Chemical Properties of Cyclohexane, 1,2-dimethyl-, trans- (CAS 6876-23-9)

InChI

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

InChI Key

KVZJLSYJROEPSQ-YUMQZZPRSA-N

Formula

C8H16

SMILES

CC1CCCCC1C

Molecular Weight¹

112.21

CAS

6876-23-9

Other Names

• (1R*,2R*)-1,2-dimethylcyclohexane
• 1,2-Dimethyl(trans)-cyclohexane
• 1,2-Dimethylcyclohexane, trans-
• 1,2-trans-dimethylcyclohexane
• 1,trans-2-Dimethylcyclohexane
• Cyclohexane, trans-1,2-dimethyl-
• NSC 74158
• t-1,2-Dimethylcyclohexane
• trans-1,2-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	[0.2296; 0.2420]
ω	0.2296		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2416		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2416		ChemSep v8.3 pure component data Compiled value
ω	0.2420		KDB
AP	321.450	K	KDB
ΔcH°liquid	-5216.50 ± 1.80	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[34.48; 34.50]	kJ/mol
ΔfG°	34.48	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	34.50	kJ/mol	KDB
Δc,grossH	5216.44	kJ/mol	KDB
Δc,netH	4864.360	kJ/mol	KDB
ΔfH°gas	[-180.10; -180.00]	kJ/mol
ΔfH°gas	-180.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-180.10	kJ/mol	KDB
ΔfusH°	9.38	kJ/mol	Joback Calculated Property
ΔvapH°	[38.30; 38.41]	kJ/mol
ΔvapH°	38.41	kJ/mol	NIST
ΔvapH°	38.30	kJ/mol	NIST
ΔvapH°	38.40	kJ/mol	NIST
ΔvapH°	38.40 ± 0.10	kJ/mol	NIST
ΔvapH°	38.35	kJ/mol	NIST
IE	[9.41; 10.08]	eV
IE	9.41	eV	NIST
IE	9.89 ± 0.05	eV	NIST
IE	10.03 ± 0.05	eV	NIST
IE	10.08 ± 0.03	eV	NIST
log10WS	-4.55		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	8.04e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[779.00; 837.80]
Inp	Outlier 837.80		NIST
Inp	783.00		NIST
Inp	807.70		NIST
Inp	Outlier 828.20		NIST
Inp	Outlier 834.70		NIST
Inp	797.40		NIST
Inp	797.50		NIST
Inp	797.70		NIST
Inp	797.80		NIST
Inp	797.50		NIST
Inp	Outlier 836.60		NIST
Inp	801.80		NIST
Inp	807.50		NIST
Inp	805.00		NIST
Inp	801.10		NIST
Inp	819.40		NIST
Inp	820.10		NIST
Inp	791.80		NIST
Inp	793.90		NIST
Inp	796.20		NIST
Inp	798.40		NIST
Inp	801.80		NIST
Inp	797.40		NIST
Inp	797.80		NIST
Inp	804.00		NIST
Inp	794.00		NIST
Inp	794.00		NIST
Inp	794.00		NIST
Inp	818.00		NIST
Inp	801.50		NIST
Inp	807.30		NIST
Inp	812.30		NIST
Inp	812.50		NIST
Inp	812.60		NIST
Inp	807.50		NIST
Inp	807.60		NIST
Inp	810.00		NIST
Inp	810.00		NIST
Inp	802.00		NIST
Inp	808.00		NIST
Inp	799.00		NIST
Inp	803.00		NIST
Inp	805.00		NIST
Inp	808.00		NIST
Inp	811.00		NIST
Inp	802.00		NIST
Inp	799.00		NIST
Inp	806.00		NIST
Inp	817.00		NIST
Inp	802.00		NIST
Inp	807.00		NIST
Inp	817.00		NIST
Inp	802.01		NIST
Inp	792.00		NIST
Inp	819.00		NIST
Inp	792.70		NIST
Inp	794.00		NIST
Inp	795.70		NIST
Inp	790.99		NIST
Inp	791.42		NIST
Inp	796.70		NIST
Inp	798.00		NIST
Inp	798.40		NIST
Inp	804.80		NIST
Inp	795.10		NIST
Inp	796.70		NIST
Inp	798.00		NIST
Inp	798.40		NIST
Inp	792.78		NIST
Inp	793.00		NIST
Inp	792.00		NIST
Inp	816.00		NIST
Inp	798.00		NIST
Inp	807.00		NIST
Inp	793.00		NIST
Inp	803.80		NIST
Inp	806.80		NIST
Inp	809.20		NIST
Inp	811.20		NIST
