Chemical Properties of Butane, decafluoro- (CAS 355-25-9)

InChI

InChI=1S/C4F10/c5-1(6,3(9,10)11)2(7,8)4(12,13)14

InChI Key

KAVGMUDTWQVPDF-UHFFFAOYSA-N

Formula

C4F10

SMILES

FC(F)(F)C(F)(F)C(F)(F)C(F)(F)F

Molecular Weight¹

238.03

CAS

355-25-9

Other Names

• DECAFLUOROBUTANE
• PERFLUOROBUTANE
• Perfluoro-n-butane

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (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_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• c_sound,fluid : Speed of sound in fluid (m/s).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3740		KDB
ΔfG°	-1953.94	kJ/mol	Joback Calculated Property
ΔfH°gas	-2184.99	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	7.26	kJ/mol	Joback Calculated Property
ΔvapH°	23.60	kJ/mol	Relay (1.0) Calculated Property
IE	12.48	eV	Relay (1.0) Calculated Property
log10WS	-4.25		Relay (1.0) Calculated Property
logPoct/wat	3.382		Crippen Calculated Property
McVol	84.920	ml/mol	McGowan Calculated Property
Pc	[2323.00; 2323.38]	kPa
Pc	2323.00	kPa	KDB
Pc	2323.38 ± 10.13	kPa	NIST
ρc	599.83 ± 10.00	kg/m3	NIST
Tboil	[271.00; 277.20]	K
Tboil	271.20	K	KDB
Tboil	271.00	K	NIST
Tboil	277.20	K	NIST
Tboil	271.20 ± 0.50	K	NIST
Tboil	271.15 ± 0.10	K	NIST
Tc	[386.35; 386.40]	K
Tc	386.40	K	KDB
Tc	386.35 ± 0.20	K	NIST
Tfus	[144.00; 144.90]	K
Tfus	144.90	K	KDB
Tfus	144.00 ± 1.00	K	NIST
Vc	0.378	m3/kmol	KDB
Zc	0.2733170		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[165.29; 217.03]	J/mol×K	[270.70; 387.83]
Cp,gas	165.29	J/mol×K	270.70	Joback Calculated Property
Cp,gas	175.21	J/mol×K	290.22	Joback Calculated Property
Cp,gas	184.60	J/mol×K	309.74	Joback Calculated Property
Cp,gas	193.45	J/mol×K	329.26	Joback Calculated Property
Cp,gas	201.80	J/mol×K	348.79	Joback Calculated Property
Cp,gas	209.65	J/mol×K	368.31	Joback Calculated Property
Cp,gas	217.03	J/mol×K	387.83	Joback Calculated Property
Cp,liquid	127.20	J/mol×K	293.00	NIST
ΔvapH	[17.10; 25.80]	kJ/mol	[246.50; 354.50]
ΔvapH	25.80	kJ/mol	246.50	NIST
ΔvapH	24.20	kJ/mol	253.00	NIST
ΔvapH	24.20	kJ/mol	299.50	NIST
ΔvapH	21.00	kJ/mol	308.00	NIST
ΔvapH	17.10	kJ/mol	308.00	NIST
ΔvapH	23.10	kJ/mol	354.50	NIST
Pvap	[72.70; 1997.70]	kPa	[263.15; 379.05]
Pvap	72.70	kPa	263.15	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	72.70	kPa	263.15	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	72.70	kPa	263.15	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	89.60	kPa	268.12	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	89.60	kPa	268.12	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	89.60	kPa	268.12	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	89.60	kPa	268.13	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	91.00	kPa	268.13	Vapor-liquid equilibria of ethylene (C2H4) + decafluorobutane (C4F10) at 268 to 298 K from experiment, molecular simulation and the Peng-Robinson equation of state
Pvap	89.60	kPa	268.13	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	109.40	kPa	273.09	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	109.40	kPa	273.09	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	109.40	kPa	273.09	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	132.40	kPa	278.00	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	132.40	kPa	278.00	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	132.40	kPa	278.00	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	132.40	kPa	278.03	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	132.30	kPa	278.03	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	132.40	kPa	278.03	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	132.30	kPa	278.03	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	132.30	kPa	278.03	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	132.30	kPa	278.03	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	132.30	kPa	278.03	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	132.30	kPa	278.03	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	132.60	kPa	278.06	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	132.60	kPa	278.06	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	134.60	kPa	278.36	Vapor-liquid equilibria of ethylene (C2H4) + decafluorobutane (C4F10) at 268 to 298 K from experiment, molecular simulation and the Peng-Robinson equation of state
Pvap	159.00	kPa	282.99	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	159.00	kPa	282.99	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	159.00	kPa	282.99	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	189.30	kPa	287.91	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	189.30	kPa	287.91	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	189.30	kPa	287.91	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	192.90	kPa	288.16	Vapor-liquid equilibria of ethylene (C2H4) + decafluorobutane (C4F10) at 268 to 298 K from experiment, molecular simulation and the Peng-Robinson equation of state
