Chemical Properties of Propene (CAS 115-07-1)

InChI

InChI=1S/C3H6/c1-3-2/h3H,1H2,2H3

InChI Key

QQONPFPTGQHPMA-UHFFFAOYSA-N

Formula

C3H6

SMILES

C=CC

Molecular Weight¹

42.08

CAS

115-07-1

Other Names

• 1-Propene
• 1-Propylene
• CH3CH=CH2
• HC-1270
• Methylethene
• Methylethylene
• NCI-C50077
• R 1270
• UN 1077
• propylene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_gas : Standard gas 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).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• ρ_g : Gas Density (kg/m³).
• 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).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• 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.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.1376; 0.1480]
ω	0.1480		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.1477		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.1376		ChemSep v8.3 pure component data Compiled value
ω	0.1440		KDB
PAff	751.60	kJ/mol	NIST
Tig	770.37	K	KDB
BasG	722.70	kJ/mol	NIST
ΔcH°gas	[-2057.80; -2057.70]	kJ/mol
ΔcH°gas	-2057.80 ± 1.10	kJ/mol	NIST
ΔcH°gas	-2057.70 ± 0.60	kJ/mol	NIST
μ	[0.37; 0.40]	debye
μ	0.37	debye	ChemSep v8.3 pure component data Compiled value
μ	0.40	debye	KDB
LFL	2.00	% in Air	KDB
UFL	11.00	% in Air	KDB
Tflash,oc	165.37	K	KDB
ΔfG°	[62.64; 62.76]	kJ/mol
ΔfG°	62.64	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	62.76	kJ/mol	KDB
Rg	2.2280		KDB
ΔfH°gas	[20.23; 20.43]	kJ/mol
ΔfH°gas	20.37 ± 0.33	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	20.23	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	20.43	kJ/mol	KDB
ΔfH°gas	20.41	kJ/mol	NIST
ΔfH°gas	20.41	kJ/mol	NIST
ΔfusH°	2.25	kJ/mol	Joback Calculated Property
ΔvapH°	16.04	kJ/mol	NIST
IE	[9.69; 10.20]	eV
IE	9.73 ± 0.01	eV	NIST
IE	9.73	eV	NIST
IE	9.69 ± 0.09	eV	NIST
IE	9.73 ± 0.02	eV	NIST
IE	9.70 ± 0.10	eV	NIST
IE	9.73 ± 0.01	eV	NIST
IE	9.74 ± 0.00	eV	NIST
IE	9.72	eV	NIST
IE	9.72	eV	NIST
IE	9.74	eV	NIST
IE	9.74 ± 0.01	eV	NIST
IE	9.69	eV	NIST
IE	9.76	eV	NIST
IE	9.73 ± 0.01	eV	NIST
IE	9.74	eV	NIST
IE	9.73 ± 0.02	eV	NIST
IE	9.73	eV	NIST
IE	9.73 ± 0.01	eV	NIST
IE	9.91 ± 0.01	eV	NIST
IE	Outlier 10.20	eV	NIST
IE	10.03	eV	NIST
IE	Outlier 10.20	eV	NIST
IE	9.70	eV	NIST
IE	9.90	eV	NIST
IE	9.86	eV	NIST
log10WS	-1.08		Estimated Solubility
logPoct/wat	1.192		Crippen Calculated Property
McVol	48.830	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	1		KDB
NFPA Safety	1		KDB
Pc	[4555.00; 4664.60]	kPa
Pc	4630.00	kPa	Gas-Liquid Critical Properties of Ethylene + Hydrogen and Propylene + Hydrogen Binary Mixtures
Pc	4600.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Pc	4620.42	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4612.59	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	4600.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4555.00	kPa	Air Liquide Gas Encyclopedia
Pc	4600.00	kPa	KDB
Pc	4600.00 ± 30.00	kPa	NIST
Pc	4579.00 ± 15.00	kPa	NIST
Pc	Outlier 4664.60 ± 200.00	kPa	NIST
Pc	4621.00 ± 15.19	kPa	NIST
Pc	4594.68 ± 33.33	kPa	NIST
Ptriple	[7.44e-07; 950.00]	kPa
Ptriple	1.17e-06	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	7.44e-07	kPa	Air Liquide Gas Encyclopedia
Ptriple	9.50e-07	kPa	KDB
Ptriple	950.00 ± 15.00	kPa	NIST
ρc	[223.40; 233.50]	kg/m3
ρc	230.08	kg/m3	Air Liquide Gas Encyclopedia
ρc	228.07 ± 1.26	kg/m3	NIST
ρc	233.50 ± 2.95	kg/m3	NIST
ρc	223.40 ± 15.15	kg/m3	NIST
Inp	[280.00; 310.00]
Inp	292.00		NIST
Inp	294.00		NIST
Inp	300.00		NIST
Inp	289.00		NIST
Inp	283.30		NIST
Inp	287.00		NIST
Inp	289.00		NIST
Inp	287.00		NIST
Inp	287.00		NIST
Inp	288.00		NIST
Inp	288.00		NIST
Inp	289.00		NIST
Inp	283.00		NIST
Inp	290.00		NIST
Inp	295.00		NIST
Inp	294.00		NIST
Inp	286.00		NIST
Inp	294.00		NIST
Inp	295.00		NIST
Inp	295.00		NIST
Inp	295.00		NIST
Inp	295.00		NIST
Inp	298.00		NIST
Inp	290.00		NIST
Inp	288.00		NIST
Inp	290.00		NIST
Inp	290.00		NIST
Inp	283.00		NIST
Inp	290.00		NIST
Inp	290.00		NIST
Inp	283.00		NIST
Inp	Outlier 310.00		NIST
Inp	280.00		NIST
Inp	290.00		NIST
Inp	286.00		NIST
Inp	295.00		NIST
Inp	292.00		NIST
Inp	287.00		NIST
Inp	288.00		NIST
Inp	290.00		NIST
Inp	283.00		NIST
S°liquid	195.70	J/mol×K	NIST
Tboil	[224.95; 226.20]	K
Tboil	225.45	K	ChemSep v8.3 pure component data Compiled value
Tboil	225.53	K	Air Liquide Gas Encyclopedia
Tboil	225.46	K	KDB
Tboil	225.80	K	NIST
Tboil	225.50	K	NIST
Tboil	225.50 ± 0.60	K	NIST
Tboil	225.50 ± 0.50	K	NIST
Tboil	225.53 ± 0.38	K	NIST
Tboil	225.40 ± 0.30	K	NIST
Tboil	225.65 ± 0.50	K	NIST
Tboil	Outlier 226.20 ± 0.30	K	NIST
Tboil	Outlier 224.95 ± 0.60	K	NIST
Tc	[364.21; 365.75]	K
Tc	364.90	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	365.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	364.76	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	364.85	K	ChemSep v8.3 pure component data Compiled value
Tc	364.21	K	Air Liquide Gas Encyclopedia
Tc	364.90	K	KDB
Tc	364.90 ± 0.40	K	NIST
Tc	364.59 ± 0.50	K	NIST
Tc	365.57 ± 0.50	K	NIST
Tc	364.91 ± 0.20	K	NIST
Tc	365.30 ± 0.50	K	NIST
Tc	365.75 ± 0.50	K	NIST
Tfus	[87.89; 88.25]	K
Tfus	88.08	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	87.90	K	ChemSep v8.3 pure component data Compiled value
Tfus	87.89	K	Air Liquide Gas Encyclopedia
Tfus	87.90	K	KDB
Tfus	88.00 ± 0.30	K	NIST
Tfus	87.90 ± 0.40	K	NIST
Tfus	Outlier 88.25 ± 1.00	K	NIST
Tfus	87.95 ± 0.60	K	NIST