Inp	813.00		NIST
Inp	803.00		NIST
Inp	806.00		NIST
Inp	809.00		NIST
Inp	811.00		NIST
Inp	813.00		NIST
Inp	Outlier 779.00		NIST
Inp	802.00		NIST
Inp	800.00		NIST
Inp	793.00		NIST
Inp	783.00		NIST
Inp	804.00		NIST
Inp	812.00		NIST
Inp	807.00		NIST
Inp	816.00		NIST
Inp	792.70		NIST
Inp	793.00		NIST
Inp	813.00		NIST
S°gas	371.33	J/mol×K	NIST
S°liquid	273.22	J/mol×K	NIST
Tboil	[396.00; 417.20]	K
Tboil	396.58	K	ChemSep v8.3 pure component data Compiled value
Tboil	396.70	K	KDB
Tboil	396.70	K	NIST
Tboil	396.60	K	NIST
Tboil	397.00 ± 2.00	K	NIST
Tboil	396.56 ± 0.20	K	NIST
Tboil	397.00 ± 2.00	K	NIST
Tboil	396.00 ± 1.50	K	NIST
Tboil	396.15 ± 0.30	K	NIST
Tboil	396.75 ± 0.50	K	NIST
Tboil	396.85 ± 0.30	K	NIST
Tboil	396.54 ± 0.25	K	NIST
Tboil	396.54 ± 0.30	K	NIST
Tboil	396.56 ± 0.02	K	NIST
Tboil	396.57 ± 0.20	K	NIST
Tboil	396.85 ± 0.30	K	NIST
Tboil	396.85 ± 0.30	K	NIST
Tboil	396.84 ± 0.30	K	NIST
Tboil	Outlier 417.20 ± 0.20	K	NIST
Tboil	397.00 ± 3.00	K	NIST
Tc	[595.93; 596.30]	K
Tc	596.30	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	596.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	595.93	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	596.15	K	ChemSep v8.3 pure component data Compiled value
Tc	596.00	K	KDB
Tc	596.00	K	NIST
Tfus	[183.55; 185.00]	K
Tfus	184.99	K	ChemSep v8.3 pure component data Compiled value
Tfus	185.00	K	KDB
Tfus	183.75 ± 0.40	K	NIST
Tfus	184.60 ± 0.50	K	NIST
Tfus	184.97 ± 0.04	K	NIST
Tfus	184.45 ± 0.20	K	NIST
Tfus	184.86 ± 0.02	K	NIST
Tfus	184.55 ± 0.50	K	NIST
Tfus	183.55 ± 0.30	K	NIST
Ttriple	[184.98; 184.99]	K
Ttriple	184.99	K	ChemSep v8.3 pure component data Compiled value
Ttriple	184.99 ± 0.02	K	NIST
Ttriple	184.98 ± 0.05	K	NIST
Ttriple	184.99 ± 0.03	K	NIST
Ttriple	184.99 ± 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	[0.2730000; 0.2758120]
Zc	0.2730000		ChemSep v8.3 pure component data Compiled value
Zc	0.2758120		KDB
Zra	0.27		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[167.40; 210.40]	J/mol×K	[190.00; 300.00]
Cp,liquid	167.40	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	170.20	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	173.20	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	176.50	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
Cp,liquid	180.00	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
Cp,liquid	183.70	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	187.60	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	191.70	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	196.00	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	197.50	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	200.60	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	205.40	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	209.41	J/mol×K	298.15	NIST
Cp,liquid	210.40	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	[10.49; 10.50]	kJ/mol	[184.99; 185.00]
ΔfusH	10.49	kJ/mol	184.99	NIST
ΔfusH	10.49	kJ/mol	184.99	NIST
ΔfusH	10.50	kJ/mol	185.00	NIST
