Chemical Properties of Indane (CAS 496-11-7)

InChI

InChI=1S/C9H10/c1-2-5-9-7-3-6-8(9)4-1/h1-2,4-5H,3,6-7H2

InChI Key

PQNFLJBBNBOBRQ-UHFFFAOYSA-N

Formula

C9H10

SMILES

c1ccc2c(c1)CCC2

Molecular Weight¹

118.18

CAS

496-11-7

Other Names

• 1,2-Hydrindene
• 1H-Indene, 2,3-dihydro-
• 2,3-Dihydroindene
• 2,3-dihydro-1H-indene
• Benzocyclopentane
• Hydrindene
• Hydrindonaphthene
• NSC 5292
• indan
• indene, 2,3-dihydro-

• 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).
• 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).
• 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°_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	[0.2913; 0.3092]
ω	0.2913		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3092		ChemSep v8.3 pure component data Compiled value
ω	0.3080		KDB
ΔcH°liquid	[-4982.50; -4981.60]	kJ/mol
ΔcH°liquid	-4982.50 ± 1.40	kJ/mol	NIST
ΔcH°liquid	-4981.60 ± 2.00	kJ/mol	NIST
μ	0.54	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	166.80	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[59.70; 60.90]	kJ/mol
ΔfH°gas	60.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	60.90 ± 2.10	kJ/mol	NIST
ΔfH°gas	60.70 ± 1.50	kJ/mol	NIST
ΔfH°gas	59.70 ± 2.00	kJ/mol	NIST
ΔfH°liquid	[10.70; 11.70]	kJ/mol
ΔfH°liquid	11.70 ± 1.80	kJ/mol	NIST
ΔfH°liquid	11.70 ± 1.50	kJ/mol	NIST
ΔfH°liquid	10.70 ± 2.00	kJ/mol	NIST
ΔfusH°	9.78	kJ/mol	Joback Calculated Property
ΔvapH°	[48.80; 49.20]	kJ/mol
ΔvapH°	48.80	kJ/mol	NIST
ΔvapH°	49.20 ± 1.00	kJ/mol	NIST
ΔvapH°	49.00	kJ/mol	NIST
ΔvapH°	49.03 ± 0.20	kJ/mol	NIST
IE	[8.45; 9.05]	eV
IE	8.60 ± 0.10	eV	NIST
IE	8.60 ± 0.01	eV	NIST
IE	8.52	eV	NIST
IE	Outlier 9.05 ± 0.05	eV	NIST
IE	8.50	eV	NIST
IE	8.46 ± 0.03	eV	NIST
IE	8.45 ± 0.02	eV	NIST
IE	8.46	eV	NIST
log10WS	[-3.04; -3.03]
log10WS	-3.03		Aq. Solubility Prediction
log10WS	-3.04		Estimated Solubility
logPoct/wat	2.175		Crippen Calculated Property
McVol	103.050	ml/mol	McGowan Calculated Property
Pc	[3789.56; 3950.00]	kPa
Pc	3950.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Pc	Outlier 3789.56	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3950.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3950.00	kPa	KDB
Pc	3950.00 ± 40.00	kPa	NIST
Pc	3950.00 ± 30.00	kPa	NIST
Ptriple	1.53e-04	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[165.50; 1066.70]
Inp	1050.80		NIST
Inp	1066.70		NIST
Inp	982.00		NIST
Inp	1059.00		NIST
Inp	1058.00		NIST
Inp	1016.00		NIST
Inp	1012.00		NIST
Inp	1015.70		NIST
Inp	1043.00		NIST
Inp	1052.00		NIST
Inp	1018.00		NIST
Inp	1011.20		NIST
Inp	1014.50		NIST
Inp	1027.40		NIST
Inp	1036.10		NIST
Inp	1046.00		NIST
Inp	1017.00		NIST
Inp	1011.00		NIST
Inp	1011.20		NIST
Inp	1018.00		NIST
Inp	1019.00		NIST
Inp	1011.00		NIST
Inp	1014.00		NIST
Inp	1011.20		NIST
Inp	1014.50		NIST
Inp	1033.00		NIST
Inp	1018.00		NIST
Inp	1011.80		NIST
Inp	1051.00		NIST
Inp	1034.00		NIST
Inp	1013.00		NIST
Inp	1058.00		NIST
Inp	1019.45		NIST
Inp	1022.00		NIST
Inp	1020.00		NIST
Inp	1030.00		NIST
Inp	1024.50		NIST
Inp	1027.40		NIST
Inp	1032.40		NIST
Inp	1035.50		NIST
Inp	1047.80		NIST
Inp	1017.40		NIST
Inp	1027.40		NIST
Inp	1032.40		NIST
Inp	1035.50		NIST
Inp	1015.41		NIST
Inp	1015.61		NIST
Inp	1016.00		NIST
Inp	1028.00		NIST
Inp	1036.00		NIST
Inp	1007.28		NIST
Inp	1013.03		NIST