Ttriple	[86.85; 88.20]	K
Ttriple	87.86	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	87.89	K	ChemSep v8.3 pure component data Compiled value
Ttriple	87.95	K	Air Liquide Gas Encyclopedia
Ttriple	87.89	K	KDB
Ttriple	87.85 ± 0.02	K	NIST
Ttriple	87.89 ± 0.02	K	NIST
Ttriple	87.90 ± 0.30	K	NIST
Ttriple	Outlier 86.85 ± 0.06	K	NIST
Ttriple	88.20 ± 0.30	K	NIST
Ttriple	88.00 ± 0.40	K	NIST
UQi	2.02		ChemSep v8.3 pure component data Compiled value
URi	2.25		ChemSep v8.3 pure component data Compiled value
Vc	[0.181; 0.192]	m3/kmol
Vc	0.185	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Vc	0.181	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.185	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.185	m3/kmol	KDB
Vc	0.185	m3/kmol	NIST
Vc	Outlier 0.192 ± 0.005	m3/kmol	NIST
VCOSTALD	0.18	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.15		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2798850; 0.2810000]
Zc	0.2800000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Zc	0.2810000		ChemSep v8.3 pure component data Compiled value
Zc	0.2798850		KDB
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
Zra	0.28		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[44.52; 96.18]	J/mol×K	[148.20; 510.00]
Cp,gas	44.52	J/mol×K	148.20	NIST
Cp,gas	45.44	J/mol×K	157.60	NIST
Cp,gas	52.22	J/mol×K	213.10	NIST
Cp,gas	53.09	J/mol×K	220.10	NIST
Cp,gas	53.68	J/mol×K	223.70	NIST
Cp,gas	58.45	J/mol×K	258.00	NIST
Cp,gas	59.78	J/mol×K	270.00	NIST
Cp,gas	60.08 ± 0.13	J/mol×K	272.29	NIST
Cp,gas	61.45	J/mol×K	280.00	NIST
Cp,gas	63.43	J/mol×K	291.10	NIST
Cp,gas	63.79 ± 0.13	J/mol×K	298.15	NIST
Cp,gas	64.73 ± 0.13	J/mol×K	299.33	NIST
Cp,gas	64.71	J/mol×K	300.00	NIST
Cp,gas	67.89	J/mol×K	320.00	NIST
Cp,gas	67.88 ± 0.14	J/mol×K	323.15	NIST
Cp,gas	70.04 ± 0.17	J/mol×K	333.86	NIST
Cp,gas	71.03	J/mol×K	340.00	NIST
Cp,gas	71.78 ± 0.14	J/mol×K	348.15	NIST
Cp,gas	74.13	J/mol×K	360.00	NIST
Cp,gas	74.47 ± 0.15	J/mol×K	365.15	NIST
Cp,gas	75.02 ± 0.08	J/mol×K	367.11	NIST
Cp,gas	75.79 ± 0.15	J/mol×K	373.15	NIST
Cp,gas	79.85 ± 0.16	J/mol×K	378.15	NIST
Cp,gas	77.14	J/mol×K	380.00	NIST
Cp,gas	80.15	J/mol×K	400.00	NIST
Cp,gas	83.17	J/mol×K	420.00	NIST
Cp,gas	83.61 ± 0.17	J/mol×K	423.15	NIST
Cp,gas	86.09	J/mol×K	440.00	NIST
Cp,gas	87.44 ± 0.17	J/mol×K	448.15	NIST
Cp,gas	89.02	J/mol×K	460.00	NIST
Cp,gas	91.18 ± 0.18	J/mol×K	473.15	NIST
Cp,gas	91.91	J/mol×K	480.00	NIST
Cp,gas	94.76	J/mol×K	500.00	NIST
Cp,gas	96.18	J/mol×K	510.00	NIST
Cp,liquid	[87.00; 175.00]	J/mol×K	[90.00; 350.00]
Cp,liquid	92.68	J/mol×K	90.00	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	90.82	J/mol×K	100.00	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	89.37	J/mol×K	110.00	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	88.30	J/mol×K	120.00	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	87.57	J/mol×K	130.00	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	87.14	J/mol×K	140.00	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	87.00	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
Cp,liquid	87.09	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
Cp,liquid	87.40	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
Cp,liquid	87.88	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
Cp,liquid	88.51	J/mol×K	190.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	89.25	J/mol×K	200.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	90.08	J/mol×K	210.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	90.00	J/mol×K	210.30	NIST
Cp,liquid	91.00	J/mol×K	220.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	92.03	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	92.09	J/mol×K	230.00	NIST
Cp,liquid	93.18	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	94.47	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	95.90	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	97.49	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	98.02	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	99.25	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	101.20	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	102.00	J/mol×K	298.15	NIST
Cp,liquid	102.90	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	103.40	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	98.90	J/mol×K	300.00	NIST
Cp,liquid	105.70	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	109.00	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	118.00	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	138.00	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	175.00	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
ΔfusH	[2.93; 3.00]	kJ/mol	[87.85; 88.20]
ΔfusH	3.00	kJ/mol	87.85	NIST
ΔfusH	3.00	kJ/mol	87.85	NIST
ΔfusH	3.00	kJ/mol	87.85	NIST
ΔfusH	2.94	kJ/mol	87.89	Air Liquide Gas Encyclopedia
ΔfusH	2.93	kJ/mol	88.20	NIST
ΔfusH	2.93	kJ/mol	88.20	NIST
ΔfusH	2.93	kJ/mol	88.20	NIST
ΔvapH	[18.41; 22.20]	kJ/mol	[132.50; 360.50]
ΔvapH	22.20	kJ/mol	132.50	NIST
ΔvapH	19.60	kJ/mol	196.00	NIST
ΔvapH	19.20	kJ/mol	201.50	NIST
ΔvapH	18.42	kJ/mol	225.35	NIST
ΔvapH	18.42	kJ/mol	225.50	NIST
ΔvapH	18.47	kJ/mol	225.53	Air Liquide Gas Encyclopedia
ΔvapH	18.41	kJ/mol	225.70	KDB
ΔvapH	18.70	kJ/mol	249.50	NIST
ΔvapH	19.30	kJ/mol	259.50	NIST
ΔvapH	18.50	kJ/mol	298.50	NIST
ΔvapH	18.70	kJ/mol	330.00	NIST
ΔvapH	18.80	kJ/mol	344.00	NIST
ΔvapH	18.70	kJ/mol	360.50	NIST
