Chemical Properties of Cyclopentane, 1,3-dimethyl-, trans- (CAS 1759-58-6)

InChI

InChI=1S/C7H14/c1-6-3-4-7(2)5-6/h6-7H,3-5H2,1-2H3/t6-,7-/m0/s1

InChI Key

XAZKFISIRYLAEE-BQBZGAKWSA-N

Formula

C7H14

SMILES

CC1CCC(C)C1

Molecular Weight¹

98.19

CAS

1759-58-6

Other Names

• 1,3-Dimethylcyclopentane, trans
• 1,trans-3-Dimethylcyclopentane
• 1-trans-3-dimethylcyclopentane
• t-1,3-Dimethylcyclopentane
• trans-1,3-Dimethylcyclopentane

• ω : Acentric Factor.
• 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).
• C_sat : Molar heat capacity at saturation pressure (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase 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).
• 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°_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).
• V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
• ω_SRK : SRK acentric factor.
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2480; 0.2584]
ω	0.2480		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2584		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2530		ChemSep v8.3 pure component data Compiled value
ΔcH°liquid	-4585.20 ± 1.10	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	41.46	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-135.90; -133.60]	kJ/mol
ΔfH°gas	-133.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-135.90 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-170.20 ± 1.20	kJ/mol	NIST
ΔfusH°	8.89	kJ/mol	Joback Calculated Property
ΔvapH°	[34.30; 34.50]	kJ/mol
ΔvapH°	34.50	kJ/mol	NIST
ΔvapH°	34.30	kJ/mol	NIST
IE	9.47	eV	Relay (1.0) Calculated Property
log10WS	-4.29		Relay (1.0) Calculated Property
logPoct/wat	2.442		Crippen Calculated Property
McVol	98.630	ml/mol	McGowan Calculated Property
Pc	[3300.16; 3447.38]	kPa
Pc	3300.16	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3447.38	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	3400.00	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	4.38e-08	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[676.00; 698.00]
Inp	678.00		NIST
Inp	691.30		NIST
Inp	682.00		NIST
Inp	684.00		NIST
Inp	687.00		NIST
Inp	692.00		NIST
Inp	686.30		NIST
Inp	688.70		NIST
Inp	689.10		NIST
Inp	692.00		NIST
Inp	688.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	684.50		NIST
Inp	686.20		NIST
Inp	687.90		NIST
Inp	689.70		NIST
Inp	680.00		NIST
Inp	684.00		NIST
Inp	687.00		NIST
Inp	689.00		NIST
Inp	690.00		NIST
Inp	690.00		NIST
Inp	688.30		NIST
Inp	688.60		NIST
Inp	686.00		NIST
Inp	686.00		NIST
Inp	686.00		NIST
Inp	686.00		NIST
Inp	692.90		NIST
Inp	691.60		NIST
Inp	691.60		NIST
Inp	689.00		NIST
Inp	Outlier 697.00		NIST
Inp	689.00		NIST
Inp	692.00		NIST
Inp	687.00		NIST
Inp	690.00		NIST
Inp	686.00		NIST
Inp	688.00		NIST
Inp	689.00		NIST
Inp	691.00		NIST
Inp	693.00		NIST
Inp	687.50		NIST
Inp	686.00		NIST
Inp	Outlier 698.00		NIST
Inp	683.00		NIST
Inp	688.00		NIST
Inp	690.00		NIST
Inp	694.00		NIST
Inp	690.00		NIST
Inp	696.00		NIST
Inp	684.30		NIST
Inp	685.00		NIST
Inp	683.80		NIST
Inp	678.37		NIST
Inp	679.11		NIST
Inp	684.80		NIST
Inp	683.00		NIST
Inp	680.88		NIST
Inp	680.95		NIST
Inp	678.00		NIST
Inp	680.73		NIST
Inp	680.98		NIST
Inp	681.00		NIST
Inp	680.66		NIST
Inp	687.00		NIST
Inp	686.00		NIST
Inp	690.00		NIST
Inp	688.00		NIST
Inp	681.00		NIST
Inp	678.00		NIST
Inp	687.00		NIST
Inp	687.00		NIST
Inp	684.00		NIST
Inp	Outlier 676.00		NIST
