Chemical Properties of Cyclohexane, 1,4-dimethyl-, trans- (CAS 2207-04-7)

InChI

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

InChI Key

QRMPKOFEUHIBNM-ZKCHVHJHSA-N

Formula

C8H16

SMILES

C[C@H]1CC[C@H](C)CC1

Molecular Weight¹

112.22

CAS

2207-04-7

Other Names

• 1,4(trans)-dimethylcyclohexane
• 1,4-Dimethylcyclohexane, trans-
• 1,trans-4-dimethylcyclohexane
• Cyclohexane, trans-1,4-dimethyl-
• t-1,4-Dimethylcyclohexane
• trans-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	[0.2419; 0.2502]
ω	0.2502		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2419		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2429		ChemSep v8.3 pure component data Compiled value
ω	0.2420		KDB
AP	325.850	K	KDB
ΔcH°liquid	-5212.30 ± 1.70	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[31.71; 31.74]	kJ/mol
ΔfG°	31.71	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	31.74	kJ/mol	KDB
Δc,grossH	5212.34	kJ/mol	KDB
Δc,netH	4860.260	kJ/mol	KDB
ΔfH°gas	[-184.70; -184.60]	kJ/mol
ΔfH°gas	-184.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-184.70	kJ/mol	KDB
ΔfusH°	9.38	kJ/mol	Joback Calculated Property
ΔvapH°	[37.60; 39.90]	kJ/mol
ΔvapH°	37.95	kJ/mol	NIST
ΔvapH°	37.60	kJ/mol	NIST
ΔvapH°	37.90	kJ/mol	NIST
ΔvapH°	39.90 ± 0.10	kJ/mol	NIST
ΔvapH°	37.87	kJ/mol	NIST
IE	[9.56; 9.92]	eV
IE	9.56	eV	NIST
IE	9.92 ± 0.05	eV	NIST
log10WS	-4.47		Estimated Solubility
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	2940.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2970.00	kPa	KDB
Ptriple	0.04	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[736.00; 816.70]
Inp	Outlier 816.70		NIST
Inp	765.00		NIST
Inp	802.60		NIST
Inp	Outlier 808.00		NIST
Inp	780.00		NIST
Inp	780.20		NIST
Inp	780.30		NIST
Inp	780.50		NIST
Inp	779.90		NIST
Inp	Outlier 816.00		NIST
Inp	774.00		NIST
Inp	779.00		NIST
Inp	784.00		NIST
Inp	788.00		NIST
Inp	784.90		NIST
Inp	786.20		NIST
Inp	790.30		NIST
Inp	774.90		NIST
Inp	777.20		NIST
Inp	779.60		NIST
Inp	782.00		NIST
Inp	785.60		NIST
Inp	772.00		NIST
Inp	774.00		NIST
Inp	776.00		NIST
Inp	779.00		NIST
Inp	781.00		NIST
Inp	784.00		NIST
Inp	780.20		NIST
Inp	780.50		NIST
Inp	785.00		NIST
Inp	777.00		NIST
Inp	777.00		NIST
Inp	777.00		NIST
Inp	784.10		NIST
Inp	791.90		NIST
Inp	790.20		NIST
Inp	790.80		NIST
Inp	800.00		NIST
Inp	783.00		NIST
Inp	786.00		NIST
Inp	788.00		NIST
Inp	791.00		NIST
Inp	794.00		NIST
Inp	785.00		NIST
Inp	783.00		NIST
Inp	796.00		NIST
Inp	781.00		NIST
Inp	789.00		NIST
Inp	796.00		NIST
Inp	772.00		NIST
Inp	800.00		NIST
Inp	774.50		NIST
Inp	778.50		NIST
Inp	772.09		NIST
Inp	770.39		NIST
Inp	775.60		NIST
Inp	776.70		NIST
Inp	777.30		NIST
Inp	785.40		NIST
Inp	776.70		NIST
Inp	775.60		NIST
Inp	776.70		NIST
Inp	777.30		NIST
Inp	774.00		NIST
Inp	772.00		NIST
Inp	790.00		NIST
Inp	779.00		NIST
Inp	774.00		NIST
Inp	779.00		NIST
Inp	774.00		NIST
Inp	773.00		NIST
Inp	784.60		NIST
Inp	786.10		NIST
Inp	788.40		NIST
Inp	790.20		NIST
Inp	791.70		NIST
Inp	793.10		NIST
Inp	Outlier 736.00		NIST
Inp	774.00		NIST