Pvap	[1.10e-03; 2897.31]	kPa	[110.00; 340.00]
Pvap	1.10e-03	kPa	110.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	5.20e-03	kPa	120.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	0.03	kPa	130.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	0.12	kPa	140.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	0.41	kPa	150.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	1.21	kPa	160.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	3.07	kPa	170.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	6.93	kPa	180.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	14.18	kPa	190.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	26.76	kPa	200.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	47.11	kPa	210.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	78.23	kPa	220.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	123.61	kPa	230.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	187.14	kPa	240.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	273.12	kPa	250.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	307.20	kPa	253.05	Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
Pvap	386.13	kPa	260.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	428.70	kPa	263.15	Measurement of Vapor-Liquid Equilibria for the Pentafluoroethane + Propene Binary System from (263.15 to 323.15) K
Pvap	531.01	kPa	270.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	586.00	kPa	273.15	Measurement of vapor liquid equilibria for the binary mixture of propylene (R-1270) + propane (R-290)
Pvap	587.80	kPa	273.15	Measurement of Vapor-Liquid Equilibria for the Binary Mixture Difluoromethane (HFC-32) + Propylene (R-1270)
Pvap	673.60	kPa	278.15	Measurement of Vapor-Liquid Equilibria for the Pentafluoroethane + Propene Binary System from (263.15 to 323.15) K
Pvap	678.50	kPa	278.15	Measurement of vapor liquid equilibria for the binary mixture of propylene (R-1270) + propane (R-290)
Pvap	712.83	kPa	280.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	769.00	kPa	282.97	Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Pvap	780.80	kPa	283.15	Measurement of vapor liquid equilibria for the binary mixture of propylene (R-1270) + propane (R-290)
Pvap	781.20	kPa	283.15	Measurement of Vapor-Liquid Equilibria for the Binary Mixture Difluoromethane (HFC-32) + Propylene (R-1270)
Pvap	873.00	kPa	287.57	Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Pvap	936.86	kPa	290.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	1012.90	kPa	293.15	Measurement of Vapor-Liquid Equilibria for the Pentafluoroethane + Propene Binary System from (263.15 to 323.15) K
Pvap	1015.90	kPa	293.15	Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
Pvap	1019.00	kPa	293.15	Measurement of vapor liquid equilibria for the binary mixture of propylene (R-1270) + propane (R-290)
Pvap	1020.20	kPa	293.15	Measurement of Vapor-Liquid Equilibria for the Binary Mixture Difluoromethane (HFC-32) + Propylene (R-1270)
Pvap	1028.00	kPa	293.48	Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Pvap	1152.00	kPa	298.02	Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Pvap	1208.64	kPa	300.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	1291.00	kPa	302.83	Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Pvap	1308.20	kPa	303.15	Measurement of Vapor-Liquid Equilibria for the Binary Mixture Difluoromethane (HFC-32) + Propylene (R-1270)
Pvap	1307.60	kPa	303.15	Measurement of vapor liquid equilibria for the binary mixture of propylene (R-1270) + propane (R-290)
Pvap	1458.00	kPa	307.67	Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Pvap	1465.30	kPa	308.15	Measurement of Vapor-Liquid Equilibria for the Pentafluoroethane + Propene Binary System from (263.15 to 323.15) K
Pvap	1533.97	kPa	310.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	1650.80	kPa	313.15	Measurement of Vapor-Liquid Equilibria for the Binary Mixture Difluoromethane (HFC-32) + Propylene (R-1270)
Pvap	1652.20	kPa	313.15	Measurement of vapor liquid equilibria for the binary mixture of propylene (R-1270) + propane (R-290)
Pvap	1691.00	kPa	314.06	Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Pvap	1854.00	kPa	318.36	Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Pvap	1919.12	kPa	320.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	2039.00	kPa	322.91	Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Pvap	2047.90	kPa	323.15	Measurement of Vapor-Liquid Equilibria for the Pentafluoroethane + Propene Binary System from (263.15 to 323.15) K
Pvap	2058.90	kPa	323.27	Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + 1,2-Ethanediol and Propene + Acetophenone
Pvap	2239.00	kPa	327.27	Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
Pvap	2370.92	kPa	330.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
Pvap	2897.31	kPa	340.00	Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
ρg	[1.81; 2.36]	kg/m3	[225.53; 288.15]
ρg	2.36	kg/m3	225.53	Air Liquide Gas Encyclopedia
ρg	1.81	kg/m3	288.15	Air Liquide Gas Encyclopedia
ρl	[610.06; 612.00]	kg/m3	[223.00; 225.53]
ρl	612.00	kg/m3	223.00	KDB
ρl	610.06	kg/m3	225.53	Air Liquide Gas Encyclopedia
ΔfusS	[33.30; 34.18]	J/mol×K	[87.85; 88.20]
ΔfusS	34.18	J/mol×K	87.85	NIST
ΔfusS	34.18	J/mol×K	87.85	NIST
ΔfusS	33.30	J/mol×K	88.20	NIST
γ	0.02	N/m	233.20	KDB
ΔvapS	81.73	J/mol×K	225.35	NIST

