	kJ/mol	413.58	Calculated Property
ΔvapH	28.45	kJ/mol	459.68	Calculated Property
ΔvapH	23.92	kJ/mol	505.79	Calculated Property
ΔvapH	17.81	kJ/mol	551.89	Calculated Property
ΔvapH	1.22	kJ/mol	598.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[286.07; 423.77]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39936e+01
Coefficient B			-3.26162e+03
Coefficient C			-4.81030e+01
Temperature range, min.			286.07
Temperature range, max.			423.77
Pvap	1.33	kPa	286.07	Calculated Property
Pvap	3.05	kPa	301.37	Calculated Property
Pvap	6.35	kPa	316.67	Calculated Property
Pvap	12.23	kPa	331.97	Calculated Property
Pvap	22.00	kPa	347.27	Calculated Property
Pvap	37.40	kPa	362.57	Calculated Property
Pvap	60.52	kPa	377.87	Calculated Property
Pvap	93.83	kPa	393.17	Calculated Property
Pvap	140.16	kPa	408.47	Calculated Property
Pvap	202.63	kPa	423.77	Calculated Property
Pvap	[4.11e-05; 2940.57]	kPa	[183.05; 598.00]	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			7.34332e+01
Coefficient B			-7.07020e+03
Coefficient C			-8.65030e+00
Coefficient D			4.70540e-06
Coefficient E			2.00000e+00
Temperature range, min.			183.05
Temperature range, max.			598.00
Pvap	4.11e-05	kPa	183.05	Calculated Property
Pvap	0.02	kPa	229.16	Calculated Property
Pvap	0.61	kPa	275.26	Calculated Property
Pvap	7.27	kPa	321.37	Calculated Property
Pvap	41.86	kPa	367.47	Calculated Property
Pvap	152.35	kPa	413.58	Calculated Property
Pvap	409.92	kPa	459.68	Calculated Property
Pvap	898.41	kPa	505.79	Calculated Property
Pvap	1708.27	kPa	551.89	Calculated Property
Pvap	2940.57	kPa	598.00	Calculated Property
Pvap	[4.22e-05; 2937.30]	kPa	[183.05; 598.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			7.23828e+01
Coefficient B			-7.02468e+03
Coefficient C			-8.49035e+00
Coefficient D			4.56712e-06
Coefficient E			0.00000e+00
Temperature range, min.			183.05
Temperature range, max.			598.00
Pvap	4.22e-05	kPa	183.05	Calculated Property
Pvap	0.02	kPa	229.16	Calculated Property
Pvap	0.61	kPa	275.26	Calculated Property
Pvap	7.28	kPa	321.37	Calculated Property
Pvap	41.84	kPa	367.47	Calculated Property
Pvap	152.29	kPa	413.58	Calculated Property
Pvap	409.90	kPa	459.68	Calculated Property
Pvap	898.46	kPa	505.79	Calculated Property
Pvap	1707.84	kPa	551.89	Calculated Property
Pvap	2937.30	kPa	598.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[872.82; 427.12]	kg/m3	[183.05; 576.16]	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			5.75696e+01
Coefficient B			2.39920e-01
Coefficient C			5.98150e+02
Coefficient D			2.74410e-01
Temperature range, min.			183.05
Temperature range, max.			576.16
ρl	872.82	kg/m3	183.05	Calculated Property
ρl	839.60	kg/m3	226.73	Calculated Property
ρl	804.85	kg/m3	270.41	Calculated Property
ρl	768.22	kg/m3	314.09	Calculated Property
ρl	729.22	kg/m3	357.77	Calculated Property
ρl	687.09	kg/m3	401.44	Calculated Property
ρl	640.61	kg/m3	445.12	Calculated Property
ρl	587.52	kg/m3	488.80	Calculated Property
ρl	522.68	kg/m3	532.48	Calculated Property
ρl	427.12	kg/m3	576.16	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 8.32e-06]	N/m	[183.05; 593.85]	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			-8.16040e-03
Coefficient B			5.05520e+01
Coefficient C			-3.36360e+00
Coefficient D			9.93600e-04
Coefficient E			-6.00870e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 598 K.
Temperature range, min.			183.05
Temperature range, max.			593.85
γ	0.04	N/m	183.05	Calculated Property
γ	0.03	N/m	228.69	Calculated Property
γ	0.03	N/m	274.34	Calculated Property
γ	0.02	N/m	319.98	Calculated Property
γ	0.02	N/m	365.63	Calculated Property
γ	0.01	N/m	411.27	Calculated Property
γ	0.01	N/m	456.92	Calculated Property
γ	0.01	N/m	502.56	Calculated Property
γ	0.00	N/m	548.21	Calculated Property
γ	8.32e-06	N/m	593.85	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.09]	W/m×K	[183.05; 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			1.64850e-02
Coefficient B			3.43260e-01
Coefficient C			5.66870e+00
Coefficient D			8.94520e+05
Temperature range, min.			183.05
Temperature range, max.			1000.00
λgas	0.00	W/m×K	183.05	Calculated Property
λgas	0.01	W/m×K	273.82	Calculated Property
λgas	0.02	W/m×K	364.59	Calculated Property
λgas	0.03	W/m×K	455.37	Calculated Property
λgas	0.04	W/m×K	546.14	Calculated Property
λgas	0.05	W/m×K	636.91	Calculated Property
λgas	0.06	W/m×K	727.68	Calculated Property
λgas	0.07	W/m×K	818.46	Calculated Property
λgas	0.08	W/m×K	909.23	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	[183.05; 397.61]	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			-4.69770e-02
Coefficient B			2.88970e+00
Coefficient C			-1.56460e+00
Coefficient D			-4.64190e-04
Coefficient E			-1.33040e-06
Temperature range, min.			183.05
Temperature range, max.			397.61
λliquid	0.14	W/m×K	183.05	Calculated Property
λliquid	0.14	W/m×K	206.89	Calculated Property
λliquid	0.13	W/m×K	230.73	Calculated Property
λliquid	0.13	W/m×K	254.57	Calculated Property
λliquid	0.12	W/m×K	278.41	Calculated Property
λliquid	0.12	W/m×K	302.25	Calculated Property
λliquid	0.11	W/m×K	326.09	Calculated Property
λliquid	0.11	W/m×K	349.93	Calculated Property
λliquid	0.10	W/m×K	373.77	Calculated Property
λliquid	0.09	W/m×K	397.61	Calculated Property

Similar Compounds

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

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
• 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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