Chemical Properties of Ethyl ether (CAS 60-29-7)

InChI

InChI=1S/C4H10O/c1-3-5-4-2/h3-4H2,1-2H3

InChI Key

RTZKZFJDLAIYFH-UHFFFAOYSA-N

Formula

C4H10O

SMILES

CCOCC

Molecular Weight¹

74.12

CAS

60-29-7

Other Names

• (C2H5)2O
• 1,1'-Oxybisethane
• 1,1'-oxybis-ethane
• 3-Oxapentane
• Aether
• Anaesthetic ether
• Anesthesia ether
• Anesthetic ether
• Diaethylaether
• Diethyl oxide
• Dwuetylowy eter
• Etere etilico
• Ethane, 1,1'-oxybis-
• Ether
• Ether ethylique
• Ether, ethyl
• Ethoxy ethane
• Ethyl ether anhydrous A.C.S.
• Ethyl ether, tech.
• Ethyl oxide
• NSC 100036
• Oxyde d'ethyle
• Pronarcol
• Rcra waste number U117
• Solvent ether
• Sulfuric ether
• UN 1155
• diethyl ether
• ethoxyethane

• 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).
• 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).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• 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_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• pKa : Log10 of Acid Dissociation Constant.
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• 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°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• 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_boil(P) : Boiling point at given pressure (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. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.2810; 0.2810]
ω	0.2810		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2810		ChemSep v8.3 pure component data Compiled value
ω	0.2810		KDB
PAff	828.40	kJ/mol	NIST
Tig	[433.15; 453.15]	K
Tig	453.15	K	KDB
Tig	433.15	K	NCMS SOLV-DB
BasG	801.00	kJ/mol	NIST
ΔcH°gas	[-2751.10; -2726.30]	kJ/mol
ΔcH°gas	-2726.30 ± 1.80	kJ/mol	NIST
ΔcH°gas	-2751.10 ± 0.75	kJ/mol	NIST
ΔcH°liquid	-2732.10 ± 1.90	kJ/mol	NIST
μ	[1.15; 1.30]	debye
μ	1.15	debye	ChemSep v8.3 pure component data Compiled value
μ	1.30	debye	KDB
εr	4.20		NCMS SOLV-DB
LFL	1.85	% in Air	KDB
UFL	36.50	% in Air	KDB
Tflash,cc	[228.15; 233.15]	K
Tflash,cc	233.15	K	KDB
Tflash,cc	228.15	K	NCMS SOLV-DB
Tflash,oc	228.15	K	KDB
ΔfG°	[-122.40; -122.10]	kJ/mol
ΔfG°	-122.10	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-122.40	kJ/mol	KDB
Rg	3.1400		KDB
ΔfH°gas	[-252.70; -244.00]	kJ/mol
ΔfH°gas	-252.10	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-252.40	kJ/mol	KDB
ΔfH°gas	-252.70 ± 2.00	kJ/mol	NIST
ΔfH°gas	-252.20 ± 0.79	kJ/mol	NIST
ΔfH°gas	-244.00	kJ/mol	NIST
ΔfH°liquid	-271.20 ± 1.90	kJ/mol	NIST
ΔfusH°	7.30	kJ/mol	Joback Calculated Property
ΔvapH°	[26.60; 27.37]	kJ/mol
ΔvapH°	27.24	kJ/mol	NCMS SOLV-DB
ΔvapH°	27.37	kJ/mol	NIST
ΔvapH°	27.14	kJ/mol	NIST
ΔvapH°	27.10 ± 0.10	kJ/mol	NIST
ΔvapH°	27.20	kJ/mol	NIST
ΔvapH°	Outlier 26.60	kJ/mol	NIST
ΔvapH°	27.20 ± 0.30	kJ/mol	NIST
IE	[9.41; 9.70]	eV
IE	9.51 ± 0.03	eV	NIST
IE	9.52 ± 0.07	eV	NIST
IE	9.60 ± 0.01	eV	NIST
IE	9.41	eV	NIST
IE	9.50 ± 0.01	eV	NIST
IE	9.51	eV	NIST
IE	9.53 ± 0.02	eV	NIST
IE	9.61	eV	NIST
IE	9.66	eV	NIST
IE	9.59	eV	NIST
IE	9.70	eV	NIST
log10WS	[-0.09; -0.09]
log10WS	-0.09		Aq. Solubility Prediction
log10WS	-0.09		Estimated Solubility
logPoct/wat	0.890		NCMS SOLV-DB
McVol	73.090	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=4); %!d(float64=4)]
NFPA Fire	4		KDB
NFPA Fire	4		NCMS SOLV-DB
NFPA Health	[%!d(float64=2); %!d(float64=2)]
NFPA Health	2		KDB
NFPA Health	2		NCMS SOLV-DB
NFPA Safety	1		NCMS SOLV-DB
Pc	[3545.00; 4050.00]	kPa
Pc	3605.00	kPa	Experimental Study of the Thermodynamic Properties of Diethyl Ether (DEE) at Saturation
Pc	3644.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	3637.57	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3640.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3638.00	kPa	KDB
Pc	3637.60 ± 0.36	kPa	NIST
Pc	3638.00 ± 303.98	kPa	NIST
Pc	3605.94 ± 27.57	kPa	NIST
Pc	3651.00 ± 34.47	kPa	NIST
Pc	3545.00 ± 117.68	kPa	NIST
Pc	3610.00 ± 101.32	kPa	NIST
Pc	3675.00 ± 39.99	kPa	NIST
Pc	3657.80 ± 41.36	kPa	NIST
Pc	3607.70 ± 41.36	kPa	NIST
Pc	3739.00 ± 101.32	kPa	NIST