Inp	1016.71		NIST
Inp	1030.81		NIST
Inp	1036.70		NIST
Inp	1041.08		NIST
Inp	1013.00		NIST
Inp	1039.25		NIST
Inp	1038.00		NIST
Inp	1046.00		NIST
Inp	1027.00		NIST
Inp	1027.00		NIST
Inp	1036.00		NIST
Inp	1036.00		NIST
Inp	1019.00		NIST
Inp	1032.00		NIST
Inp	1026.00		NIST
Inp	1029.00		NIST
Inp	1020.00		NIST
Inp	1023.00		NIST
Inp	1027.00		NIST
Inp	1002.00		NIST
Inp	1033.00		NIST
Inp	1017.00		NIST
Inp	1022.00		NIST
Inp	1029.00		NIST
Inp	1034.00		NIST
Inp	1041.00		NIST
Inp	1048.00		NIST
Inp	1016.00		NIST
Inp	1013.00		NIST
Inp	1013.00		NIST
Inp	1036.00		NIST
Inp	1040.00		NIST
Inp	1014.00		NIST
Inp	1018.00		NIST
Inp	1021.00		NIST
Inp	Outlier 169.04		NIST
Inp	Outlier 169.10		NIST
Inp	Outlier 168.83		NIST
Inp	Outlier 170.21		NIST
Inp	Outlier 168.87		NIST
Inp	Outlier 165.50		NIST
Inp	Outlier 167.82		NIST
Inp	Outlier 168.87		NIST
Inp	Outlier 169.87		NIST
Inp	1020.00		NIST
Inp	1035.50		NIST
Inp	1036.00		NIST
Inp	1036.70		NIST
Inp	1046.00		NIST
Inp	1019.00		NIST
Inp	1034.00		NIST
Inp	1013.00		NIST
Inp	1021.00		NIST
Ip	[1355.90; 1382.00]
Ip	1355.90		NIST
Ip	1382.00		NIST
Ip	1365.00		NIST
Ip	1370.00		NIST
Ip	1356.00		NIST
Ip	1365.00		NIST
Ip	1377.00		NIST
Ip	1355.90		NIST
Ip	1356.00		NIST
S°liquid	[234.34; 234.35]	J/mol×K
S°liquid	234.35	J/mol×K	NIST
S°liquid	234.34	J/mol×K	NIST
Tboil	[449.15; 451.12]	K
Tboil	451.00	K	ChemSep v8.3 pure component data Compiled value
Tboil	451.12	K	KDB
Tboil	449.20	K	NIST
Tboil	451.00	K	NIST
Tboil	451.00	K	NIST
Tboil	449.15 ± 0.50	K	NIST
Tboil	449.65 ± 1.00	K	NIST
Tboil	451.00 ± 0.15	K	NIST
Tboil	450.97 ± 0.20	K	NIST
Tboil	449.40 ± 0.50	K	NIST
Tboil	450.15 ± 0.50	K	NIST
Tc	[684.90; 684.90]	K
Tc	684.90	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Tc	684.90	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	684.90	K	ChemSep v8.3 pure component data Compiled value
Tc	684.90	K	KDB
Tc	684.90 ± 0.50	K	NIST
Tc	684.90	K	NIST
Tc	684.90 ± 0.40	K	NIST
Tfus	[221.46; 221.95]	K
Tfus	221.95	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	221.74	K	ChemSep v8.3 pure component data Compiled value
Tfus	221.70	K	KDB
Tfus	221.95	K	Aq. Solubility Prediction
Tfus	221.46 ± 0.40	K	NIST
Ttriple	[221.74; 221.79]	K
Ttriple	221.79	K	Thermodynamic properties of indan: Experimental and computational results
Ttriple	221.74	K	ChemSep v8.3 pure component data Compiled value
Ttriple	221.77 ± 0.02	K	NIST
Ttriple	221.77 ± 0.02	K	NIST
UQi	3.11		ChemSep v8.3 pure component data Compiled value
URi	4.66		ChemSep v8.3 pure component data Compiled value
Vc	[0.384; 0.393]	m3/kmol
Vc	0.384	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.393	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2730000		ChemSep v8.3 pure component data Compiled value
Zra	0.26		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[193.64; 228.37]	J/mol×K	[435.65; 523.15]
Cp,gas	193.64 ± 0.39	J/mol×K	435.65	NIST
Cp,gas	199.15 ± 0.39	J/mol×K	448.15	NIST
Cp,gas	209.22 ± 0.39	J/mol×K	473.15	NIST
Cp,gas	219.20 ± 0.39	J/mol×K	498.15	NIST
Cp,gas	228.37 ± 0.39	J/mol×K	523.15	NIST
Cp,liquid	[170.40; 199.80]	J/mol×K	[240.00; 320.00]
Cp,liquid	170.40	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	173.20	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