ΔfusH	10.50	kJ/mol	185.00	NIST
ΔvapH	[32.89; 37.00]	kJ/mol	[357.50; 396.70]
ΔvapH	37.00	kJ/mol	357.50	NIST
ΔvapH	34.40 ± 0.10	kJ/mol	373.00	NIST
ΔvapH	33.50 ± 0.10	kJ/mol	387.00	NIST
ΔvapH	32.96	kJ/mol	396.60	NIST
ΔvapH	32.89	kJ/mol	396.70	KDB
n0	1.42470		298.15	KDB
ρl	776.00	kg/m3	293.00	KDB
ΔfusS	[56.72; 56.72]	J/mol×K	[184.99; 184.99]
ΔfusS	56.72	J/mol×K	184.99	NIST
ΔfusS	56.72	J/mol×K	184.99	NIST
γ	0.02	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[115.14; 493.87]	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			9.77390e+01
Coefficient B			-7.99790e+02
Coefficient C			6.94824e+00
Coefficient D			-4.90410e-04
Coefficient E			1.34360e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	115.14	J/mol×K	200.00	Calculated Property
Cp,gas	185.38	J/mol×K	344.44	Calculated Property
Cp,gas	262.53	J/mol×K	488.89	Calculated Property
Cp,gas	325.60	J/mol×K	633.33	Calculated Property
Cp,gas	373.57	J/mol×K	777.78	Calculated Property
Cp,gas	409.74	J/mol×K	922.22	Calculated Property
Cp,gas	437.49	J/mol×K	1066.67	Calculated Property
Cp,gas	459.51	J/mol×K	1211.11	Calculated Property
Cp,gas	477.81	J/mol×K	1355.56	Calculated Property
Cp,gas	493.87	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[165.74; 269.85]	J/mol×K	[183.68; 396.58]	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			1.07760e+02
Coefficient B			9.52780e+01
Coefficient C			2.03784e+00
Coefficient D			9.13450e-03
Coefficient E			-5.16600e-06
Temperature range, min.			183.68
Temperature range, max.			396.58
Cp,liquid	165.74	J/mol×K	183.68	Calculated Property
Cp,liquid	172.42	J/mol×K	207.34	Calculated Property
Cp,liquid	180.34	J/mol×K	230.99	Calculated Property
Cp,liquid	189.46	J/mol×K	254.65	Calculated Property
Cp,liquid	199.80	J/mol×K	278.30	Calculated Property
Cp,liquid	211.36	J/mol×K	301.96	Calculated Property
Cp,liquid	224.16	J/mol×K	325.61	Calculated Property
Cp,liquid	238.19	J/mol×K	349.27	Calculated Property
Cp,liquid	253.43	J/mol×K	372.92	Calculated Property
Cp,liquid	269.85	J/mol×K	396.58	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0082971; 0.0001872]	Pa×s	[184.99; 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			-9.86950e+00
Coefficient B			1.12440e+03
Coefficient C			-1.94680e-01
Coefficient D			4.60830e-07
Coefficient E			2.00000e+00
Temperature range, min.			184.99
Temperature range, max.			472.00
η	0.0082971	Pa×s	184.99	Calculated Property
η	0.0033106	Pa×s	216.88	Calculated Property
η	0.0016697	Pa×s	248.77	Calculated Property
η	0.0009835	Pa×s	280.66	Calculated Property
η	0.0006456	Pa×s	312.55	Calculated Property
η	0.0004584	Pa×s	344.44	Calculated Property
η	0.0003453	Pa×s	376.33	Calculated Property
η	0.0002723	Pa×s	408.22	Calculated Property
η	0.0002225	Pa×s	440.11	Calculated Property
η	0.0001872	Pa×s	472.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[44.64; 13.29]	kJ/mol	[184.99; 574.51]	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			6.39640e+01
Coefficient B			1.69460e+00
Coefficient C			-3.20860e+00