Pc	3668.00 ± 81.06	kPa	NIST
Pc	3600.00 ± 202.65	kPa	NIST
Pc	3676.00 ± 60.79	kPa	NIST
Pc	3624.20 ± 81.06	kPa	NIST
Pc	3607.70 ± 53.32	kPa	NIST
Pc	Outlier 4050.00 ± 303.98	kPa	NIST
Pc	3740.00 ± 303.98	kPa	NIST
pKa	-2.39		NCMS SOLV-DB
Ptriple	3.95e-04	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[208.28; 266.47]	kg/m3
ρc	261.87 ± 2.22	kg/m3	NIST
ρc	265.36 ± 2.22	kg/m3	NIST
ρc	265.36 ± 2.96	kg/m3	NIST
ρc	265.36 ± 2.22	kg/m3	NIST
ρc	266.47 ± 2.96	kg/m3	NIST
ρc	262.46 ± 2.96	kg/m3	NIST
ρc	257.94 ± 5.19	kg/m3	NIST
ρc	260.39 ± 3.71	kg/m3	NIST
ρc	Outlier 208.28 ± 40.03	kg/m3	NIST
ρc	246.08 ± 9.64	kg/m3	NIST
Inp	[464.00; 515.00]
Inp	495.00		NIST
Inp	496.00		NIST
Inp	478.00		NIST
Inp	486.00		NIST
Inp	473.00		NIST
Inp	471.00		NIST
Inp	476.00		NIST
Inp	482.60		NIST
Inp	476.00		NIST
Inp	474.00		NIST
Inp	480.00		NIST
Inp	484.00		NIST
Inp	476.00		NIST
Inp	500.00		NIST
Inp	493.00		NIST
Inp	494.00		NIST
Inp	464.00		NIST
Inp	510.00		NIST
Inp	485.00		NIST
Inp	485.00		NIST
Inp	504.00		NIST
Inp	509.00		NIST
Inp	508.00		NIST
Inp	504.00		NIST
Inp	504.00		NIST
Inp	484.00		NIST
Inp	499.00		NIST
Inp	485.00		NIST
Inp	485.00		NIST
Inp	499.00		NIST
Inp	515.00		NIST
Inp	470.00		NIST
Inp	477.00		NIST
Inp	510.00		NIST
Ip	[567.00; 640.00]
Ip	630.00		NIST
Ip	577.00		NIST
Ip	570.00		NIST
Ip	577.00		NIST
Ip	570.00		NIST
Ip	567.00		NIST
Ip	567.00		NIST
Ip	576.00		NIST
Ip	596.00		NIST
Ip	608.00		NIST
Ip	606.00		NIST
Ip	618.00		NIST
Ip	619.00		NIST
Ip	640.00		NIST
Ip	590.00		NIST
Ip	616.00		NIST
Ip	630.00		NIST
Ip	567.00		NIST
Ip	590.00		NIST
Ip	596.00		NIST
Ip	640.00		NIST
S°gas	342.20	J/mol×K	NIST
S°liquid	[252.70; 283.30]	J/mol×K
S°liquid	253.50	J/mol×K	NIST
S°liquid	252.70	J/mol×K	NIST
S°liquid	283.30	J/mol×K	NIST
Tboil	[307.15; 309.20]	K
Tboil	307.59	K	ChemSep v8.3 pure component data Compiled value
Tboil	307.60	K	KDB
Tboil	307.58	K	NCMS SOLV-DB
Tboil	307.70	K	NIST
Tboil	307.60	K	NIST
Tboil	307.65	K	NIST
Tboil	Outlier 309.20 ± 0.30	K	NIST
Tboil	307.80 ± 0.40	K	NIST
Tboil	307.70 ± 0.30	K	NIST
Tboil	307.80 ± 0.40	K	NIST
Tboil	307.15 ± 0.50	K	NIST
Tboil	308.20 ± 1.00	K	NIST
Tboil	307.80 ± 0.30	K	NIST
Tboil	307.63 ± 0.02	K	NIST
Tboil	307.75 ± 0.30	K	NIST
Tboil	307.45 ± 0.30	K	NIST
Tboil	307.75 ± 0.15	K	NIST
Tboil	307.80 ± 0.30	K	NIST
Tboil	307.81 ± 0.20	K	NIST
Tboil	307.69 ± 0.25	K	NIST
Tboil	307.80 ± 0.50	K	NIST
Tboil	307.65 ± 0.50	K	NIST
Tboil	307.90 ± 0.70	K	NIST
Tboil	307.80 ± 0.40	K	NIST
Tboil	307.75 ± 0.20	K	NIST
Tc	[463.20; 472.50]	K
Tc	466.70	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	466.70	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	466.70	K	ChemSep v8.3 pure component data Compiled value
Tc	466.74	K	KDB
Tc	466.70	K	NIST
Tc	466.70 ± 0.30	K	NIST
Tc	466.74 ± 0.04	K	NIST
Tc	466.70 ± 0.40	K	NIST
Tc	466.70 ± 0.40	K	NIST
Tc	466.80 ± 0.60	K	NIST
Tc	465.80 ± 1.00	K	NIST
Tc	466.56 ± 0.40	K	NIST
Tc	465.50 ± 2.00	K	NIST
Tc	466.50 ± 0.40	K	NIST
Tc	467.80 ± 1.00	K	NIST
Tc	466.76 ± 0.40	K	NIST
Tc	466.00 ± 2.00	K	NIST
Tc	467.00 ± 0.60	K	NIST
Tc	467.00 ± 0.40	K	NIST
Tc	466.60 ± 0.80	K	NIST
Tc	467.50 ± 0.60	K	NIST
Tc	466.76 ± 0.50	K	NIST
Tc	466.00 ± 4.00	K	NIST
Tc	467.60 ± 0.50	K	NIST
Tc	466.76 ± 0.40	K	NIST
Tc	467.90 ± 1.00	K	NIST
Tc	466.80 ± 1.00	K	NIST
Tc	Outlier 470.00 ± 3.00	K	NIST
Tc	Outlier 472.50 ± 5.00	K	NIST
Tc	466.70 ± 1.00	K	NIST
Tc	464.00 ± 2.00	K	NIST
Tc	467.00 ± 2.00	K	NIST
Tc	468.70 ± 2.00	K	NIST
Tc	Outlier 463.20 ± 3.00	K	NIST
Tfus	[122.00; 157.15]	K
Tfus	157.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	156.85	K	ChemSep v8.3 pure component data Compiled value
Tfus	156.80	K	KDB
Tfus	157.07	K	Aq. Solubility Prediction
Tfus	156.85	K	NCMS SOLV-DB
Tfus	156.85	K	NIST
Tfus	157.15 ± 0.00	K	NIST
Tfus	149.90 ± 0.80	K	NIST
Tfus	156.90 ± 0.80	K	NIST
Tfus	149.75 ± 0.20	K	NIST
Tfus	156.75 ± 0.30	K	NIST
Tfus	Outlier 122.00 ± 2.00	K	NIST
Tfus	157.00 ± 0.40	K	NIST
Tfus	149.85 ± 0.20	K	NIST
Tfus	149.85 ± 0.50	K	NIST
Tfus	156.85 ± 0.25	K	NIST
Tfus	150.61 ± 0.50	K	NIST
Tfus	149.85 ± 0.30	K	NIST