Inp	690.00		NIST
Inp	680.66		NIST
Inp	684.30		NIST
Inp	696.00		NIST
Inp	687.00		NIST
S°liquid	271.54	J/mol×K	NIST
Tboil	[363.20; 364.91]	K
Tboil	363.90	K	ChemSep v8.3 pure component data Compiled value
Tboil	363.92	K	KDB
Tboil	364.90	K	NIST
Tboil	364.80 ± 0.60	K	NIST
Tboil	364.15 ± 1.50	K	NIST
Tboil	363.95 ± 0.30	K	NIST
Tboil	363.92 ± 0.02	K	NIST
Tboil	364.91 ± 0.50	K	NIST
Tboil	364.75 ± 0.50	K	NIST
Tboil	364.82 ± 0.30	K	NIST
Tboil	364.20 ± 0.30	K	NIST
Tboil	Outlier 363.20 ± 1.00	K	NIST
Tboil	363.95 ± 0.20	K	NIST
Tboil	363.85 ± 0.50	K	NIST
Tc	[552.00; 553.15]	K
Tc	552.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	553.15	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	553.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	[128.95; 139.47]	K
Tfus	139.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	139.18	K	ChemSep v8.3 pure component data Compiled value
Tfus	139.46	K	KDB
Tfus	138.15 ± 0.50	K	NIST
Tfus	139.18 ± 0.20	K	NIST
Tfus	130.25 ± 10.00	K	NIST
Tfus	130.45 ± 3.00	K	NIST
Tfus	128.95 ± 4.00	K	NIST
Tfus	139.17 ± 0.03	K	NIST
Tfus	139.16 ± 0.06	K	NIST
Tfus	139.25 ± 0.05	K	NIST
Tfus	139.47 ± 0.40	K	NIST
Ttriple	[139.18; 139.35]	K
Ttriple	139.18	K	ChemSep v8.3 pure component data Compiled value
Ttriple	139.35 ± 0.05	K	NIST
Ttriple	139.26 ± 0.03	K	NIST
UQi	3.77		ChemSep v8.3 pure component data Compiled value
URi	4.72		ChemSep v8.3 pure component data Compiled value
Vc	[0.363; 0.378]	m3/kmol
Vc	0.378	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.363	m3/kmol	ChemSep v8.3 pure component data Compiled value
VCOSTALD	0.38	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.27		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	0.2760000		ChemSep v8.3 pure component data Compiled value
Zra	[0.28; 0.28]
Zra	0.28		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.28		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	190.87	J/mol×K	304.03	NIST
Csat	[145.50; 189.20]	J/mol×K	[150.00; 300.00]
Csat	145.50	J/mol×K	150.00	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
Csat	147.10	J/mol×K	160.00	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
Csat	148.90	J/mol×K	170.00	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
Csat	150.90	J/mol×K	180.00	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
Csat	153.10	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
Csat	155.50	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
Csat	158.10	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
Csat	160.90	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
Csat	163.80	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
Csat	166.90	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
Csat	170.20	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
Csat	173.70	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
Csat	177.40	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
Csat	178.50	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
Csat	181.20	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
Csat	185.10	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
Csat	188.50	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
Csat	189.20	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	[7.40; 7.41]	kJ/mol	[139.48; 139.50]
ΔfusH	7.40	kJ/mol	139.48	NIST
ΔfusH	7.41	kJ/mol	139.50	NIST
ΔfusH	7.40	kJ/mol	139.50	NIST
ΔvapH	[34.00; 34.20]	kJ/mol	[328.00; 331.00]
