Chemical Properties of Indene (CAS 95-13-6)

InChI

InChI=1S/C9H8/c1-2-5-9-7-3-6-8(9)4-1/h1-6H,7H2

InChI Key

YBYIRNPNPLQARY-UHFFFAOYSA-N

Formula

C9H8

SMILES

C1=Cc2ccccc2C1

Molecular Weight¹

116.16

CAS

95-13-6

Other Names

• 1H-indene
• INDEN
• INDONAPHTHENE

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• BasG : Gas basicity (kJ/mol).
• 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).
• EA : Electron affinity (eV).
• 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).
• 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	[0.2571; 0.3338]
ω	0.2571		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3338		ChemSep v8.3 pure component data Compiled value
ω	0.2620		KDB
PAff	[848.50; 848.80]	kJ/mol
PAff	848.80	kJ/mol	NIST
PAff	848.50	kJ/mol	NIST
BasG	[819.20; 819.60]	kJ/mol
BasG	819.60	kJ/mol	NIST
BasG	819.20	kJ/mol	NIST
ΔcH°liquid	-4795.50 ± 1.30	kJ/mol	NIST
μ	0.67	debye	ChemSep v8.3 pure component data Compiled value
EA	0.17 ± 0.03	eV	NIST
ΔfG°	233.96	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[161.20; 163.28]	kJ/mol
ΔfH°gas	163.28	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	161.20 ± 2.30	kJ/mol	NIST
ΔfH°liquid	[110.00; 110.60]	kJ/mol
ΔfH°liquid	110.60 ± 1.80	kJ/mol	NIST
ΔfH°liquid	110.00 ± 1.00	kJ/mol	NIST
ΔfusH°	11.00	kJ/mol	Joback Calculated Property
ΔvapH°	50.60 ± 1.50	kJ/mol	NIST
IE	[8.13; 8.62]	eV
IE	8.14 ± 0.01	eV	NIST
IE	8.33 ± 0.01	eV	NIST
IE	8.14 ± 0.01	eV	NIST
IE	Outlier 8.62	eV	NIST
IE	8.13 ± 0.05	eV	NIST
IE	8.15 ± 0.01	eV	NIST
logPoct/wat	2.256		Crippen Calculated Property
McVol	98.750	ml/mol	McGowan Calculated Property
Pc	[3799.69; 3820.00]	kPa
Pc	3799.69	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3820.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3800.00	kPa	KDB
Ptriple	0.02	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[168.80; 1072.50]
Inp	1059.00		NIST
Inp	1052.00		NIST
Inp	1059.00		NIST
Inp	1036.00		NIST
Inp	1015.00		NIST
Inp	1016.00		NIST
Inp	1034.00		NIST
Inp	1034.00		NIST
Inp	1031.00		NIST
Inp	1034.00		NIST
Inp	1031.00		NIST
Inp	1035.00		NIST
Inp	1026.00		NIST
Inp	1018.00		NIST
Inp	1013.00		NIST
Inp	1023.30		NIST
Inp	1059.00		NIST
Inp	1049.00		NIST
Inp	1059.00		NIST
Inp	1023.00		NIST
Inp	1011.80		NIST
Inp	1015.70		NIST
Inp	1034.10		NIST
Inp	1043.30		NIST
Inp	1053.80		NIST
Inp	1021.00		NIST
Inp	1011.80		NIST
Inp	1015.70		NIST
Inp	1016.90		NIST
Inp	1016.90		NIST
Inp	1017.00		NIST
Inp	1017.50		NIST
Inp	1060.00		NIST
Inp	1030.00		NIST
Inp	1062.00		NIST
Inp	1026.00		NIST
Inp	1037.00		NIST
Inp	1072.50		NIST
Inp	1069.00		NIST
Inp	1041.00		NIST
Inp	1045.00		NIST