Cp,liquid	176.20	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	179.50	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	180.60	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	183.10	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	186.90	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	190.20	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	190.25	J/mol×K	298.15	NIST
Cp,liquid	190.25	J/mol×K	298.15	NIST
Cp,liquid	191.00	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
Cp,liquid	195.30	J/mol×K	310.00	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	199.80	J/mol×K	320.00	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	[8.60; 8.60]	kJ/mol	[221.77; 221.80]
ΔfusH	8.60	kJ/mol	221.77	NIST
ΔfusH	8.60	kJ/mol	221.80	NIST
ΔfusH	8.60	kJ/mol	221.80	NIST
ΔvapH	[39.63; 45.00]	kJ/mol	[418.50; 451.00]
ΔvapH	45.00	kJ/mol	418.50	NIST
ΔvapH	44.00	kJ/mol	420.00	NIST
ΔvapH	39.63	kJ/mol	451.00	NIST
n0	1.53580		298.15	KDB
ΔfusS	38.77	J/mol×K	221.77	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[84.31; 390.94]	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			6.03210e+01
Coefficient B			-6.43060e+02
Coefficient C			6.42924e+00
Coefficient D			-1.88070e-04
Coefficient E			3.66770e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	84.31	J/mol×K	200.00	Calculated Property
Cp,gas	150.51	J/mol×K	344.44	Calculated Property
Cp,gas	213.36	J/mol×K	488.89	Calculated Property
Cp,gas	262.57	J/mol×K	633.33	Calculated Property
Cp,gas	299.78	J/mol×K	777.78	Calculated Property
Cp,gas	327.98	J/mol×K	922.22	Calculated Property
Cp,gas	349.63	J/mol×K	1066.67	Calculated Property
Cp,gas	366.54	J/mol×K	1211.11	Calculated Property
Cp,gas	380.00	J/mol×K	1355.56	Calculated Property
Cp,gas	390.94	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[165.55; 250.54]	J/mol×K	[221.74; 451.12]	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			1.36380e+02
Coefficient B			-2.94780e+01
Coefficient C			1.15304e+00
Coefficient D			1.30500e-02
Coefficient E			-1.09930e-05
Temperature range, min.			221.74
Temperature range, max.			451.12
Cp,liquid	165.55	J/mol×K	221.74	Calculated Property
Cp,liquid	172.55	J/mol×K	247.23	Calculated Property
Cp,liquid	180.47	J/mol×K	272.71	Calculated Property
Cp,liquid	189.27	J/mol×K	298.20	Calculated Property
Cp,liquid	198.83	J/mol×K	323.69	Calculated Property
Cp,liquid	208.99	J/mol×K	349.17	Calculated Property
Cp,liquid	219.53	J/mol×K	374.66	Calculated Property
Cp,liquid	230.18	J/mol×K	400.15	Calculated Property
Cp,liquid	240.63	J/mol×K	425.63	Calculated Property
Cp,liquid	250.54	J/mol×K	451.12	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0136247; 0.0001698]	Pa×s	[221.74; 547.92]	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			-1.51950e+02
Coefficient B			6.81020e+03
Coefficient C			2.18630e+01
Coefficient D			-2.34200e-05
Coefficient E			2.00000e+00
Temperature range, min.			221.74
Temperature range, max.			547.92
η	0.0136247	Pa×s	221.74	Calculated Property
η	0.0033196	Pa×s	257.98	Calculated Property
η	0.0014239	Pa×s	294.22	Calculated Property
η	0.0008389	Pa×s	330.47	Calculated Property
η	0.0005892	Pa×s	366.71	Calculated Property
η	0.0004529	Pa×s	402.95	Calculated Property
η	0.0003611	Pa×s	439.19	Calculated Property
η	0.0002884	Pa×s	475.44	Calculated Property