Tfus	157.00 ± 0.30	K	NIST
Tfus	156.15 ± 1.50	K	NIST
Ttriple	[149.86; 156.92]	K
Ttriple	156.86	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	156.85	K	ChemSep v8.3 pure component data Compiled value
Ttriple	156.92	K	KDB
Ttriple	156.92 ± 0.05	K	NIST
Ttriple	149.86 ± 0.02	K	NIST
Ttriple	156.92 ± 0.02	K	NIST
Ttriple	156.80 ± 0.20	K	NIST
Ttriple	149.86 ± 0.02	K	NIST
Ttriple	156.92 ± 0.02	K	NIST
Ttriple	156.80 ± 0.20	K	NIST
UQi	3.02		ChemSep v8.3 pure component data Compiled value
URi	3.39		ChemSep v8.3 pure component data Compiled value
Vc	[0.274; 0.281]	m3/kmol
Vc	0.281	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc	0.280	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.280	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.280	m3/kmol	KDB
Vc	0.274 ± 0.005	m3/kmol	NIST
VCOSTALD	0.28	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.28		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2624880; 0.2640000]
Zc	0.2640000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Zc	0.2630000		ChemSep v8.3 pure component data Compiled value
Zc	0.2624880		KDB
Zra	[0.26; 0.27]
Zra	0.26		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[121.94; 155.11]	J/mol×K	[309.98; 450.04]
Cp,gas	121.94	J/mol×K	309.98	NIST
Cp,gas	126.57	J/mol×K	329.99	NIST
Cp,gas	131.32	J/mol×K	350.00	NIST
Cp,gas	137.21	J/mol×K	375.00	NIST
Cp,gas	143.27	J/mol×K	400.01	NIST
Cp,gas	149.10	J/mol×K	424.99	NIST
Cp,gas	155.11	J/mol×K	450.04	NIST
Cp,liquid	[164.80; 179.90]	J/mol×K	[255.20; 308.00]
Cp,liquid	164.80	J/mol×K	255.20	NIST
Cp,liquid	179.10	J/mol×K	286.60	NIST
Cp,liquid	167.40	J/mol×K	290.00	NIST
Cp,liquid	170.70	J/mol×K	290.00	NIST
Cp,liquid	172.00	J/mol×K	293.00	NIST
Cp,liquid	171.88	J/mol×K	293.15	NIST
Cp,liquid	172.50	J/mol×K	298.15	NIST
Cp,liquid	179.90	J/mol×K	308.00	NIST
η	0.0002420	Pa×s	298.15	NCMS SOLV-DB
ΔfusH	[7.19; 7.30]	kJ/mol	[156.80; 156.90]
ΔfusH	7.30	kJ/mol	156.80	NIST
ΔfusH	7.30	kJ/mol	156.80	NIST
ΔfusH	7.19	kJ/mol	156.90	NIST
ΔfusH	7.19	kJ/mol	156.90	NIST
ΔfusH	7.19	kJ/mol	156.90	NIST
ΔfusH	7.19	kJ/mol	156.90	NIST
ΔvapH	[26.52; 29.50]	kJ/mol	[253.00; 442.00]
ΔvapH	28.40	kJ/mol	253.00	NIST
ΔvapH	27.53	kJ/mol	285.00	NIST
ΔvapH	29.50	kJ/mol	289.50	NIST
ΔvapH	27.25 ± 0.01	kJ/mol	295.63	NIST
ΔvapH	27.25 ± 0.01	kJ/mol	295.63	NIST
ΔvapH	28.10	kJ/mol	307.50	NIST
ΔvapH	26.52	kJ/mol	307.60	NIST
ΔvapH	26.69	kJ/mol	307.70	KDB
ΔvapH	27.50	kJ/mol	332.50	NIST
ΔvapH	26.90	kJ/mol	382.00	NIST
ΔvapH	26.70	kJ/mol	442.00	NIST
Pvap	[10.11; 2390.00]	kPa	[255.47; 438.90]
Pvap	10.11	kPa	255.47	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	10.13	kPa	255.48	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	10.14	kPa	255.50	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	17.06	kPa	265.44	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	17.06	kPa	265.44	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	17.07	kPa	265.45	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	26.90	kPa	274.86	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	26.91	kPa	274.87	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	41.98	kPa	284.83	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	42.00	kPa	284.84	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	62.89	kPa	294.77	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	62.93	kPa	294.78	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	71.59	kPa	298.15	NCMS SOLV-DB
Pvap	91.58	kPa	304.75	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	91.56	kPa	304.75	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	91.60	kPa	304.76	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	129.30	kPa	314.74	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	129.45	kPa	314.74	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	129.42	kPa	314.75	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	179.51	kPa	324.89	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	179.65	kPa	324.89	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	179.77	kPa	324.89	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	1790.00	kPa	424.30	Experimental High-Pressure Isochoric/Isoplethic Equilibrium for the Systems Propane + n-Pentane and Propane + Diethyl Ether