Inp	1054.00		NIST
Inp	1011.00		NIST
Inp	1014.00		NIST
Inp	1036.00		NIST
Inp	1033.00		NIST
Inp	1051.00		NIST
Inp	1049.00		NIST
Inp	1039.00		NIST
Inp	1025.00		NIST
Inp	1024.00		NIST
Inp	1025.00		NIST
Inp	1042.00		NIST
Inp	1036.00		NIST
Inp	1060.00		NIST
Inp	1060.00		NIST
Inp	1041.00		NIST
Inp	1059.00		NIST
Inp	1031.00		NIST
Inp	1037.00		NIST
Inp	1020.00		NIST
Inp	1042.00		NIST
Inp	1045.00		NIST
Inp	1017.00		NIST
Inp	1059.00		NIST
Inp	1062.00		NIST
Inp	Outlier 171.05		NIST
Inp	Outlier 173.26		NIST
Inp	Outlier 172.05		NIST
Inp	Outlier 172.51		NIST
Inp	Outlier 170.83		NIST
Inp	Outlier 169.00		NIST
Inp	Outlier 168.80		NIST
Inp	Outlier 170.08		NIST
Inp	1026.00		NIST
Inp	1045.00		NIST
Inp	1059.00		NIST
Inp	1016.00		NIST
Inp	1031.00		NIST
Inp	1023.30		NIST
Inp	1011.80		NIST
Inp	1021.00		NIST
Inp	1017.00		NIST
Inp	1030.00		NIST
Inp	1060.00		NIST
Inp	1054.00		NIST
Inp	1037.00		NIST
Inp	Outlier 169.00		NIST
Inp	Outlier 171.05		NIST
Ip	[1430.80; 1479.00]
Ip	1455.80		NIST
Ip	1430.80		NIST
Ip	1431.00		NIST
Ip	1471.00		NIST
Ip	1466.00		NIST
Ip	1472.00		NIST
Ip	1467.00		NIST
Ip	1479.00		NIST
Ip	1467.00		NIST
Ip	1431.00		NIST
S°liquid	[214.18; 215.35]	J/mol×K
S°liquid	214.18	J/mol×K	NIST
S°liquid	215.35	J/mol×K	NIST
Tboil	[450.00; 455.80]	K
Tboil	455.77	K	ChemSep v8.3 pure component data Compiled value
Tboil	455.59	K	KDB
Tboil	454.80	K	NIST
Tboil	455.80	K	NIST
Tboil	455.45 ± 0.50	K	NIST
Tboil	455.72 ± 0.15	K	NIST
Tboil	455.59 ± 0.30	K	NIST
Tboil	455.75 ± 0.30	K	NIST
Tboil	455.60 ± 0.50	K	NIST
Tboil	453.20 ± 1.50	K	NIST
Tboil	450.90 ± 1.50	K	NIST
Tboil	454.00 ± 1.00	K	NIST
Tboil	Outlier 450.00 ± 3.00	K	NIST
Tc	[687.00; 695.15]	K
Tc	695.15	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	687.00	K	ChemSep v8.3 pure component data Compiled value
Tc	695.15	K	KDB
Tfus	[270.48; 271.70]	K
Tfus	271.25	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	271.70	K	ChemSep v8.3 pure component data Compiled value
Tfus	271.00	K	KDB
Tfus	271.40 ± 0.50	K	NIST
Tfus	270.48 ± 0.30	K	NIST
Ttriple	[271.70; 271.70]	K
Ttriple	271.70	K	ChemSep v8.3 pure component data Compiled value
Ttriple	271.70 ± 0.02	K	NIST
Ttriple	271.70 ± 0.02	K	NIST
UQi	2.89		ChemSep v8.3 pure component data Compiled value
URi	4.43		ChemSep v8.3 pure component data Compiled value
Vc	[0.368; 0.368]	m3/kmol
Vc	0.368	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.368	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.368	m3/kmol	KDB
Zc	[0.2422730; 0.2460000]
Zc	0.2460000		ChemSep v8.3 pure component data Compiled value
Zc	0.2422730		KDB
Zra	0.26		ChemSep v8.3 pure component data Compiled value