η	0.0002255	Pa×s	511.68	Calculated Property
η	0.0001698	Pa×s	547.92	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[53.42; 0.00]	kJ/mol	[221.74; 684.90]	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			6.20670e+01
Coefficient B			-4.58740e-03
Coefficient C			2.08170e+00
Coefficient D			-3.24760e+00
Coefficient E			1.60130e+00
Critical temperature, Tc (K)			6.84900e+02
Temperature range, min.			221.74
Temperature range, max.			684.90
ΔvapH	53.42	kJ/mol	221.74	Calculated Property
ΔvapH	50.36	kJ/mol	273.20	Calculated Property
ΔvapH	47.30	kJ/mol	324.66	Calculated Property
ΔvapH	44.26	kJ/mol	376.13	Calculated Property
ΔvapH	41.19	kJ/mol	427.59	Calculated Property
ΔvapH	37.89	kJ/mol	479.05	Calculated Property
ΔvapH	34.02	kJ/mol	530.51	Calculated Property
ΔvapH	28.98	kJ/mol	581.98	Calculated Property
ΔvapH	21.50	kJ/mol	633.44	Calculated Property
ΔvapH	0.00	kJ/mol	684.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[329.70; 451.73]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.67689e+01
Coefficient B			-4.58687e+03
Coefficient C			-5.13930e+01
Temperature range, min.			329.70
Temperature range, max.			451.73
Pvap	1.33	kPa	329.70	Calculated Property
Pvap	2.87	kPa	343.26	Calculated Property
Pvap	5.76	kPa	356.82	Calculated Property
Pvap	10.91	kPa	370.38	Calculated Property
Pvap	19.60	kPa	383.94	Calculated Property
Pvap	33.65	kPa	397.49	Calculated Property
Pvap	55.45	kPa	411.05	Calculated Property
Pvap	88.14	kPa	424.61	Calculated Property
Pvap	135.60	kPa	438.17	Calculated Property
Pvap	202.63	kPa	451.73	Calculated Property
Pvap	[1.70e-04; 4018.25]	kPa	[221.74; 684.90]	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			9.01143e+01
Coefficient B			-8.79505e+03
Coefficient C			-1.10025e+01
Coefficient D			6.10513e-06
Coefficient E			2.00000e+00
Temperature range, min.			221.74
Temperature range, max.			684.90
Pvap	1.70e-04	kPa	221.74	Calculated Property
Pvap	0.04	kPa	273.20	Calculated Property
Pvap	1.04	kPa	324.66	Calculated Property
Pvap	10.50	kPa	376.13	Calculated Property
Pvap	54.97	kPa	427.59	Calculated Property
Pvap	190.73	kPa	479.05	Calculated Property
Pvap	505.90	kPa	530.51	Calculated Property
Pvap	1122.36	kPa	581.98	Calculated Property
Pvap	2209.56	kPa	633.44	Calculated Property
Pvap	4018.25	kPa	684.90	Calculated Property
Pvap	[1.58e-04; 3939.29]	kPa	[221.74; 684.90]	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			8.37734e+01
Coefficient B			-8.59035e+03
Coefficient C			-1.00029e+01
Coefficient D			5.02936e-06
Coefficient E			0.00000e+00
Temperature range, min.			221.74
Temperature range, max.			684.90
Pvap	1.58e-04	kPa	221.74	Calculated Property
Pvap	0.03	kPa	273.20	Calculated Property
Pvap	1.00	kPa	324.66	Calculated Property
Pvap	10.28	kPa	376.13	Calculated Property
Pvap	54.81	kPa	427.59	Calculated Property
Pvap	192.46	kPa	479.05	Calculated Property
Pvap	512.86	kPa	530.51	Calculated Property
Pvap	1134.21	kPa	581.98	Calculated Property
Pvap	2208.10	kPa	633.44	Calculated Property
Pvap	3939.29	kPa	684.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1022.14; 298.63]	kg/m3	[221.74; 684.90]	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			7.51917e+01
Coefficient B			2.51790e-01
Coefficient C			6.84900e+02
Coefficient D			2.91650e-01
Temperature range, min.			221.74