Pvap	2150.00	kPa	434.30	Experimental High-Pressure Isochoric/Isoplethic Equilibrium for the Systems Propane + n-Pentane and Propane + Diethyl Ether
Pvap	2390.00	kPa	438.90	Experimental High-Pressure Isochoric/Isoplethic Equilibrium for the Systems Propane + n-Pentane and Propane + Diethyl Ether
n0	[1.34900; 1.34970]		[293.15; 298.15]
n0	1.34970		293.15	Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0	1.34900		298.15	NCMS SOLV-DB
ρl	[212.60; 713.00]	kg/m3	[293.00; 466.85]
ρl	713.00	kg/m3	293.00	KDB
ρl	707.79	kg/m3	298.15	Volumetric properties of (N,N-dimethylformamide + aliphatic diethers) at Temperatures ranging from (298.15 to 358.15) K
ρl	534.60	kg/m3	416.10	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	517.30	kg/m3	425.19	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	485.20	kg/m3	437.14	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	441.50	kg/m3	450.60	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	440.80	kg/m3	450.77	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	394.80	kg/m3	459.61	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	348.20	kg/m3	464.79	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	212.60	kg/m3	466.12	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	310.80	kg/m3	466.47	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	233.70	kg/m3	466.66	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	296.70	kg/m3	466.75	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	288.30	kg/m3	466.80	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	278.70	kg/m3	466.81	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	275.70	kg/m3	466.82	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	255.00	kg/m3	466.83	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	260.70	kg/m3	466.83	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ρl	261.20	kg/m3	466.85	PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
ΔfusS	[46.60; 46.60]	J/mol×K	[156.80; 156.80]
ΔfusS	46.60	J/mol×K	156.80	NIST
ΔfusS	46.60	J/mol×K	156.80	NIST
γ	[0.01; 0.02]	N/m	[258.17; 373.17]
γ	0.02	N/m	258.17	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	263.17	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	268.18	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	273.18	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	278.18	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	283.18	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	288.18	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	293.16	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	298.10	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	298.15	NCMS SOLV-DB
γ	0.02	N/m	298.20	KDB
γ	0.02	N/m	303.17	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.02	N/m	308.11	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	313.19	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	318.16	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	323.16	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	328.12	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	333.18	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	338.17	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	343.17	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	348.17	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	353.19	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	358.18	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	363.16	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	368.18	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
γ	0.01	N/m	373.17	Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
ΔvapS	96.60	J/mol×K	285.00	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	307.75	K	96.60	Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere

Datasets

1. Molar heat capacity at constant volume, J/K/mol (1)
2. Viscosity, Pa*s (1)
3. Thermal conductivity, W/m/K (1)

Molar heat capacity at constant volume, J/K/mol

Fixed		Measured
Mass density, kg/m3 - Fluid (supercritical or subcritical phases)	Temperature, K - Fluid (supercritical or subcritical phases)	Molar heat capacity at constant volume, J/K/mol - Fluid (supercritical or subcritical phases)
534.6	416.10	156.7672
534.6	416.11	156.026
534.6	416.19	155.2106
534.6	416.30	153.58
534.6	416.40	154.5435
534.6	416.51	153.6541
534.6	416.62	153.2093
534.6	417.58	153.58
534.6	417.69	154.247
534.6	417.79	153.3576
534.6	417.90	154.3212
534.6	418.01	153.8764
534.6	421.51	155.2848
534.6	421.73	154.6918
534.6	421.83	155.1365
534.6	421.94	154.247
534.6	422.05	154.0988
534.6	426.25	155.9518
534.6	426.49	156.3966
534.6	426.59	154.0988
534.6	426.70	154.6918
534.6	426.80	155.2848
534.6	426.91	154.3212
534.6	426.96	155.5812
534.6	433.20	157.7308
534.6	433.31	158.1014
534.6	433.41	156.3225
534.6	433.52	158.1014
534.6	433.62	157.0637
534.6	433.73	155.433
534.6	433.83	155.1365
534.6	439.24	158.1014
534.6	439.35	157.3602
534.6	439.45	158.472
534.6	439.55	159.1391
534.6	439.66	158.472
534.6	439.76	157.0637
534.6	439.86	156.6931
534.6	439.97	158.7685
534.6	449.24	157.879
534.6	449.34	158.6202
534.6	449.44	159.2873
534.6	449.55	159.6579
534.6	449.75	158.6202
534.6	449.85	159.2873
534.6	449.96	160.0285
534.6	460.94	163.5122
534.6	461.04	162.1781
534.6	461.14	161.511
534.6	461.25	162.9934
534.6	461.35	160.8439
534.6	461.45	161.511
534.6	471.19	164.9206
534.6	471.29	165.2912
534.6	471.39	163.0675
534.6	471.49	163.0675
534.6	471.59	164.9206
534.6	471.69	163.8087
517.3	425.19	159.3614
517.3	425.23	158.0273
517.3	425.27	155.8777
517.3	425.32	154.3953
517.3	425.36	156.6189
517.3	425.44	155.5071
517.3	425.53	154.3953
517.3	425.63	154.7659
517.3	425.74	153.8764
517.3	426.05	154.9141
517.3	426.16	154.6177
517.3	426.26	154.0988
517.3	426.37	154.7659
517.3	426.48	153.9506
517.3	426.58	154.1729
517.3	426.69	154.3212
517.3	426.79	155.2106
517.3	426.90	154.84
517.3	427.00	154.5435
485.2	437.14	163.8087
485.2	437.27	163.1416
485.2	437.37	160.7698
485.2	437.47	161.8075
485.2	437.58	158.3237
485.2	437.68	159.5838
485.2	437.88	159.1391
485.2	438.00	156.7672
485.2	438.10	157.5825
485.2	438.20	158.0273
485.2	438.41	157.286
485.2	438.51	158.5461
485.2	438.62	157.7308
485.2	438.72	156.5448
485.2	445.95	158.2496
485.2	446.06	159.6579
485.2	446.16	158.6943
485.2	446.26	159.8062
485.2	446.47	157.7308
485.2	446.58	158.8426
485.2	460.03	165.217
485.2	460.13	163.957
485.2	460.23	165.8841
485.2	460.33	165.8841
485.2	460.44	164.4017
485.2	460.54	163.2158
485.2	460.64	162.9193
485.2	471.59	168.9972
485.2	471.69	167.8113
485.2	471.80	165.217
485.2	471.89	165.217
485.2	471.99	166.1806
485.2	472.09	169.8867
485.2	472.19	166.6995
485.2	472.29	169.442
485.2	479.25	173.5187
485.2	479.35	172.7033
485.2	479.45	172.2586
485.2	479.55	169.3679
485.2	479.64	170.6279
485.2	479.74	173.5187
485.2	479.85	173.5187
485.2	479.94	174.2599
485.2	480.05	170.6279
485.2	480.44	171.8139
485.2	480.54	172.7774
485.2	480.64	174.0375
485.2	480.73	173.741
485.2	480.93	172.481
485.2	481.03	170.4797
485.2	481.33	173.4445
485.2	492.92	179.4484
485.2	493.02	181.1532
485.2	493.11	181.8944
485.2	493.11	179.7449
485.2	493.21	176.4835
485.2	493.41	179.7449
485.2	493.51	177.8177
485.2	493.60	179.0037
485.2	504.28	184.9334
485.2	504.38	183.451
485.2	504.47	185.7487
485.2	504.57	182.7839
485.2	504.95	181.8203
441.5	450.60	170.2573
441.5	450.85	167.0701
441.5	450.93	170.9985
441.5	451.07	167.5889
441.5	451.18	165.81
441.5	451.28	168.6266
441.5	451.38	163.957
441.5	451.49	167.1442
441.5	452.20	163.2899
441.5	452.30	162.2522
441.5	452.40	164.6982
441.5	452.51	161.8075
441.5	452.57	165.4394