Datasets

Speed of sound, m/s

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Speed of sound, m/s - Fluid (supercritical or subcritical phases)
240.01	1302.95	1101.184
240.01	2103.60	1108.727
240.01	3104.34	1117.981
240.01	4105.03	1127.052
240.01	5105.72	1135.947
240.01	6106.44	1144.672
240.00	7107.33	1153.244
240.00	8108.06	1161.649
240.00	9108.71	1169.913
240.00	10109.30	1178.038
240.00	12611.00	1197.777
240.00	15112.70	1216.761
240.00	17613.80	1235.067
240.00	20115.50	1252.744
240.00	25118.70	1286.456
240.00	30122.10	1318.218
240.00	35125.50	1348.316
240.00	40128.90	1376.953
240.00	45132.30	1404.298
240.00	50135.80	1430.49
240.00	60143.90	1479.896
260.00	1303.35	970.6167
260.00	2103.91	979.8807
260.00	3104.55	991.1728
260.00	4105.29	1002.157
260.00	5106.05	1012.855
260.00	6106.61	1023.292
260.00	7107.25	1033.466
260.00	8107.79	1043.406
260.00	9108.24	1053.122
260.00	10108.60	1062.635
260.00	12612.70	1085.589
260.00	15114.30	1107.451
260.00	17616.00	1128.358
260.00	20117.70	1148.412
260.00	25120.80	1186.29
260.00	30124.20	1221.63
260.00	35127.60	1254.829
260.00	40130.90	1286.199
260.00	45134.30	1315.977
260.00	50137.70	1344.352
260.00	60144.70	1397.522
260.00	70151.70	1446.691
260.00	80158.30	1492.558
260.00	90165.40	1535.614
260.00	100172.00	1576.274
280.00	1301.64	836.3895
280.00	2102.40	848.1849
280.00	3103.25	862.3844
280.00	4104.04	876.0391
280.00	5104.90	889.1962
280.00	6105.80	901.9084
280.00	7107.30	914.226
280.00	8108.06	926.147
280.00	9108.75	937.7206
280.00	10109.50	948.9727
280.00	12611.20	975.844
280.00	15112.90	1001.134
280.00	17613.00	1025.03
280.00	20116.60	1047.822
280.00	25118.10	1090.299
280.00	30122.10	1129.497
280.00	35125.60	1165.965
280.00	40129.10	1200.175
280.00	45132.60	1232.436
280.00	50137.50	1263.053
280.00	60144.50	1319.965
280.00	70151.40	1372.233
280.00	80157.10	1420.745
280.00	90163.80	1466.06
280.00	100171.00	1508.713
300.00	1402.74	696.0055
300.00	1402.49	696.0019
300.00	2102.73	709.9808
300.00	3103.18	728.8441
300.00	4103.79	746.5981
300.00	5104.16	763.3956
300.00	6104.72	779.3623
300.00	7107.16	794.6502
300.00	8106.02	809.2137
300.00	9106.68	823.2426
300.00	10107.40	836.7487
300.00	12611.00	868.5757
300.00	15112.80	898.0009
300.00	17612.90	925.4679
300.00	20114.50	951.3014
300.00	25117.90	998.9279
300.00	30121.00	1042.26
300.00	35124.50	1082.142
300.00	40127.90	1119.233
300.00	45131.30	1153.99
300.00	50134.70	1186.769
300.00	60141.60	1247.367
300.00	70148.60	1302.641
299.99	80156.40	1353.625
300.00	90163.40	1401.096
300.00	100170.00	1445.593
320.00	2104.38	556.1954
320.00	3105.15	584.4265
320.00	4105.81	609.6331
320.00	5106.44	632.5514
320.00	6107.10	653.6827
320.00	7107.76	673.3549
320.00	8108.42	691.8119
320.00	9108.44	709.2415
320.00	10109.00	725.7727
320.00	12610.80	763.8982
320.00	15112.40	798.3686
320.00	17614.20	829.9901
320.00	20115.90	859.315
319.99	22616.10	886.7121
320.00	25119.10	912.5156
320.00	30122.60	960.177
320.00	35126.10	1003.57