Temperature range, max.			684.90
ρl	1022.14	kg/m3	221.74	Calculated Property
ρl	980.54	kg/m3	273.20	Calculated Property
ρl	937.01	kg/m3	324.66	Calculated Property
ρl	891.07	kg/m3	376.13	Calculated Property
ρl	842.02	kg/m3	427.59	Calculated Property
ρl	788.78	kg/m3	479.05	Calculated Property
ρl	729.47	kg/m3	530.51	Calculated Property
ρl	660.31	kg/m3	581.98	Calculated Property
ρl	571.05	kg/m3	633.44	Calculated Property
ρl	298.63	kg/m3	684.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 5.54e-06]	N/m	[221.74; 677.95]	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			-9.44030e-03
Coefficient B			8.15880e+01
Coefficient C			-3.36640e+00
Coefficient D			1.37890e-03
Coefficient E			-5.11500e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 684.9 K.
Temperature range, min.			221.74
Temperature range, max.			677.95
γ	0.04	N/m	221.74	Calculated Property
γ	0.04	N/m	272.43	Calculated Property
γ	0.03	N/m	323.12	Calculated Property
γ	0.03	N/m	373.81	Calculated Property
γ	0.02	N/m	424.50	Calculated Property
γ	0.02	N/m	475.19	Calculated Property
γ	0.01	N/m	525.88	Calculated Property
γ	0.01	N/m	576.57	Calculated Property
γ	0.00	N/m	627.26	Calculated Property
γ	5.54e-06	N/m	677.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.08]	W/m×K	[221.74; 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			8.95270e-03
Coefficient B			4.34470e-01
Coefficient C			6.17910e+02
Coefficient D			7.64370e+05
Temperature range, min.			221.74
Temperature range, max.			1000.00
λgas	0.00	W/m×K	221.74	Calculated Property
λgas	0.01	W/m×K	308.21	Calculated Property
λgas	0.02	W/m×K	394.69	Calculated Property
λgas	0.02	W/m×K	481.16	Calculated Property
λgas	0.03	W/m×K	567.63	Calculated Property
λgas	0.04	W/m×K	654.11	Calculated Property
λgas	0.05	W/m×K	740.58	Calculated Property
λgas	0.06	W/m×K	827.05	Calculated Property
λgas	0.07	W/m×K	913.53	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.10]	W/m×K	[221.74; 451.12]	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			-4.13180e-02
Coefficient B			5.70980e+00
Coefficient C			-1.53690e+00
Coefficient D			-4.36390e-04
Coefficient E			-1.01950e-06
Temperature range, min.			221.74
Temperature range, max.			451.12
λliquid	0.15	W/m×K	221.74	Calculated Property
λliquid	0.14	W/m×K	247.23	Calculated Property
λliquid	0.14	W/m×K	272.71	Calculated Property
λliquid	0.13	W/m×K	298.20	Calculated Property
λliquid	0.13	W/m×K	323.69	Calculated Property
λliquid	0.12	W/m×K	349.17	Calculated Property
λliquid	0.12	W/m×K	374.66	Calculated Property
λliquid	0.11	W/m×K	400.15	Calculated Property
λliquid	0.11	W/m×K	425.63	Calculated Property
λliquid	0.10	W/m×K	451.12	Calculated Property

Similar Compounds

Find more compounds similar to Indane.

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 3 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 3. Aromatic Hydrocarbons. J. Chem. Eng. Data 1995, 40, 547-558.
• 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.
• 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
• Thermodynamic properties of indan: Experimental and computational results
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• 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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