Coefficient D			3.16630e+00
Coefficient E			-1.19470e+00
Critical temperature, Tc (K)			5.96150e+02
Temperature range, min.			184.99
Temperature range, max.			574.51
ΔvapH	44.64	kJ/mol	184.99	Calculated Property
ΔvapH	42.17	kJ/mol	228.27	Calculated Property
ΔvapH	39.88	kJ/mol	271.55	Calculated Property
ΔvapH	37.61	kJ/mol	314.83	Calculated Property
ΔvapH	35.19	kJ/mol	358.11	Calculated Property
ΔvapH	32.51	kJ/mol	401.39	Calculated Property
ΔvapH	29.41	kJ/mol	444.67	Calculated Property
ΔvapH	25.69	kJ/mol	487.95	Calculated Property
ΔvapH	20.91	kJ/mol	531.23	Calculated Property
ΔvapH	13.29	kJ/mol	574.51	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[284.85; 425.06]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39092e+01
Coefficient B			-3.26861e+03
Coefficient C			-4.48910e+01
Temperature range, min.			284.85
Temperature range, max.			425.06
Pvap	1.33	kPa	284.85	Calculated Property
Pvap	3.06	kPa	300.43	Calculated Property
Pvap	6.38	kPa	316.01	Calculated Property
Pvap	12.28	kPa	331.59	Calculated Property
Pvap	22.11	kPa	347.17	Calculated Property
Pvap	37.56	kPa	362.74	Calculated Property
Pvap	60.72	kPa	378.32	Calculated Property
Pvap	94.05	kPa	393.90	Calculated Property
Pvap	140.34	kPa	409.48	Calculated Property
Pvap	202.64	kPa	425.06	Calculated Property
Pvap	[7.92e-05; 2938.88]	kPa	[184.99; 596.15]	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			7.20432e+01
Coefficient B			-6.90580e+03
Coefficient C			-8.49150e+00
Coefficient D			5.04060e-06
Coefficient E			2.00000e+00
Temperature range, min.			184.99
Temperature range, max.			596.15
Pvap	7.92e-05	kPa	184.99	Calculated Property
Pvap	0.02	kPa	230.67	Calculated Property
Pvap	0.74	kPa	276.36	Calculated Property
Pvap	8.06	kPa	322.04	Calculated Property
Pvap	43.95	kPa	367.73	Calculated Property
Pvap	155.05	kPa	413.41	Calculated Property
Pvap	410.30	kPa	459.10	Calculated Property
Pvap	893.08	kPa	504.78	Calculated Property
Pvap	1698.28	kPa	550.47	Calculated Property
Pvap	2938.88	kPa	596.15	Calculated Property
Pvap	[8.03e-05; 2937.27]	kPa	[184.99; 596.15]	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			7.15749e+01
Coefficient B			-6.88423e+03
Coefficient C			-8.42118e+00
Coefficient D			4.99052e-06
Coefficient E			0.00000e+00
Temperature range, min.			184.99
Temperature range, max.			596.15
Pvap	8.03e-05	kPa	184.99	Calculated Property
Pvap	0.02	kPa	230.67	Calculated Property
Pvap	0.74	kPa	276.36	Calculated Property
Pvap	8.05	kPa	322.04	Calculated Property
Pvap	43.90	kPa	367.73	Calculated Property
Pvap	154.89	kPa	413.41	Calculated Property
Pvap	409.94	kPa	459.10	Calculated Property
Pvap	892.49	kPa	504.78	Calculated Property
Pvap	1697.38	kPa	550.47	Calculated Property
Pvap	2937.27	kPa	596.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[855.72; 433.01]	kg/m3	[184.99; 574.51]	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			6.10639e+01
Coefficient B			2.50290e-01
Coefficient C			5.96150e+02
Coefficient D			2.65820e-01
Temperature range, min.			184.99
Temperature range, max.			574.51