441.5	452.67	161.1404
441.5	452.77	162.771
441.5	462.04	166.2547
441.5	462.14	164.1793
441.5	462.25	166.996
441.5	462.35	164.8464
441.5	462.45	164.0311
441.5	462.55	163.2899
441.5	462.65	163.4381
440.8	450.77	171.9621
440.8	450.87	170.8503
440.8	450.97	169.0714
440.8	451.07	170.1832
440.8	451.39	166.6995
440.8	451.49	166.9218
440.8	451.59	164.9947
440.8	451.69	167.2183
440.8	451.80	164.6982
440.8	451.90	164.2535
440.8	452.00	165.6618
440.8	452.10	164.4758
440.8	452.21	165.0688
440.8	452.31	163.1416
440.8	462.36	164.3276
440.8	462.46	164.6982
440.8	462.56	164.0311
440.8	462.66	164.1793
440.8	462.76	165.81
440.8	462.86	164.8464
440.8	462.96	163.957
440.8	463.06	163.7346
440.8	477.76	172.8516
440.8	477.86	170.702
440.8	477.96	171.5174
440.8	478.06	169.9608
440.8	478.16	170.9985
440.8	478.26	169.6643
440.8	478.36	169.6643
440.8	478.46	172.5551
440.8	490.96	181.7462
440.8	491.06	182.7097
440.8	491.45	180.7085
440.8	491.55	178.9295
440.8	491.65	178.3366
440.8	491.75	180.0414
440.8	491.84	177.4471
394.8	459.61	178.6331
394.8	459.72	177.4471
394.8	459.82	173.4445
394.8	459.92	175.0011
394.8	460.02	173.2222
394.8	460.12	176.4835
394.8	460.23	171.6656
394.8	460.33	170.3314
394.8	460.74	173.6669
394.8	460.94	169.5902
394.8	461.04	173.3704
394.8	461.14	170.5538
394.8	461.35	168.4043
394.8	461.45	171.5174
394.8	472.79	172.1845
394.8	472.89	171.6656
394.8	473.09	171.295
394.8	473.19	170.3314
394.8	473.29	172.9257
394.8	473.39	169.9608
394.8	473.49	171.4433
394.8	487.34	169.0714
394.8	487.44	166.4771
394.8	487.53	168.6266
394.8	487.63	170.035
394.8	487.73	165.6618
394.8	487.83	169.2937
394.8	487.93	167.4407
394.8	499.44	165.5877
394.8	499.54	166.3289
394.8	499.63	167.3666
394.8	499.73	168.7008
394.8	499.83	164.4758
394.8	499.92	165.4394
394.8	500.12	165.5877
394.8	500.21	164.1052
394.8	518.00	169.2196
394.8	518.09	171.1468
394.8	518.28	169.8126
394.8	518.38	171.888
394.8	518.47	170.702
394.8	533.79	178.0401
394.8	533.98	178.7813
394.8	534.08	174.6305
394.8	534.17	176.78
394.8	534.26	175.7423
394.8	554.74	183.451
394.8	554.83	187.0829
394.8	554.92	183.8957
394.8	555.02	185.4522
394.8	555.20	185.897
394.8	555.29	182.265
394.8	555.38	183.451
394.8	574.77	193.3091
394.8	574.87	191.0855
394.8	574.96	188.936
394.8	575.05	192.4197
394.8	575.14	189.8254
394.8	575.23	191.382
394.8	575.32	190.3443
348.2	464.79	190.4925
348.2	464.82	186.1935
348.2	464.87	188.6395
348.2	464.91	182.9321
348.2	464.95	187.6018
348.2	464.99	185.8229
348.2	465.03	182.4133
348.2	465.07	184.6369
348.2	465.17	182.0426
348.2	465.27	184.4887
348.2	465.37	183.2286
348.2	465.47	182.265
348.2	470.58	180.7085
348.2	470.68	177.966
348.2	470.78	182.4133
348.2	470.88	179.4484
348.2	470.98	178.3366
348.2	471.08	182.0426
348.2	471.18	180.5602
348.2	471.28	177.373
310.8	466.47	203.8344
310.8	466.51	202.5002
310.8	466.55	202.0555
310.8	466.59	200.4989
310.8	466.63	196.7187
310.8	466.68	202.4261
310.8	466.78	199.7577
310.8	466.88	197.0893
310.8	466.98	199.2389
310.8	467.08	195.9034
310.8	467.28	199.4612
310.8	467.38	194.6433
310.8	467.48	197.0893
310.8	467.58	195.5328
310.8	467.79	195.8293
310.8	467.88	193.3833
310.8	467.98	195.2363
310.8	468.08	198.0529
310.8	468.19	192.9385
310.8	468.29	194.2727
310.8	480.13	171.9621
310.8	480.23	175.9647
310.8	480.33	177.8177
310.8	480.43	174.5564
310.8	480.53	172.8516
310.8	480.63	173.9634
310.8	480.73	171.3691
310.8	480.83	176.1129
310.8	499.30	186.1935
310.8	499.40	187.6759
310.8	499.50	189.0101
310.8	499.59	187.6018
310.8	499.69	184.6369
310.8	499.79	188.4912
310.8	499.89	188.0465
310.8	499.99	183.6733
296.7	466.75	210.6536
296.7	466.80	207.837
296.7	466.84	205.0203
296.7	466.92	201.8331
296.7	467.00	200.573
296.7	467.04	198.3494
296.7	467.08	199.7577
296.7	467.18	196.9411
296.7	467.28	200.9437
296.7	467.38	198.2012