ΔvapH	34.20	kJ/mol	328.00	NIST
ΔvapH	34.00	kJ/mol	331.00	NIST
ΔfusS	53.04	J/mol×K	139.48	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[99.53; 420.08]	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			8.63180e+01
Coefficient B			-8.31430e+02
Coefficient C			6.85024e+00
Coefficient D			-5.97820e-04
Coefficient E			1.82760e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	99.53	J/mol×K	200.00	Calculated Property
Cp,gas	156.58	J/mol×K	344.44	Calculated Property
Cp,gas	220.74	J/mol×K	488.89	Calculated Property
Cp,gas	273.51	J/mol×K	633.33	Calculated Property
Cp,gas	313.75	J/mol×K	777.78	Calculated Property
Cp,gas	344.28	J/mol×K	922.22	Calculated Property
Cp,gas	368.07	J/mol×K	1066.67	Calculated Property
Cp,gas	387.52	J/mol×K	1211.11	Calculated Property
Cp,gas	404.41	J/mol×K	1355.56	Calculated Property
Cp,gas	420.08	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[144.06; 218.96]	J/mol×K	[139.18; 364.88]	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			1.28140e+02
Coefficient B			2.15870e+02
Coefficient C			-1.70736e+00
Coefficient D			2.44600e-02
Coefficient E			-2.47890e-05
Temperature range, min.			139.18
Temperature range, max.			364.88
Cp,liquid	144.06	J/mol×K	139.18	Calculated Property
Cp,liquid	147.36	J/mol×K	164.26	Calculated Property
Cp,liquid	152.07	J/mol×K	189.34	Calculated Property
Cp,liquid	158.24	J/mol×K	214.41	Calculated Property
Cp,liquid	165.86	J/mol×K	239.49	Calculated Property
Cp,liquid	174.89	J/mol×K	264.57	Calculated Property
Cp,liquid	185.14	J/mol×K	289.65	Calculated Property
Cp,liquid	196.26	J/mol×K	314.72	Calculated Property
Cp,liquid	207.76	J/mol×K	339.80	Calculated Property
Cp,liquid	218.96	J/mol×K	364.88	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0221047; 0.0001240]	Pa×s	[139.18; 508.65]	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			-1.11520e+01
Coefficient B			9.96910e+02
Coefficient C			3.63740e-02
Coefficient D			-1.15450e-07
Coefficient E			2.00000e+00
Temperature range, min.			139.18
Temperature range, max.			508.65
η	0.0221047	Pa×s	139.18	Calculated Property
η	0.0043588	Pa×s	180.23	Calculated Property
η	0.0015708	Pa×s	221.28	Calculated Property
η	0.0007792	Pa×s	262.34	Calculated Property
η	0.0004672	Pa×s	303.39	Calculated Property
η	0.0003163	Pa×s	344.44	Calculated Property
η	0.0002325	Pa×s	385.49	Calculated Property
η	0.0001813	Pa×s	426.55	Calculated Property
η	0.0001475	Pa×s	467.60	Calculated Property
η	0.0001240	Pa×s	508.65	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[46.48; 0.00]	kJ/mol	[139.18; 553.00]	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			6.56856e+01
Coefficient B			1.54707e+00
Coefficient C			-1.42972e+00
Coefficient D			-1.59084e-03
Coefficient E			3.62451e-01
Critical temperature, Tc (K)			5.53000e+02
Temperature range, min.			139.18
Temperature range, max.			553.00
ΔvapH	46.48	kJ/mol	139.18	Calculated Property
ΔvapH	42.26	kJ/mol	185.16	Calculated Property
ΔvapH	38.74	kJ/mol	231.14	Calculated Property
ΔvapH	35.72	kJ/mol	277.12	Calculated Property
ΔvapH	33.02	kJ/mol	323.10	Calculated Property
ΔvapH	30.40	kJ/mol	369.08	Calculated Property
ΔvapH	27.53	kJ/mol	415.06	Calculated Property
ΔvapH	23.88	kJ/mol	461.04	Calculated Property
ΔvapH	18.28	kJ/mol	507.02	Calculated Property
ΔvapH	0.00	kJ/mol	553.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[263.68; 388.98]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43537e+01