Inp	765.00		NIST
Inp	772.00		NIST
Inp	778.00		NIST
Inp	785.00		NIST
Inp	779.00		NIST
Inp	784.60		NIST
Inp	793.10		NIST
S°gas	365.89	J/mol×K	NIST
S°liquid	268.03	J/mol×K	NIST
Tboil	[392.00; 397.15]	K
Tboil	392.51	K	ChemSep v8.3 pure component data Compiled value
Tboil	392.50	K	KDB
Tboil	392.50	K	NIST
Tboil	392.80 ± 0.50	K	NIST
Tboil	392.00 ± 2.00	K	NIST
Tboil	392.70 ± 1.00	K	NIST
Tboil	392.00 ± 2.00	K	NIST
Tboil	393.00 ± 2.00	K	NIST
Tboil	393.00 ± 2.00	K	NIST
Tboil	392.78 ± 0.20	K	NIST
Tboil	392.00 ± 3.00	K	NIST
Tboil	Outlier 397.15 ± 0.50	K	NIST
Tboil	392.48 ± 0.50	K	NIST
Tboil	392.50 ± 0.15	K	NIST
Tboil	392.48 ± 0.30	K	NIST
Tboil	392.80 ± 0.50	K	NIST
Tboil	392.48 ± 0.30	K	NIST
Tboil	392.50 ± 0.02	K	NIST
Tboil	392.50 ± 0.25	K	NIST
Tboil	392.75 ± 0.30	K	NIST
Tboil	392.78 ± 0.30	K	NIST
Tboil	392.70 ± 2.00	K	NIST
Tc	[585.84; 5877.70]	K
Tc	585.84	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	587.70	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Tc	587.70	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	589.82	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	590.15	K	ChemSep v8.3 pure component data Compiled value
Tc	587.70	K	KDB
Tc	Outlier 5877.70 ± 0.50	K	NIST
Tc	590.00	K	NIST
Tc	587.70 ± 0.58	K	NIST
Tfus	[186.15; 242.21]	K
Tfus	Outlier 186.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	236.21	K	ChemSep v8.3 pure component data Compiled value
Tfus	236.20	K	KDB
Tfus	236.21 ± 0.50	K	NIST
Tfus	236.23 ± 0.06	K	NIST
Tfus	242.21 ± 0.20	K	NIST
Tfus	236.05 ± 0.02	K	NIST
Tfus	235.85 ± 0.30	K	NIST
Tfus	236.15 ± 2.00	K	NIST
Ttriple	[236.21; 236.23]	K
Ttriple	236.23	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	236.21	K	ChemSep v8.3 pure component data Compiled value
Ttriple	236.22 ± 0.02	K	NIST
Ttriple	236.22 ± 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	[0.450; 0.450]	m3/kmol
Vc	0.450	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.450	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.450	m3/kmol	KDB
Zc	[0.2710000; 0.2735120]
Zc	0.2710000		ChemSep v8.3 pure component data Compiled value
Zc	0.2735120		KDB
Zra	0.26		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[186.60; 211.20]	J/mol×K	[240.00; 300.00]
Cp,liquid	186.60	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	190.10	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	193.80	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	202.00	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	210.30	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	210.25	J/mol×K	298.15	NIST
Cp,liquid	211.20	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	[12.33; 12.34]	kJ/mol	[236.20; 236.22]
ΔfusH	12.34	kJ/mol	236.20	NIST
ΔfusH	12.34	kJ/mol	236.20	NIST
ΔfusH	12.33	kJ/mol	236.22	NIST
ΔfusH	12.33	kJ/mol	236.22	NIST
ΔvapH	[32.56; 36.70]	kJ/mol	[341.00; 392.50]
ΔvapH	35.60 ± 0.10	kJ/mol	341.00	NIST
ΔvapH	36.70	kJ/mol	354.00	NIST
ΔvapH	34.60 ± 0.10	kJ/mol	357.00	NIST
ΔvapH	33.50 ± 0.10	kJ/mol	377.00	NIST
ΔvapH	32.59	kJ/mol	392.50	KDB