296.7	467.48	199.0906
296.7	472.28	177.7436
296.7	472.38	173.8152
296.7	472.49	174.5564
296.7	472.59	176.8541
296.7	472.68	172.2586
296.7	472.78	175.5199
296.7	472.88	173.2222
296.7	472.98	177.7436
296.7	473.08	174.7787
296.7	473.19	176.5577
296.7	473.29	176.9283
296.7	473.39	174.2599
296.7	473.49	176.1129
288.3	466.80	218.6587
288.3	466.84	214.4338
288.3	466.88	209.5418
288.3	466.92	205.6874
288.3	466.96	198.4976
288.3	466.99	197.2376
288.3	467.04	195.9775
288.3	467.08	193.828
288.3	467.18	199.9801
288.3	467.28	192.0491
288.3	467.38	190.9372
288.3	467.48	193.235
288.3	467.58	196.1258
288.3	473.37	187.2312
288.3	473.47	183.6733
288.3	473.57	180.9308
288.3	473.67	188.0465
288.3	473.77	182.1909
288.3	473.87	183.7474
288.3	473.97	185.6005
288.3	474.07	181.0791
288.3	474.17	186.3417
288.3	480.38	185.4522
288.3	480.43	183.5251
288.3	480.53	181.8944
288.3	480.63	179.5225
288.3	480.73	181.1532
288.3	480.83	185.3781
288.3	480.93	184.8593
288.3	481.02	183.1545
288.3	481.19	186.1935
278.7	466.81	233.483
278.7	466.90	219.4741
278.7	466.94	226.3674
278.7	466.98	212.5066
278.7	467.06	205.6874
278.7	467.10	219.3999
278.7	467.14	212.136
278.7	467.22	204.2791
278.7	467.26	208.2817
278.7	467.40	212.2101
278.7	467.50	204.4274
278.7	467.60	208.4299
278.7	467.70	202.5743
278.7	467.81	208.7264
278.7	467.91	201.166
278.7	469.28	203.3897
278.7	469.38	200.2766
278.7	469.48	201.9814
278.7	469.58	200.2024
278.7	469.68	198.3494
278.7	469.78	201.166
278.7	469.88	199.4612
275.7	466.81	245.639
275.7	466.83	241.1917
275.7	466.87	234.1501
275.7	466.91	228.2945
275.7	466.95	225.4038
275.7	466.99	227.4792
275.7	467.03	223.1801
275.7	467.07	218.4364
275.7	467.11	220.2894
275.7	467.15	217.5469
275.7	467.19	213.5443
275.7	467.23	213.1737
275.7	467.33	212.8772
275.7	467.43	213.8408
275.7	467.53	211.543
275.7	467.63	210.6536
275.7	469.17	208.2817
275.7	469.27	210.5053
275.7	469.38	204.5756
275.7	469.48	207.9111
275.7	469.58	205.5392
275.7	469.68	206.3545
275.7	469.78	203.4638
275.7	469.88	204.2791
261.2	466.85	264.2435
261.2	466.86	253.57
261.2	466.90	240.3763
261.2	466.94	230.9629
261.2	466.98	232.5195
261.2	467.02	226.738
261.2	467.06	225.7003
261.2	467.16	221.1789
261.2	467.26	219.1776
261.2	467.76	212.6549
261.2	467.87	211.0242
261.2	467.97	213.9891
261.2	468.07	211.6913
261.2	468.17	208.1335
261.2	468.27	211.2466
261.2	468.37	207.7628
261.2	479.63	195.2363
261.2	479.73	190.1219
261.2	479.83	194.1245
261.2	479.93	192.4938
261.2	480.03	190.196
261.2	480.13	194.1245
261.2	480.23	193.0126
261.2	480.33	191.9749
261.2	480.43	193.5315
260.7	466.83	248.6038
260.7	466.88	237.0409
260.7	466.92	222.513
260.7	466.96	219.5482
260.7	466.99	218.214
260.7	467.04	213.0255
260.7	467.08	213.9891
260.7	467.18	218.4364
260.7	467.28	219.5482
260.7	467.38	214.5079
260.7	467.48	210.5795
260.7	467.58	213.9891
260.7	467.69	207.9111
260.7	467.79	207.6887
260.7	467.89	209.1712
260.7	467.99	206.3545
260.7	468.08	206.5028
260.7	468.19	202.7226
260.7	468.29	205.5392
260.7	468.39	201.9072
260.7	468.49	204.9462
260.7	468.59	202.2037
260.7	468.69	203.9826
255.0	466.82	234.9655
255.0	466.90	231.2594
255.0	466.94	223.8472
255.0	466.98	217.9175
255.0	467.02	219.3999
255.0	467.12	216.4351
255.0	467.22	218.7328
255.0	467.54	208.8747
255.0	467.64	209.1712
255.0	467.74	205.1686
255.0	467.84	205.8357
255.0	467.94	208.3558
255.0	468.04	203.9085
255.0	468.14	205.391
255.0	468.24	202.7967
233.7	466.66	208.5041
233.7	466.67	203.9826
233.7	466.78	200.0542
233.7	466.88	201.4625
233.7	466.98	194.5692
233.7	467.08	191.8267
233.7	467.18	194.0503
233.7	467.28	190.3443
233.7	467.68	184.7851
233.7	467.79	190.0478
233.7	467.88	187.3794
233.7	467.99	189.6772
233.7	468.09	186.3417
233.7	468.19	190.9372
233.7	468.29	188.1206
212.6	466.12	190.1219
212.6	466.16	187.0088
212.6	466.20	188.4171