320.00	40129.50	1043.576
320.00	45133.00	1080.799
320.00	50136.40	1115.7
320.00	60143.30	1179.838
320.00	70150.30	1237.921
320.00	80157.30	1291.239
320.00	90164.30	1340.678
319.99	100172.00	1386.918
340.01	4104.99	453.1596
340.01	5105.68	489.4936
340.01	6106.34	520.3782
340.01	7107.01	547.5906
340.01	8107.68	572.1165
340.01	9108.21	594.5675
340.01	10109.20	615.3622
340.01	12611.10	661.8283
340.01	15113.00	702.4814
340.01	17614.90	738.9356
340.01	20116.70	772.1799
340.01	25118.70	831.3877
340.01	30122.20	883.5328
340.01	35125.70	930.4511
340.01	40129.20	973.3167
340.01	45132.70	1012.939
340.01	50136.20	1049.877
340.01	60143.20	1117.334
340.01	70150.10	1178.042
340.02	80157.20	1233.504
340.02	90164.10	1284.765
340.02	100171.00	1332.533
360.00	5105.03	311.2621
360.00	6105.74	370.1493
360.00	30122.50	812.7998
360.00	35126.60	863.1282
360.00	7106.48	413.2767
360.00	8107.12	448.5373
360.00	9107.83	478.9194
360.00	10108.60	505.8886
360.00	12610.20	563.3187
360.00	15112.00	611.3697
360.00	17613.80	653.2581
360.00	20115.50	690.7152
360.00	25119.00	756.1986
360.00	40130.30	908.7145
360.00	45133.80	950.5766
360.00	50137.20	989.4131
360.00	60144.20	1059.921
360.00	70151.20	1123.012
360.00	80158.20	1180.418
360.00	90165.30	1233.294
360.00	100172.00	1282.448
380.00	7106.08	268.3329
380.00	7357.45	283.4828
380.00	7606.54	297.2909
380.00	7858.19	310.3168
380.00	8106.93	322.3437
380.00	9107.64	364.5579
380.00	10108.40	399.8405
380.00	12610.20	470.5486
380.00	15112.00	526.7248
380.00	17612.70	574.2551
380.00	20115.60	615.9259
380.00	25119.30	687.4295
380.00	30122.80	748.2189
380.00	35126.40	801.6801
380.00	40129.90	849.7384
380.00	45133.60	893.6203
380.00	50137.20	934.1499
380.00	60144.20	1007.369
380.00	70151.90	1072.573
380.00	80159.00	1131.68
380.00	90166.20	1185.973
380.00	100173.00	1236.348
400.00	10108.40	309.3001
400.00	11109.00	343.8351
400.00	12109.60	374.7474
400.00	13110.20	402.6829
400.00	14110.80	428.2085
400.00	15111.40	451.7568
400.00	25116.70	625.8106
400.00	30120.70	690.1602
400.00	35124.30	746.2882
400.00	40128.00	796.4534
400.00	45131.70	842.0517
400.00	50135.30	884.0224
400.00	16111.20	473.6279
400.00	17109.90	494.1486
400.00	18111.60	513.4833
400.00	19112.30	531.7898
400.00	20113.10	549.1977
400.00	22614.80	589.4087
400.00	60142.50	959.552
400.01	70148.40	1026.538
400.01	80155.50	1087.01
400.01	90162.60	1142.605
400.01	100170.00	1194.015
420.00	12107.30	315.0009
420.00	13108.20	341.8445
420.00	14109.00	367.291
420.00	15109.60	391.2481
420.00	16110.50	413.7903
420.00	17113.10	435.0734
420.00	18114.20	455.1739
420.00	19114.90	474.2406
420.00	20115.70	492.387
420.00	22617.60	534.318
420.00	25119.70	572.2371
420.00	30123.10	639.0872
420.00	35126.80	697.1889
420.00	40130.30	748.9529
420.00	45133.90	795.8868
420.00	50137.50	838.9913
420.00	60145.10	916.3699
420.00	70152.30	984.8194
420.00	80159.40	1046.574
300.00	2104.10	710.0426
300.00	3104.74	728.903
300.00	3105.09	728.9086
300.00	4105.75	746.6704
Reference