ΔvapH	32.56	kJ/mol	392.50	NIST
n0	1.41853		298.15	KDB
ρl	763.00	kg/m3	293.00	KDB
ΔfusS	[52.21; 52.21]	J/mol×K	[236.22; 236.22]
ΔfusS	52.21	J/mol×K	236.22	NIST
ΔfusS	52.21	J/mol×K	236.22	NIST
γ	0.02	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[113.93; 494.86]	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			9.79790e+01
Coefficient B			-8.30680e+02
Coefficient C			7.02724e+00
Coefficient D			-5.52380e-04
Coefficient E			1.50560e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	113.93	J/mol×K	200.00	Calculated Property
Cp,gas	183.02	J/mol×K	344.44	Calculated Property
Cp,gas	261.03	J/mol×K	488.89	Calculated Property
Cp,gas	325.26	J/mol×K	633.33	Calculated Property
Cp,gas	374.06	J/mol×K	777.78	Calculated Property
Cp,gas	410.65	J/mol×K	922.22	Calculated Property
Cp,gas	438.54	J/mol×K	1066.67	Calculated Property
Cp,gas	460.55	J/mol×K	1211.11	Calculated Property
Cp,gas	478.80	J/mol×K	1355.56	Calculated Property
Cp,gas	494.86	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[185.45; 266.88]	J/mol×K	[236.21; 392.51]	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			1.19770e+02
Coefficient B			1.86950e+02
Coefficient C			1.05264e+00
Coefficient D			1.15540e-02
Coefficient E			-6.96330e-06
Temperature range, min.			236.21
Temperature range, max.			392.51
Cp,liquid	185.45	J/mol×K	236.21	Calculated Property
Cp,liquid	191.43	J/mol×K	253.58	Calculated Property
Cp,liquid	198.18	J/mol×K	270.94	Calculated Property
Cp,liquid	205.69	J/mol×K	288.31	Calculated Property
Cp,liquid	213.97	J/mol×K	305.68	Calculated Property
Cp,liquid	223.02	J/mol×K	323.04	Calculated Property
Cp,liquid	232.84	J/mol×K	340.41	Calculated Property
Cp,liquid	243.44	J/mol×K	357.78	Calculated Property
Cp,liquid	254.79	J/mol×K	375.14	Calculated Property
Cp,liquid	266.88	J/mol×K	392.51	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0018699; 0.0001571]	Pa×s	[236.21; 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			-8.79460e+00
Coefficient B			1.11380e+03
Coefficient C			-4.13140e-01
Coefficient D			9.87670e-07
Coefficient E			2.00000e+00
Temperature range, min.			236.21
Temperature range, max.			472.00
η	0.0018699	Pa×s	236.21	Calculated Property
η	0.0011326	Pa×s	262.41	Calculated Property
η	0.0007514	Pa×s	288.61	Calculated Property
η	0.0005340	Pa×s	314.81	Calculated Property
η	0.0004005	Pa×s	341.01	Calculated Property
η	0.0003133	Pa×s	367.20	Calculated Property
η	0.0002538	Pa×s	393.40	Calculated Property
η	0.0002115	Pa×s	419.60	Calculated Property
η	0.0001805	Pa×s	445.80	Calculated Property
η	0.0001571	Pa×s	472.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[41.14; 5.66]	kJ/mol	[236.21; 587.70]	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			5.56480e+01
Coefficient B			9.53600e-01
Coefficient C			-1.37470e+00
Coefficient D			1.39270e+00
Coefficient E			-5.56060e-01
Critical temperature, Tc (K)			5.90150e+02
Temperature range, min.			236.21
Temperature range, max.			587.70
ΔvapH	41.14	kJ/mol	236.21	Calculated Property