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[181.00; 211.00]	J/mol×K	[280.00; 370.00]
Cp,liquid	181.00	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	184.00	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	186.94	J/mol×K	298.15	NIST
Cp,liquid	187.00	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	186.94	J/mol×K	298.15	NIST
Cp,liquid	188.00	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	191.00	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	194.00	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
Cp,liquid	198.00	J/mol×K	330.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	201.00	J/mol×K	340.00	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	205.00	J/mol×K	350.00	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	208.00	J/mol×K	360.00	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	211.00	J/mol×K	370.00	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	[10.20; 10.20]	kJ/mol	[271.70; 271.70]
ΔfusH	10.20	kJ/mol	271.70	NIST
ΔfusH	10.20	kJ/mol	271.70	NIST
ΔfusH	10.20	kJ/mol	271.70	NIST
ΔvapH	[43.60; 45.30]	kJ/mol	[372.00; 413.00]
ΔvapH	43.60	kJ/mol	372.00	NIST
ΔvapH	43.90	kJ/mol	391.50	NIST
ΔvapH	45.30	kJ/mol	413.00	NIST
n0	1.57370		298.15	KDB
ρl	998.99	kg/m3	293.10	KDB
ΔfusS	37.55	J/mol×K	271.70	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[81.54; 350.75]	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			5.45980e+01
Coefficient B			-5.72630e+02
Coefficient C			6.16924e+00
Coefficient D			-6.23040e-05
Coefficient E			-1.40840e-09
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	81.54	J/mol×K	200.00	Calculated Property
Cp,gas	143.29	J/mol×K	344.44	Calculated Property
Cp,gas	198.22	J/mol×K	488.89	Calculated Property
Cp,gas	240.47	J/mol×K	633.33	Calculated Property
Cp,gas	272.42	J/mol×K	777.78	Calculated Property
Cp,gas	296.77	J/mol×K	922.22	Calculated Property
Cp,gas	315.55	J/mol×K	1066.67	Calculated Property
Cp,gas	330.19	J/mol×K	1211.11	Calculated Property
Cp,gas	341.68	J/mol×K	1355.56	Calculated Property
Cp,gas	350.75	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[178.25; 221.48]	J/mol×K	[271.70; 400.00]	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			8.76610e+01
Coefficient B			-1.86330e+01
Coefficient C			3.35024e+00
Coefficient D			5.61950e-03
Coefficient E			-4.09340e-06
Temperature range, min.			271.70
Temperature range, max.			400.00
Cp,liquid	178.25	J/mol×K	271.70	Calculated Property
Cp,liquid	182.99	J/mol×K	285.96	Calculated Property
Cp,liquid	187.77	J/mol×K	300.21	Calculated Property
Cp,liquid	192.60	J/mol×K	314.47	Calculated Property
Cp,liquid	197.44	J/mol×K	328.72	Calculated Property
Cp,liquid	202.30	J/mol×K	342.98	Calculated Property
Cp,liquid	207.14	J/mol×K	357.23	Calculated Property
Cp,liquid	211.97	J/mol×K	371.49	Calculated Property
Cp,liquid	216.75	J/mol×K	385.74	Calculated Property
Cp,liquid	221.48	J/mol×K	400.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0029065; 0.0002629]	Pa×s	[271.70; 455.77]	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			-1.36890e+02
Coefficient B			6.16540e+03
Coefficient C			1.96690e+01
Coefficient D			-2.54880e-05
Coefficient E			2.00000e+00
Temperature range, min.			271.70
Temperature range, max.			455.77
η	0.0029065	Pa×s	271.70	Calculated Property
η	0.0018441	Pa×s	292.15	Calculated Property
η	0.0012801	Pa×s	312.60	Calculated Property
η	0.0009472	Pa×s	333.06	Calculated Property
η	0.0007327	Pa×s	353.51	Calculated Property
η	0.0005840	Pa×s	373.96	Calculated Property
η	0.0004743	Pa×s	394.41	Calculated Property