Coefficient B			-3.17213e+03
Coefficient C			-3.81640e+01
Temperature range, min.			263.68
Temperature range, max.			388.98
Pvap	1.33	kPa	263.68	Calculated Property
Pvap	3.02	kPa	277.60	Calculated Property
Pvap	6.26	kPa	291.52	Calculated Property
Pvap	12.01	kPa	305.45	Calculated Property
Pvap	21.61	kPa	319.37	Calculated Property
Pvap	36.79	kPa	333.29	Calculated Property
Pvap	59.71	kPa	347.21	Calculated Property
Pvap	92.94	kPa	361.14	Calculated Property
Pvap	139.47	kPa	375.06	Calculated Property
Pvap	202.66	kPa	388.98	Calculated Property
Pvap	[1.84e-07; 3439.63]	kPa	[139.18; 553.00]	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			6.58062e+01
Coefficient B			-6.03890e+03
Coefficient C			-7.70900e+00
Coefficient D			6.35110e-06
Coefficient E			2.00000e+00
Temperature range, min.			139.18
Temperature range, max.			553.00
Pvap	1.84e-07	kPa	139.18	Calculated Property
Pvap	1.07e-03	kPa	185.16	Calculated Property
Pvap	0.14	kPa	231.14	Calculated Property
Pvap	3.14	kPa	277.12	Calculated Property
Pvap	25.44	kPa	323.10	Calculated Property
Pvap	114.59	kPa	369.08	Calculated Property
Pvap	357.02	kPa	415.06	Calculated Property
Pvap	875.47	kPa	461.04	Calculated Property
Pvap	1830.69	kPa	507.02	Calculated Property
Pvap	3439.63	kPa	553.00	Calculated Property
Pvap	[4.46e-08; 3465.01]	kPa	[139.18; 553.00]	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			9.09890e+01
Coefficient B			-7.10570e+03
Coefficient C			-1.15588e+01
Coefficient D			9.84000e-06
Coefficient E			0.00000e+00
Temperature range, min.			139.18
Temperature range, max.			553.00
Pvap	4.46e-08	kPa	139.18	Calculated Property
Pvap	6.11e-04	kPa	185.16	Calculated Property
Pvap	0.12	kPa	231.14	Calculated Property
Pvap	2.98	kPa	277.12	Calculated Property
Pvap	25.47	kPa	323.10	Calculated Property
Pvap	115.86	kPa	369.08	Calculated Property
Pvap	358.82	kPa	415.06	Calculated Property
Pvap	873.20	kPa	461.04	Calculated Property
Pvap	1824.39	kPa	507.02	Calculated Property
Pvap	3465.01	kPa	553.00	Calculated Property
Pvap	[6.35; 104.01]	kPa	[291.00; 364.82]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37534e+01
Coefficient B			-2.86369e+03
Coefficient C			-5.04380e+01
Reference			Forziati, Norris, et al., 1949, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			291.00
Temperature range, max.			364.82
Pvap	6.35	kPa	291.00	Calculated Property
Pvap	9.41	kPa	299.20	Calculated Property
Pvap	13.59	kPa	307.40	Calculated Property
Pvap	19.18	kPa	315.61	Calculated Property
Pvap	26.52	kPa	323.81	Calculated Property
Pvap	35.98	kPa	332.01	Calculated Property
Pvap	47.99	kPa	340.21	Calculated Property
Pvap	62.99	kPa	348.42	Calculated Property
Pvap	81.49	kPa	356.62	Calculated Property
Pvap	104.01	kPa	364.82	Calculated Property
Pvap	[6.35; 104.01]	kPa	[291.00; 364.82]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37534e+01
Coefficient B			-2.86369e+03
Coefficient C			-5.04380e+01
Reference			Forziati, Norris, et al., 1949
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			291.00
Temperature range, max.			364.82
Pvap	6.35	kPa	291.00	Calculated Property
Pvap	9.41	kPa	299.20	Calculated Property
Pvap	13.59	kPa	307.40	Calculated Property
Pvap	19.18	kPa	315.61	Calculated Property
Pvap	26.52	kPa	323.81	Calculated Property
Pvap	35.98	kPa	332.01	Calculated Property
Pvap	47.99	kPa	340.21	Calculated Property
Pvap	62.99	kPa	348.42	Calculated Property