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Speed of sound, m/s - Gas
260.00	293.11	232.483
260.00	275.35	233.169
260.00	248.96	234.363
260.00	227.97	235.295
260.00	206.56	236.232
260.00	185.32	237.147
260.00	164.45	238.028
270.00	389.41	233.762
270.00	361.31	234.964
270.00	333.53	236.13
270.00	302.89	237.393
270.00	262.89	239.005
270.00	263.03	239.0
270.00	236.28	240.061
270.00	206.19	241.233
270.00	173.01	242.506
270.00	144.04	243.598
280.00	556.25	232.732
280.00	519.72	234.242
280.00	478.89	235.889
280.00	438.30	237.487
280.00	438.33	237.486
280.00	397.57	239.056
280.00	354.13	240.694
280.00	308.73	242.368
280.00	267.79	243.845
280.00	226.29	245.315
280.00	188.35	246.636
280.00	149.29	247.972
290.00	695.54	233.484
290.00	677.98	234.169
290.00	672.07	234.402
290.00	616.94	236.509
290.00	553.22	238.872
290.00	495.22	240.952
290.00	434.96	243.061
290.00	372.80	245.178
290.00	313.39	247.152
290.00	257.68	248.961
290.00	199.13	250.82
290.00	141.01	252.628
300.00	960.98	230.066
300.00	903.31	232.289
300.00	826.40	235.145
300.00	740.35	238.219
300.00	661.10	240.945
300.00	582.66	243.559
300.00	505.72	246.037
300.00	425.25	248.556
300.00	344.40	251.013
300.00	260.81	253.485
300.00	182.30	255.747
300.00	134.71	257.089
310.00	952.69	237.373
310.00	906.76	238.902
310.00	810.73	242.008
310.00	713.38	245.043
310.00	623.06	247.765
310.00	520.89	250.748
310.00	424.89	253.463
310.00	325.91	256.182
310.00	235.24	258.606
310.00	142.07	261.046
320.00	976.94	243.091
320.00	905.02	245.205
320.00	834.83	247.22
320.00	756.59	249.417
320.00	677.09	251.597
320.00	596.12	253.766
320.00	509.07	256.044
320.00	425.07	258.192
320.00	349.85	260.081
320.00	279.66	261.8119
320.00	210.07	263.494
320.00	142.67	265.102
330.00	1001.35	248.498
330.00	912.04	250.844
330.00	821.61	253.162
330.00	732.74	255.39
330.00	642.65	257.599
330.00	550.82	259.806
330.00	455.62	262.043
330.00	380.89	263.766
330.00	302.35	265.548
330.00	227.66	267.217
330.00	151.93	268.885
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[39.17; 168.81]	J/mol×K	[80.00; 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			3.89654e+01
Coefficient B			-5.16384e+02
Coefficient C			4.84546e+00
Coefficient D			5.09119e-04
Coefficient E			-1.77135e-07
Temperature range, min.			80.00
Temperature range, max.			1500.00
Cp,gas	39.17	J/mol×K	80.00	Calculated Property
Cp,gas	55.16	J/mol×K	237.78	Calculated Property
Cp,gas	79.97	J/mol×K	395.56	Calculated Property
Cp,gas	101.75	J/mol×K	553.33	Calculated Property
Cp,gas	119.75	J/mol×K	711.11	Calculated Property
Cp,gas	134.53	J/mol×K	868.89	Calculated Property
Cp,gas	146.57	J/mol×K	1026.67	Calculated Property
Cp,gas	156.18	J/mol×K	1184.44	Calculated Property
Cp,gas	163.55	J/mol×K	1342.22	Calculated Property
Cp,gas	168.81	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[93.11; 126.27]	J/mol×K	[87.85; 340.00]	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			7.97900e+01
Coefficient B			3.00800e+02
Coefficient C			-1.77356e+00
Coefficient D			9.56150e-03
Coefficient E			1.27770e-05
Temperature range, min.			87.85
Temperature range, max.			340.00
Cp,liquid	93.11	J/mol×K	87.85	Calculated Property
Cp,liquid	87.97	J/mol×K	115.87	Calculated Property
Cp,liquid	86.87	J/mol×K	143.88	Calculated Property
Cp,liquid	87.16	J/mol×K	171.90	Calculated Property
Cp,liquid	88.40	J/mol×K	199.92	Calculated Property
Cp,liquid	90.70	J/mol×K	227.93	Calculated Property
Cp,liquid	94.46	J/mol×K	255.95	Calculated Property
Cp,liquid	100.51	J/mol×K	283.97	Calculated Property
Cp,liquid	110.28	J/mol×K	311.98	Calculated Property
Cp,liquid	126.27	J/mol×K	340.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0145825; 0.0000376]	Pa×s	[87.89; 363.00]	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			-5.40549e+01
Coefficient B			1.43777e+03
Coefficient C			7.53625e+00
Coefficient D			-3.42733e-05
Coefficient E			2.00000e+00
Temperature range, min.			87.89
Temperature range, max.			363.00
η	0.0145825	Pa×s	87.89	Calculated Property
η	0.0016350	Pa×s	118.46	Calculated Property
η	0.0005780	Pa×s	149.03	Calculated Property
η	0.0003235	Pa×s	179.59	Calculated Property
η	0.0002194	Pa×s	210.16	Calculated Property
η	0.0001597	Pa×s	240.73	Calculated Property
η	0.0001173	Pa×s	271.30	Calculated Property
η	0.0000841	Pa×s	301.86	Calculated Property
η	0.0000578	Pa×s	332.43	Calculated Property
η	0.0000376	Pa×s	363.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[23.86; 0.00]	kJ/mol	[87.89; 364.85]	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			2.75250e+01
Coefficient B			6.12170e-01
Coefficient C			-4.16460e-01
Coefficient D			8.37720e-02
Coefficient E			1.20920e-01
Critical temperature, Tc (K)			3.64850e+02
Comment			Range stopped at Tc; ChemSep gives it to 365 K.
Temperature range, min.			87.89
Temperature range, max.			364.85
ΔvapH	23.86	kJ/mol	87.89	Calculated Property
ΔvapH	22.70	kJ/mol	118.66	Calculated Property
ΔvapH	21.56	kJ/mol	149.44	Calculated Property
ΔvapH	20.38	kJ/mol	180.21	Calculated Property
ΔvapH	19.11	kJ/mol	210.98	Calculated Property
ΔvapH	17.67	kJ/mol	241.76	Calculated Property
ΔvapH	15.92	kJ/mol	272.53	Calculated Property
ΔvapH	13.67	kJ/mol	303.30	Calculated Property
ΔvapH	10.39	kJ/mol	334.08	Calculated Property
ΔvapH	0.00	kJ/mol	364.85	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4510.73]	kPa	[160.37; 364.21]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41198e+01
Coefficient B			-1.97958e+03
Coefficient C			-1.72550e+01
Temperature range, min.			160.37
Temperature range, max.			364.21
Pvap	1.33	kPa	160.37	Calculated Property
Pvap	8.83	kPa	183.02	Calculated Property