Pvap	225.40	kPa	292.97	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	225.40	kPa	292.97	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	225.40	kPa	292.97	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	265.30	kPa	297.95	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	265.30	kPa	297.95	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	265.30	kPa	297.95	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	268.80	kPa	298.13	Vapor-liquid equilibria of ethylene (C2H4) + decafluorobutane (C4F10) at 268 to 298 K from experiment, molecular simulation and the Peng-Robinson equation of state
Pvap	310.20	kPa	302.90	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	310.20	kPa	302.90	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	310.20	kPa	302.90	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	316.00	kPa	302.92	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	311.70	kPa	303.13	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	311.70	kPa	303.13	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	339.00	kPa	305.45	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	361.00	kPa	307.90	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	361.00	kPa	307.90	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	366.00	kPa	307.90	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	364.30	kPa	308.21	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	364.30	kPa	308.21	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	364.30	kPa	308.21	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	393.00	kPa	310.50	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	417.80	kPa	312.88	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	417.80	kPa	312.88	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	417.80	kPa	312.88	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	419.00	kPa	312.93	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	455.00	kPa	315.48	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	481.20	kPa	317.88	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	481.20	kPa	317.88	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	481.20	kPa	317.88	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	487.00	kPa	317.90	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	522.00	kPa	320.40	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	551.70	kPa	322.89	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	551.70	kPa	322.89	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	560.00	kPa	322.91	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	556.40	kPa	323.22	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	556.40	kPa	323.22	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	556.40	kPa	323.22	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	595.00	kPa	325.44	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	629.50	kPa	327.88	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	629.50	kPa	327.88	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	633.00	kPa	327.92	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	633.70	kPa	328.15	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	675.00	kPa	330.40	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	718.00	kPa	332.87	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	716.10	kPa	332.91	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	716.10	kPa	332.91	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	716.10	kPa	332.91	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	762.00	kPa	335.39	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	811.00	kPa	337.93	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	811.00	kPa	337.93	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	811.00	kPa	337.93	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	819.00	kPa	337.94	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	816.70	kPa	338.22	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	816.70	kPa	338.22	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	860.00	kPa	340.39	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	913.00	kPa	342.91	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	913.00	kPa	342.91	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	913.00	kPa	342.91	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	919.00	kPa	342.93	Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
Pvap	1025.80	kPa	347.93	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	1025.80	kPa	347.93	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	1025.80	kPa	347.93	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	1149.20	kPa	352.92	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	1149.20	kPa	352.92	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	1149.20	kPa	352.92	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	1151.60	kPa	353.01	Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
Pvap	1151.60	kPa	353.01	Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
Pvap	1261.30	kPa	357.10	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	1437.80	kPa	363.13	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	1594.10	kPa	368.03	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	1775.90	kPa	373.25	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	1912.10	kPa	376.88	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
Pvap	1997.70	kPa	379.05	Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
ρl	1517.00	kg/m3	293.00	KDB