Pvap	81.49	kPa	356.62	Calculated Property
Pvap	104.01	kPa	364.82	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[873.24; 272.73]	kg/m3	[139.18; 553.00]	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			7.65017e+01
Coefficient B			2.80500e-01
Coefficient C			5.53000e+02
Coefficient D			3.04660e-01
Temperature range, min.			139.18
Temperature range, max.			553.00
ρl	873.24	kg/m3	139.18	Calculated Property
ρl	838.15	kg/m3	185.16	Calculated Property
ρl	801.46	kg/m3	231.14	Calculated Property
ρl	762.79	kg/m3	277.12	Calculated Property
ρl	721.56	kg/m3	323.10	Calculated Property
ρl	676.86	kg/m3	369.08	Calculated Property
ρl	627.15	kg/m3	415.06	Calculated Property
ρl	569.31	kg/m3	461.04	Calculated Property
ρl	494.89	kg/m3	507.02	Calculated Property
ρl	272.73	kg/m3	553.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 1.39e-05]	N/m	[139.18; 547.21]	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			-1.08050e-02
Coefficient B			2.63240e+01
Coefficient C			-3.05710e+00
Coefficient D			-1.45380e-04
Coefficient E			-4.80210e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 553 K.
Temperature range, min.			139.18
Temperature range, max.			547.21
γ	0.04	N/m	139.18	Calculated Property
γ	0.03	N/m	184.52	Calculated Property
γ	0.03	N/m	229.85	Calculated Property
γ	0.02	N/m	275.19	Calculated Property
γ	0.02	N/m	320.53	Calculated Property
γ	0.01	N/m	365.86	Calculated Property
γ	0.01	N/m	411.20	Calculated Property
γ	0.01	N/m	456.53	Calculated Property
γ	0.00	N/m	501.87	Calculated Property
γ	1.39e-05	N/m	547.21	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.10]	W/m×K	[139.18; 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			2.14720e-03
Coefficient B			6.30730e-01
Coefficient C			2.13010e+02
Coefficient D			4.45470e+05
Temperature range, min.			139.18
Temperature range, max.			1000.00
λgas	0.00	W/m×K	139.18	Calculated Property
λgas	0.01	W/m×K	234.83	Calculated Property
λgas	0.01	W/m×K	330.47	Calculated Property
λgas	0.02	W/m×K	426.12	Calculated Property
λgas	0.04	W/m×K	521.77	Calculated Property
λgas	0.05	W/m×K	617.41	Calculated Property
λgas	0.06	W/m×K	713.06	Calculated Property
λgas	0.08	W/m×K	808.71	Calculated Property
λgas	0.09	W/m×K	904.35	Calculated Property
λgas	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.10]	W/m×K	[139.18; 364.88]	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			-3.40260e-02
Coefficient B			3.55100e+00
Coefficient C			-1.61560e+00
Coefficient D			-4.98830e-04
Coefficient E			-1.74750e-06
Temperature range, min.			139.18
Temperature range, max.			364.88
λliquid	0.15	W/m×K	139.18	Calculated Property
λliquid	0.14	W/m×K	164.26	Calculated Property
λliquid	0.14	W/m×K	189.34	Calculated Property
λliquid	0.13	W/m×K	214.41	Calculated Property
λliquid	0.13	W/m×K	239.49	Calculated Property
λliquid	0.12	W/m×K	264.57	Calculated Property
λliquid	0.12	W/m×K	289.65	Calculated Property
λliquid	0.11	W/m×K	314.72	Calculated Property
λliquid	0.10	W/m×K	339.80	Calculated Property
λliquid	0.10	W/m×K	364.88	Calculated Property

Similar Compounds

Find more compounds similar to Cyclopentane, 1,3-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).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• 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
• 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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