ρl	855.72	kg/m3	184.99	Calculated Property
ρl	825.00	kg/m3	228.27	Calculated Property
ρl	792.75	kg/m3	271.55	Calculated Property
ρl	758.64	kg/m3	314.83	Calculated Property
ρl	722.16	kg/m3	358.11	Calculated Property
ρl	682.58	kg/m3	401.39	Calculated Property
ρl	638.68	kg/m3	444.67	Calculated Property
ρl	588.20	kg/m3	487.95	Calculated Property
ρl	526.01	kg/m3	531.23	Calculated Property
ρl	433.01	kg/m3	574.51	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 9.49e-04]	N/m	[184.99; 574.51]	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			-1.39950e-02
Coefficient B			2.14160e+01
Coefficient C			-2.96890e+00
Coefficient D			-2.92980e-04
Coefficient E			-3.34330e-06
Temperature range, min.			184.99
Temperature range, max.			574.51
γ	0.03	N/m	184.99	Calculated Property
γ	0.03	N/m	228.27	Calculated Property
γ	0.03	N/m	271.55	Calculated Property
γ	0.02	N/m	314.83	Calculated Property
γ	0.02	N/m	358.11	Calculated Property
γ	0.01	N/m	401.39	Calculated Property
γ	0.01	N/m	444.67	Calculated Property
γ	0.01	N/m	487.95	Calculated Property
γ	0.00	N/m	531.23	Calculated Property
γ	9.49e-04	N/m	574.51	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.09]	W/m×K	[184.99; 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			1.46590e-02
Coefficient B			3.59600e-01
Coefficient C			2.83110e+01
Coefficient D			8.46250e+05
Temperature range, min.			184.99
Temperature range, max.			1000.00
λgas	0.00	W/m×K	184.99	Calculated Property
λgas	0.01	W/m×K	275.55	Calculated Property
λgas	0.02	W/m×K	366.10	Calculated Property
λgas	0.03	W/m×K	456.66	Calculated Property
λgas	0.04	W/m×K	547.22	Calculated Property
λgas	0.05	W/m×K	637.77	Calculated Property
λgas	0.06	W/m×K	728.33	Calculated Property
λgas	0.07	W/m×K	818.89	Calculated Property
λgas	0.08	W/m×K	909.44	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.05]	W/m×K	[184.99; 596.15]	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			-9.69660e-02
Coefficient B			-4.68560e+00
Coefficient C			-1.26780e+00
Coefficient D			-7.54240e-04
Coefficient E			-4.79620e-07
Temperature range, min.			184.99
Temperature range, max.			596.15
λliquid	0.14	W/m×K	184.99	Calculated Property
λliquid	0.13	W/m×K	230.67	Calculated Property
λliquid	0.12	W/m×K	276.36	Calculated Property
λliquid	0.11	W/m×K	322.04	Calculated Property
λliquid	0.10	W/m×K	367.73	Calculated Property
λliquid	0.09	W/m×K	413.41	Calculated Property
λliquid	0.08	W/m×K	459.10	Calculated Property
λliquid	0.07	W/m×K	504.78	Calculated Property
λliquid	0.06	W/m×K	550.47	Calculated Property
λliquid	0.05	W/m×K	596.15	Calculated Property

Similar Compounds

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

Mixtures

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

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.
• 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
• 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
• 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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