η	0.0003891	Pa×s	414.87	Calculated Property
η	0.0003202	Pa×s	435.32	Calculated Property
η	0.0002629	Pa×s	455.77	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[55.64; 19.23]	kJ/mol	[271.70; 665.14]	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			1.12717e+02
Coefficient B			2.19563e+00
Coefficient C			-2.27889e+00
Coefficient D			7.82692e-01
Coefficient E			-2.31351e-01
Critical temperature, Tc (K)			6.87000e+02
Temperature range, min.			271.70
Temperature range, max.			665.14
ΔvapH	55.64	kJ/mol	271.70	Calculated Property
ΔvapH	50.95	kJ/mol	315.42	Calculated Property
ΔvapH	46.91	kJ/mol	359.13	Calculated Property
ΔvapH	43.37	kJ/mol	402.85	Calculated Property
ΔvapH	40.22	kJ/mol	446.56	Calculated Property
ΔvapH	37.32	kJ/mol	490.28	Calculated Property
ΔvapH	34.49	kJ/mol	533.99	Calculated Property
ΔvapH	31.40	kJ/mol	577.71	Calculated Property
ΔvapH	27.31	kJ/mol	621.42	Calculated Property
ΔvapH	19.23	kJ/mol	665.14	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[335.62; 481.24]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.67872e+01
Coefficient B			-5.48854e+03
Coefficient C			-2.97000e+00
Temperature range, min.			335.62
Temperature range, max.			481.24
Pvap	1.33	kPa	335.62	Calculated Property
Pvap	2.87	kPa	351.80	Calculated Property
Pvap	5.76	kPa	367.98	Calculated Property
Pvap	10.90	kPa	384.16	Calculated Property
Pvap	19.59	kPa	400.34	Calculated Property
Pvap	33.63	kPa	416.52	Calculated Property
Pvap	55.43	kPa	432.70	Calculated Property
Pvap	88.11	kPa	448.88	Calculated Property
Pvap	135.58	kPa	465.06	Calculated Property
Pvap	202.64	kPa	481.24	Calculated Property
Pvap	[0.02; 3820.00]	kPa	[271.70; 646.50]	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			1.91405e+02
Coefficient B			-1.32120e+04
Coefficient C			-2.64764e+01
Coefficient D			2.06314e-05
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 687 K.
Temperature range, min.			271.70
Temperature range, max.			646.50
Pvap	0.02	kPa	271.70	Calculated Property
Pvap	0.41	kPa	313.34	Calculated Property
Pvap	3.72	kPa	354.99	Calculated Property
Pvap	18.76	kPa	396.63	Calculated Property
Pvap	64.76	kPa	438.28	Calculated Property
Pvap	176.28	kPa	479.92	Calculated Property
Pvap	414.67	kPa	521.57	Calculated Property
Pvap	896.67	kPa	563.21	Calculated Property
Pvap	1860.69	kPa	604.86	Calculated Property
Pvap	3820.00	kPa	646.50	Calculated Property
Pvap	[0.02; 4302.94]	kPa	[271.70; 693.15]	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			1.22605e+02
Coefficient B			-1.05135e+04
Coefficient C			-1.58068e+01
Coefficient D			9.00394e-06
Coefficient E			0.00000e+00
Temperature range, min.			271.70
Temperature range, max.			693.15
Pvap	0.02	kPa	271.70	Calculated Property
Pvap	0.55	kPa	318.53	Calculated Property
Pvap	5.79	kPa	365.36	Calculated Property
Pvap	31.43	kPa	412.18	Calculated Property
Pvap	111.75	kPa	459.01	Calculated Property
Pvap	301.25	kPa	505.84	Calculated Property
Pvap	675.75	kPa	552.67	Calculated Property
Pvap	1342.06	kPa	599.49	Calculated Property
Pvap	2462.68	kPa	646.32	Calculated Property
Pvap	4302.94	kPa	693.15	Calculated Property
Pvap	[0.14; 101.54]	kPa	[289.60; 454.80]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.68898e+01
Coefficient B			-5.78283e+03
Coefficient C			1.65240e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			289.60
Temperature range, max.			454.80
Pvap	0.14	kPa	289.60	Calculated Property
Pvap	0.39	kPa	307.96	Calculated Property
Pvap	1.02	kPa	326.31	Calculated Property
Pvap	2.41	kPa	344.67	Calculated Property
Pvap	5.23	kPa	363.02	Calculated Property