Datasets

Speed of sound, m/s

Fixed		Measured
Temperature, K - Gas	Pressure, kPa - Gas	Speed of sound, m/s - Gas
248.70	10.00	95.1
248.70	20.00	94.56
248.70	30.00	93.98
257.70	10.00	96.57
257.70	20.00	96.22
257.70	30.00	95.7
257.70	50.00	94.78
271.30	10.00	99.26
271.30	20.00	98.71
271.30	30.00	98.33
271.30	50.00	97.39
271.30	70.00	96.39
271.30	100.00	94.79
281.50	10.00	101.05
281.50	20.00	100.64
281.50	30.00	100.23
281.50	50.00	99.38
281.50	70.00	98.4
281.50	100.00	97.04
281.50	150.00	95.08
293.10	10.00	103.02
293.10	20.00	102.7
293.10	30.00	102.37
293.10	50.00	101.71
293.10	70.00	100.86
293.10	100.00	99.66
293.10	150.00	97.68
293.10	200.00	95.63
303.10	10.00	104.78
303.10	20.00	104.57
303.10	30.00	104.25
303.10	50.00	103.35
303.10	70.00	103.06
303.10	100.00	103.05
303.10	150.00	99.91
303.10	200.00	98.41
303.10	250.00	96.5
303.10	300.00	94.89
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 2340.36]	kPa	[196.90; 386.33]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.42719e+01
Coefficient B			-2.30981e+03
Coefficient C			-3.17290e+01
Temperature range, min.			196.90
Temperature range, max.			386.33
Pvap	1.33	kPa	196.90	Calculated Property
Pvap	6.48	kPa	217.95	Calculated Property
Pvap	22.82	kPa	239.00	Calculated Property
Pvap	63.76	kPa	260.04	Calculated Property
Pvap	149.76	kPa	281.09	Calculated Property
Pvap	307.97	kPa	302.14	Calculated Property
Pvap	570.70	kPa	323.19	Calculated Property
Pvap	973.23	kPa	344.23	Calculated Property
Pvap	1551.58	kPa	365.28	Calculated Property
Pvap	2340.36	kPa	386.33	Calculated Property
Pvap	[2.12e-03; 2284.39]	kPa	[144.95; 386.35]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.19638e+01
Coefficient B			-4.91335e+03
Coefficient C			-8.93526e+00
Coefficient D			1.14729e-05
Temperature range, min.			144.95
Temperature range, max.			386.35
Pvap	2.12e-03	kPa	144.95	Calculated Property
Pvap	0.10	kPa	171.77	Calculated Property
Pvap	1.49	kPa	198.59	Calculated Property
Pvap	10.37	kPa	225.42	Calculated Property
Pvap	44.67	kPa	252.24	Calculated Property
Pvap	138.68	kPa	279.06	Calculated Property
Pvap	342.43	kPa	305.88	Calculated Property
Pvap	718.02	kPa	332.71	Calculated Property
Pvap	1337.39	kPa	359.53	Calculated Property
Pvap	2284.39	kPa	386.35	Calculated Property

Similar Compounds

Find more compounds similar to Butane, decafluoro-.

Mixtures

• Butane, decafluoro- + Perfluoropropane
• Carbon dioxide + Butane, decafluoro-
• Butane, decafluoro- + Dimethyl ether
• Butane, decafluoro- + Ethylene
• Propane + Butane, decafluoro-
• 1-Butene + Butane, decafluoro-
• Butane, decafluoro- + Ethane
• Carbon monoxide + Butane, decafluoro-
• Nitric oxide + Butane, decafluoro-
• Methane + Butane, decafluoro-
• Butane, decafluoro- + Hydrogen sulfide

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Properties of saturated fluorocarbons: Experimental data and modeling using perturbed-chain-SAFT
• Isothermal vapor-liquid equilibrium data for the carbon dioxide (R744) + decafluorobutane (R610) system at temperatures from 263 to 353K
• Vapor-liquid equilibrium data for the dimethyl ether (RE170) + decafluorobutane (R3-1-10) system at temperatures from 313.28 to 392.83 K and pressures up to 4.9 MPa
• Vapor-liquid equilibria of ethylene (C2H4) + decafluorobutane (C4F10) at 268 to 298 K from experiment, molecular simulation and the Peng-Robinson equation of state
• Isothermal vapor liquid equilibrium data for the decafluorobutane(R3110) + 1,1,1,3,3-pentafluorobutane (R365mfc) system attemperatures from 333 K to 441 K
• Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
• Isothermal Vapor-Liquid Equilibrium Data for the Perfluorobutane (R610) + Ethane System at Temperatures from (263 to 353) K
• Vapor Liquid Equilibrium (VLE) Data and Thermodynamic Modeling for Binary Systems Containing Perfluorobutane (R610) with Carbon Monoxide or Nitric Oxide at (293, 313, and 333) K
• Isothermal Vapor Liquid Equilibrium Data and Thermodynamic Modeling for Binary Systems of Perfluorobutane (R610) + (Methane or Hydrogen Sulfide) at (293, 313, and 333) K
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.