Pvap	37.08	kPa	205.67	Calculated Property
Pvap	114.51	kPa	228.32	Calculated Property
Pvap	284.17	kPa	250.97	Calculated Property
Pvap	600.58	kPa	273.61	Calculated Property
Pvap	1124.10	kPa	296.26	Calculated Property
Pvap	1914.95	kPa	318.91	Calculated Property
Pvap	3028.27	kPa	341.56	Calculated Property
Pvap	4510.73	kPa	364.21	Calculated Property
Pvap	[9.93e-07; 4546.80]	kPa	[87.89; 364.85]	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			4.81959e+01
Coefficient B			-3.33045e+03
Coefficient C			-5.40588e+00
Coefficient D			9.36410e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 365.57 K.
Temperature range, min.			87.89
Temperature range, max.			364.85
Pvap	9.93e-07	kPa	87.89	Calculated Property
Pvap	3.85e-03	kPa	118.66	Calculated Property
Pvap	0.39	kPa	149.44	Calculated Property
Pvap	6.96	kPa	180.21	Calculated Property
Pvap	49.22	kPa	210.98	Calculated Property
Pvap	200.34	kPa	241.76	Calculated Property
Pvap	575.97	kPa	272.53	Calculated Property
Pvap	1317.56	kPa	303.30	Calculated Property
Pvap	2581.87	kPa	334.08	Calculated Property
Pvap	4546.80	kPa	364.85	Calculated Property
Pvap	[1.41e-06; 4571.49]	kPa	[89.00; 364.76]	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			5.20560e+01
Coefficient B			-3.41762e+03
Coefficient C			-6.06433e+00
Coefficient D			1.13944e-05
Coefficient E			0.00000e+00
Temperature range, min.			89.00
Temperature range, max.			364.76
Pvap	1.41e-06	kPa	89.00	Calculated Property
Pvap	4.69e-03	kPa	119.64	Calculated Property
Pvap	0.44	kPa	150.28	Calculated Property
Pvap	7.51	kPa	180.92	Calculated Property
Pvap	51.42	kPa	211.56	Calculated Property
Pvap	204.78	kPa	242.20	Calculated Property
Pvap	580.56	kPa	272.84	Calculated Property
Pvap	1318.75	kPa	303.48	Calculated Property
Pvap	2582.36	kPa	334.12	Calculated Property
Pvap	4571.49	kPa	364.76	Calculated Property
Pvap	[2.13; 104.11]	kPa	[165.81; 225.98]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37577e+01
Coefficient B			-1.83244e+03
Coefficient C			-2.48840e+01
Reference			Powell and Giauque, 1939
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			165.81
Temperature range, max.			225.98
Pvap	2.13	kPa	165.81	Calculated Property
Pvap	3.83	kPa	172.50	Calculated Property
Pvap	6.56	kPa	179.18	Calculated Property
Pvap	10.75	kPa	185.87	Calculated Property
Pvap	16.92	kPa	192.55	Calculated Property
Pvap	25.73	kPa	199.24	Calculated Property
Pvap	37.94	kPa	205.92	Calculated Property
Pvap	54.40	kPa	212.61	Calculated Property
Pvap	76.10	kPa	219.29	Calculated Property
Pvap	104.11	kPa	225.98	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[759.22; 260.36]	kg/m3	[87.89; 364.85]	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			4.12924e+01
Coefficient B			2.22260e-01
Coefficient C			3.65580e+02
Coefficient D			2.40390e-01
Comment			Range stopped at Tc; ChemSep gives it to 365.57 K.
Temperature range, min.			87.89
Temperature range, max.			364.85
ρl	759.22	kg/m3	87.89	Calculated Property
ρl	730.04	kg/m3	118.66	Calculated Property
ρl	699.25	kg/m3	149.44	Calculated Property
ρl	666.45	kg/m3	180.21	Calculated Property
ρl	631.07	kg/m3	210.98	Calculated Property
ρl	592.22	kg/m3	241.76	Calculated Property
ρl	548.36	kg/m3	272.53	Calculated Property
ρl	496.38	kg/m3	303.30	Calculated Property
ρl	427.88	kg/m3	334.08	Calculated Property
ρl	260.36	kg/m3	364.85	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 2.01e-05]	N/m	[87.89; 362.63]	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			-1.21710e-02
Coefficient B			1.08860e+01
Coefficient C			-2.99780e+00
Coefficient D			-4.42050e-04
Coefficient E			-9.72570e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 364.85 K.
Temperature range, min.			87.89
Temperature range, max.			362.63
γ	0.04	N/m	87.89	Calculated Property
γ	0.03	N/m	118.42	Calculated Property
γ	0.03	N/m	148.94	Calculated Property
γ	0.02	N/m	179.47	Calculated Property
γ	0.02	N/m	210.00	Calculated Property
γ	0.01	N/m	240.53	Calculated Property
γ	0.01	N/m	271.05	Calculated Property
γ	0.01	N/m	301.58	Calculated Property
γ	0.00	N/m	332.11	Calculated Property
γ	2.01e-05	N/m	362.63	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.13]	W/m×K	[87.89; 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			4.53730e-05
Coefficient B			1.20000e+00
Coefficient C			4.15830e+02
Coefficient D			2.75720e+03
Temperature range, min.			87.89
Temperature range, max.			1000.00
λgas	0.00	W/m×K	87.89	Calculated Property
λgas	0.01	W/m×K	189.24	Calculated Property
λgas	0.02	W/m×K	290.58	Calculated Property
λgas	0.03	W/m×K	391.93	Calculated Property
λgas	0.04	W/m×K	493.27	Calculated Property
λgas	0.06	W/m×K	594.62	Calculated Property
λgas	0.07	W/m×K	695.96	Calculated Property
λgas	0.09	W/m×K	797.31	Calculated Property
λgas	0.11	W/m×K	898.65	Calculated Property
λgas	0.13	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.20; 0.08]	W/m×K	[87.89; 340.49]	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			-4.45870e-02
Coefficient B			2.20610e+01
Coefficient C			-1.74400e+00
Coefficient D			1.52140e-03
Coefficient E			-7.81620e-06
Temperature range, min.			87.89
Temperature range, max.			340.49
λliquid	0.20	W/m×K	87.89	Calculated Property
λliquid	0.18	W/m×K	115.96	Calculated Property
λliquid	0.17	W/m×K	144.02	Calculated Property
λliquid	0.16	W/m×K	172.09	Calculated Property
λliquid	0.15	W/m×K	200.16	Calculated Property
λliquid	0.14	W/m×K	228.22	Calculated Property
λliquid	0.12	W/m×K	256.29	Calculated Property
λliquid	0.11	W/m×K	284.36	Calculated Property
λliquid	0.10	W/m×K	312.42	Calculated Property
λliquid	0.08	W/m×K	340.49	Calculated Property