Pvap	10.55	kPa	381.38	Calculated Property
Pvap	20.03	kPa	399.73	Calculated Property
Pvap	36.02	kPa	418.09	Calculated Property
Pvap	61.76	kPa	436.44	Calculated Property
Pvap	101.54	kPa	454.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1017.79; 504.36]	kg/m3	[271.70; 665.14]	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			7.96554e+01
Coefficient B			2.53410e-01
Coefficient C			6.87000e+02
Coefficient D			3.09140e-01
Temperature range, min.			271.70
Temperature range, max.			665.14
ρl	1017.79	kg/m3	271.70	Calculated Property
ρl	978.17	kg/m3	315.42	Calculated Property
ρl	936.92	kg/m3	359.13	Calculated Property
ρl	893.67	kg/m3	402.85	Calculated Property
ρl	847.88	kg/m3	446.56	Calculated Property
ρl	798.76	kg/m3	490.28	Calculated Property
ρl	744.97	kg/m3	533.99	Calculated Property
ρl	684.10	kg/m3	577.71	Calculated Property
ρl	610.64	kg/m3	621.42	Calculated Property
ρl	504.36	kg/m3	665.14	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 7.11e-04]	N/m	[271.70; 665.14]	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			-8.48940e-03
Coefficient B			1.35540e+02
Coefficient C			-3.72640e+00
Coefficient D			2.62690e-03
Coefficient E			-6.58470e-06
Temperature range, min.			271.70
Temperature range, max.			665.14
γ	0.04	N/m	271.70	Calculated Property
γ	0.04	N/m	315.42	Calculated Property
γ	0.03	N/m	359.13	Calculated Property
γ	0.02	N/m	402.85	Calculated Property
γ	0.02	N/m	446.56	Calculated Property
γ	0.02	N/m	490.28	Calculated Property
γ	0.01	N/m	533.99	Calculated Property
γ	0.01	N/m	577.71	Calculated Property
γ	0.00	N/m	621.42	Calculated Property
γ	7.11e-04	N/m	665.14	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.07]	W/m×K	[271.70; 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			7.51650e-05
Coefficient B			1.05500e+00
Coefficient C			5.58890e+02
Coefficient D			3.53550e+04
Temperature range, min.			271.70
Temperature range, max.			1000.00
λgas	0.01	W/m×K	271.70	Calculated Property
λgas	0.01	W/m×K	352.62	Calculated Property
λgas	0.02	W/m×K	433.54	Calculated Property
λgas	0.02	W/m×K	514.47	Calculated Property
λgas	0.03	W/m×K	595.39	Calculated Property
λgas	0.04	W/m×K	676.31	Calculated Property
λgas	0.05	W/m×K	757.23	Calculated Property
λgas	0.05	W/m×K	838.16	Calculated Property
λgas	0.06	W/m×K	919.08	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.11]	W/m×K	[271.70; 455.77]	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			-3.41450e-03
Coefficient B			-8.04590e+01
Coefficient C			-9.15710e-01
Coefficient D			-2.44080e-03
Coefficient E			2.39910e-07
Temperature range, min.			271.70
Temperature range, max.			455.77
λliquid	0.15	W/m×K	271.70	Calculated Property
λliquid	0.15	W/m×K	292.15	Calculated Property
λliquid	0.14	W/m×K	312.60	Calculated Property
λliquid	0.14	W/m×K	333.06	Calculated Property
λliquid	0.14	W/m×K	353.51	Calculated Property
λliquid	0.13	W/m×K	373.96	Calculated Property
λliquid	0.13	W/m×K	394.41	Calculated Property
λliquid	0.12	W/m×K	414.87	Calculated Property
λliquid	0.12	W/m×K	435.32	Calculated Property
λliquid	0.11	W/m×K	455.77	Calculated Property

Similar Compounds

Find more compounds similar to Indene.

Mixtures

• Indene + Water

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).
• 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
• Crippen Method
• Liquid-Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass
• 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
• 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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