ΔvapH	39.17	kJ/mol	275.26	Calculated Property
ΔvapH	37.12	kJ/mol	314.32	Calculated Property
ΔvapH	34.91	kJ/mol	353.37	Calculated Property
ΔvapH	32.50	kJ/mol	392.43	Calculated Property
ΔvapH	29.79	kJ/mol	431.48	Calculated Property
ΔvapH	26.66	kJ/mol	470.54	Calculated Property
ΔvapH	22.85	kJ/mol	509.59	Calculated Property
ΔvapH	17.65	kJ/mol	548.65	Calculated Property
ΔvapH	5.66	kJ/mol	587.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[282.89; 420.53]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38145e+01
Coefficient B			-3.15127e+03
Coefficient C			-4.99260e+01
Temperature range, min.			282.89
Temperature range, max.			420.53
Pvap	1.33	kPa	282.89	Calculated Property
Pvap	3.07	kPa	298.18	Calculated Property
Pvap	6.41	kPa	313.48	Calculated Property
Pvap	12.35	kPa	328.77	Calculated Property
Pvap	22.22	kPa	344.06	Calculated Property
Pvap	37.73	kPa	359.36	Calculated Property
Pvap	60.95	kPa	374.65	Calculated Property
Pvap	94.30	kPa	389.94	Calculated Property
Pvap	140.53	kPa	405.24	Calculated Property
Pvap	202.63	kPa	420.53	Calculated Property
Pvap	[0.04; 3033.44]	kPa	[236.21; 587.70]	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			7.86547e+01
Coefficient B			-7.07805e+03
Coefficient C			-9.54705e+00
Coefficient D			6.60253e-06
Coefficient E			2.00000e+00
Temperature range, min.			236.21
Temperature range, max.			587.70
Pvap	0.04	kPa	236.21	Calculated Property
Pvap	0.83	kPa	275.26	Calculated Property
Pvap	6.61	kPa	314.32	Calculated Property
Pvap	30.93	kPa	353.37	Calculated Property
Pvap	101.15	kPa	392.43	Calculated Property
Pvap	258.73	kPa	431.48	Calculated Property
Pvap	557.07	kPa	470.54	Calculated Property
Pvap	1061.06	kPa	509.59	Calculated Property
Pvap	1851.26	kPa	548.65	Calculated Property
Pvap	3033.44	kPa	587.70	Calculated Property
Pvap	[0.04; 3006.30]	kPa	[236.21; 590.15]	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			7.42070e+01
Coefficient B			-6.91805e+03
Coefficient C			-8.84557e+00
Coefficient D			5.63363e-06
Coefficient E			0.00000e+00
Temperature range, min.			236.21
Temperature range, max.			590.15
Pvap	0.04	kPa	236.21	Calculated Property
Pvap	0.84	kPa	275.54	Calculated Property
Pvap	6.77	kPa	314.86	Calculated Property
Pvap	31.81	kPa	354.19	Calculated Property
Pvap	104.16	kPa	393.52	Calculated Property
Pvap	266.07	kPa	432.84	Calculated Property
Pvap	570.32	kPa	472.17	Calculated Property
Pvap	1078.11	kPa	511.50	Calculated Property
Pvap	1860.78	kPa	550.82	Calculated Property
Pvap	3006.30	kPa	590.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[802.45; 270.25]	kg/m3	[236.21; 587.70]	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			7.25477e+00
Coefficient B			8.78850e-02
Coefficient C			5.90150e+02
Coefficient D			1.30930e-01
Temperature range, min.			236.21
Temperature range, max.			587.70
ρl	802.45	kg/m3	236.21	Calculated Property
ρl	775.20	kg/m3	275.26	Calculated Property
ρl	745.92	kg/m3	314.32	Calculated Property
ρl	714.12	kg/m3	353.37	Calculated Property
ρl	679.07	kg/m3	392.43	Calculated Property