Similar Compounds

Find more compounds similar to Propene.

Mixtures

• Propene + Propene, hexafluoro-
• Propene + Hexafluoropropylene oxide
• Toluene + Propene
• Propene + 2-Pyrrolidinone, 1-methyl-
• Propene + 2-Propanol + Water
• Propene + Methyl Alcohol
• Ammonia + Propene
• Propene + 1-Pentanol
• Propene + 2-Pentanol
• Propene + 3-Pentanol
• Propane + Propene
• 1-Propanol + Propene
• Propene + 1-Propanol, 2-methyl-
• 2-Propanol, 2-methyl- + Propene
• Propene + Tetrahydropyran
• Propene + 1-Butanol, 2-methyl-
• Propene + 1-Butanol, 3-methyl-
• Propene + Amylene hydrate
• Propene + Dimethyl ether
• Hydrogen + Propene

Find more mixtures with Propene.

Sources

• KDB Vapor Pressure Data
• Air Liquide Gas Encyclopedia
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• 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.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 6. Unsaturated Aliphatic Hydrocarbons. J. Chem. Eng. Data 1996, 41, 645-656.
• 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
• Henry s law constants of propane, propene, butane, and 2-methylpropane in methanol at 374-490K
• Measurement of vapor liquid equilibria for the binary mixture of propylene (R-1270) + propane (R-290)
• Experimental measurement and thermodynamic modeling of propylene and propane solubility in N-methyl pyrrolidone (NMP)
• Effects of association with impurities in ammonia purification
• Phase behavior and densities of propylene + toluene and ethylene + toluene systems to 580 K and 70 MPa
• Mixture densities and viscosities of toluene with ethylene or propylene at temperatures to 530 K and pressures to 70 MPa
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutene, 1-butene, isobutane, trans-2-butene and 1,3-butadiene in 1-propanol at T=(260 to 340) K
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in isobutanol and tert-butanol
• Measurement of the (p,.rho.,T) relation of propane, propylene, n-butane, and isobutane in the temperature range from (95 to 340) K at pressures up to 12 MPa using an accurate two-sinker densimeter
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-pentanol and 3-pentanol
• (Vapour + liquid + liquid) equilibria and excess molar enthalpies of binary and ternary mixtures of isopropanol, water, and propylene
• Isothermal phase (vapour + liquid) equilibrium data for binary mixtures of propene (R1270) with either 1,1,2,3,3,3-hexafluoro-1-propene (R1216) or 2,2,3-trifluoro-3-(trifluoromethyl)oxirane in the temperature range of (279 to 318) K
• Phase Behavior and Densities of Propylene + Hexane Binary Mixtures to 585 K and 70 MPa
• Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Propane + Dimethyl Ether and Propene + Dimethyl Ether at Temperatures from (298 to 323) K
• Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene, and 1,3-butadiene in 2-propanol at 250-330 K
• Isothermal Vapor-Liquid Equilibrium and Excess Enthalpy Data for the Binary Systems Water + 1,2-Ethanediol and Propene + Acetophenone
• Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene and 1,3-Butadiene in 1-Butanol and 2-Butanol at (250 to 330) K
• Henry's law constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Measurement of Vapor-Liquid Equilibria for the Binary Mixture Difluoromethane (HFC-32) + Propylene (R-1270)
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Propen-1-ol
• Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
• Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methyl-3-buten-2-ol and 3-Methyl-3-buten-1-ol
• Solubilities of Gases in the Ionic Liquid 1-n-Butyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
• Measurement of Vapor-Liquid Equilibria for the Pentafluoroethane + Propene Binary System from (263.15 to 323.15) K
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methylphenol, 3-Methylphenol, and 4-Methylphenol
• Measurements of the Speed of Sound in Propene in the Liquid and Supercritical Regions
• Propylene and Propane Solubility in Imidazolium, Pyridinium, and Tetralkylammonium Based Ionic Liquids Containing a Silver Salt
• Experimental and Modeling of the Propene Solubility in the Heptane and Methylbenzene Solvents
• Speed of Sound Measurements Using a Cylindrical Resonator for Gaseous Carbon Dioxide and Propene
• Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethylether, Chloroethane, 1,1-Difluoroethane, and Hexane in Tetrahydropyran
• Liquid Density and Bubble Pressure Measurements for the Propylene + 2-Propanol System
• Liquid Density Measurements for the Propylene + 2-Propanol + Water System
• Isothermal Vapor-Liquid Equilibrium Data for the Hexafluoropropylene (R1216) + Propylene System at Temperatures from (263.17 to 353.14) K
• Gas-Liquid Critical Properties of Ethylene + Hydrogen and Propylene + Hydrogen Binary Mixtures
• 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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