ρl	639.62	kg/m3	431.48	Calculated Property
ρl	593.79	kg/m3	470.54	Calculated Property
ρl	537.54	kg/m3	509.59	Calculated Property
ρl	459.98	kg/m3	548.65	Calculated Property
ρl	270.25	kg/m3	587.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 4.52e-06]	N/m	[236.21; 583.48]	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			-8.77810e-02
Coefficient B			-2.40690e+01
Coefficient C			-1.69890e+00
Coefficient D			-1.67060e-03
Coefficient E			8.28480e-07
Comment			Range stopped where the equation turns negative; ChemSep gives it to 587.7 K.
Temperature range, min.			236.21
Temperature range, max.			583.48
γ	0.03	N/m	236.21	Calculated Property
γ	0.02	N/m	274.80	Calculated Property
γ	0.02	N/m	313.38	Calculated Property
γ	0.02	N/m	351.97	Calculated Property
γ	0.01	N/m	390.55	Calculated Property
γ	0.01	N/m	429.14	Calculated Property
γ	0.01	N/m	467.72	Calculated Property
γ	0.00	N/m	506.31	Calculated Property
γ	0.00	N/m	544.90	Calculated Property
γ	4.52e-06	N/m	583.48	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.09]	W/m×K	[236.21; 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			1.24960e-02
Coefficient B			3.79390e-01
Coefficient C			-8.40500e-01
Coefficient D			8.11480e+05
Temperature range, min.			236.21
Temperature range, max.			1000.00
λgas	0.01	W/m×K	236.21	Calculated Property
λgas	0.01	W/m×K	321.08	Calculated Property
λgas	0.02	W/m×K	405.94	Calculated Property
λgas	0.03	W/m×K	490.81	Calculated Property
λgas	0.04	W/m×K	575.67	Calculated Property
λgas	0.05	W/m×K	660.54	Calculated Property
λgas	0.06	W/m×K	745.40	Calculated Property
λgas	0.07	W/m×K	830.27	Calculated Property
λgas	0.08	W/m×K	915.13	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.13; 0.09]	W/m×K	[236.21; 392.51]	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			-1.54580e-03
Coefficient B			-7.18430e+01
Coefficient C			-1.10730e+00
Coefficient D			-2.78310e-03
Coefficient E			1.55120e-07
Temperature range, min.			236.21
Temperature range, max.			392.51
λliquid	0.13	W/m×K	236.21	Calculated Property
λliquid	0.12	W/m×K	253.58	Calculated Property
λliquid	0.12	W/m×K	270.94	Calculated Property
λliquid	0.12	W/m×K	288.31	Calculated Property
λliquid	0.11	W/m×K	305.68	Calculated Property
λliquid	0.11	W/m×K	323.04	Calculated Property
λliquid	0.10	W/m×K	340.41	Calculated Property
λliquid	0.10	W/m×K	357.78	Calculated Property
λliquid	0.10	W/m×K	375.14	Calculated Property
λliquid	0.09	W/m×K	392.51	Calculated Property

Similar Compounds

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

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).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 ChEDL chemicals 1.5.2, from Daubert, T. E. Vapor-Liquid Critical Properties of Elements and Compounds. 5. Branched Alkanes and Cycloalkanes. J. Chem. Eng. Data 1996, 41, 365-372.
• 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
• 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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