212.6	466.24	184.1922
212.6	466.28	181.4497
212.6	466.38	183.2286
212.6	466.49	181.1532
212.6	466.53	184.2663
212.6	466.63	179.5966
212.6	466.69	175.1493
212.6	466.79	177.373
212.6	466.89	173.5187
212.6	466.99	176.7059
212.6	467.09	179.5966
212.6	467.19	173.8152
212.6	468.78	173.5928
212.6	468.88	170.5538
212.6	468.98	173.0739
212.6	469.08	170.2573
212.6	469.18	174.1116
212.6	469.28	172.1845
212.6	469.38	171.1468
212.6	469.48	173.6669
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
243.15	100.00	0.0004
243.15	4360.00	0.0004
243.15	9400.00	0.0004
243.15	14450.00	0.0005
243.15	19460.00	0.0005
253.15	100.00	0.0004
253.15	4440.00	0.0004
253.15	9400.00	0.0004
253.15	14460.00	0.0004
253.15	19510.00	0.0004
263.15	100.00	0.0003
263.15	4390.00	0.0003
263.15	9440.00	0.0003
263.15	14430.00	0.0004
263.15	19430.00	0.0004
273.15	100.00	0.0003
273.15	4380.00	0.0003
273.15	9430.00	0.0003
273.15	14470.00	0.0003
273.15	19480.00	0.0003
283.15	100.00	0.0003
283.15	4390.00	0.0003
283.15	9420.00	0.0003
283.15	14500.00	0.0003
283.15	19540.00	0.0003
293.15	100.00	0.0002
293.15	4380.00	0.0002
293.15	9420.00	0.0003
293.15	14480.00	0.0003
293.15	19490.00	0.0003
303.15	220.00	0.0002
303.15	4380.00	0.0002
303.15	9420.00	0.0002
303.15	14500.00	0.0002
303.15	19560.00	0.0003
313.15	410.00	0.0002
313.15	4360.00	0.0002
313.15	9430.00	0.0002
313.15	14520.00	0.0002
313.15	19610.00	0.0002
323.15	350.00	0.0002
323.15	4380.00	0.0002
323.15	9430.00	0.0002
323.15	14490.00	0.0002
323.15	19510.00	0.0002
333.15	410.00	0.0002
333.15	4390.00	0.0002
333.15	9430.00	0.0002
333.15	14470.00	0.0002
333.15	19470.00	0.0002
343.15	340.00	0.0001
343.15	4390.00	0.0002
343.15	9420.00	0.0002
343.15	14460.00	0.0002
343.15	19470.00	0.0002
353.15	410.00	0.0001
353.15	4380.00	0.0001
353.15	9410.00	0.0002
353.15	14440.00	0.0002
353.15	19400.00	0.0002
363.15	510.00	0.0001
363.15	4380.00	0.0001
363.15	9390.00	0.0001
363.15	14400.00	0.0002
363.15	19350.00	0.0002
373.15	650.00	0.0001
373.15	4380.00	0.0001
373.15	9380.00	0.0001
373.15	14400.00	0.0001
373.15	19460.00	0.0002
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Thermal conductivity, W/m/K - Liquid
234.64	100.00	0.1453
234.88	20100.00	0.1543
234.90	30300.00	0.1565
234.92	20100.00	0.1542
235.03	100.00	0.1461
235.09	20200.00	0.1538
235.10	10100.00	0.1496
235.17	5100.00	0.1478
235.22	30200.00	0.1563
235.40	30400.00	0.1559
235.48	10100.00	0.1499
235.53	5100.00	0.1479
235.89	10100.00	0.1500
235.93	5100.00	0.1477
235.94	100.00	0.1456
254.64	20200.00	0.1484
254.74	30000.00	0.1514
254.75	5200.00	0.1408
254.86	30000.00	0.1512
254.91	19700.00	0.1477
254.95	100.00	0.1386
254.98	10100.00	0.1427
254.99	4900.00	0.1411
255.26	100.00	0.1386
255.28	29900.00	0.1512
255.34	20200.00	0.1475
255.37	5100.00	0.1407
255.38	10200.00	0.1432
255.69	10000.00	0.1427
255.70	100.00	0.1386
274.69	100.00	0.1315
274.70	20100.00	0.1409
274.71	5000.00	0.1338
274.71	10000.00	0.1363
274.92	30000.00	0.1447
274.93	20000.00	0.1409
274.96	100.00	0.1319
274.97	10000.00	0.1362
275.21	30000.00	0.1450
275.37	100.00	0.1317
275.38	5000.00	0.1339
275.56	10100.00	0.1364
275.64	30000.00	0.1450
275.70	20000.00	0.1407
275.79	5000.00	0.1340
294.61	20200.00	0.1366
294.79	10100.00	0.1311
294.81	5100.00	0.1280
294.83	29900.00	0.1419
294.93	20000.00	0.1366
295.04	5000.00	0.1280
295.06	10100.00	0.1309
295.08	29700.00	0.1416
295.25	20000.00	0.1365
295.26	10000.00	0.1308
295.31	100.00	0.1248
295.43	5100.00	0.1277
295.53	29900.00	0.1419
295.60	100.00	0.1252
296.02	100.00	0.1250
314.33	5100.00	0.1201
314.44	5300.00	0.1205
314.55	30100.00	0.1357
314.60	10000.00	0.1231
314.95	10100.00	0.1236
314.95	20100.00	0.1291
314.95	30100.00	0.1361
315.01	200.00	0.1187
315.13	200.00	0.1182
315.21	5200.00	0.1202
315.39	30100.00	0.1356
315.50	200.00	0.1182
315.52	10100.00	0.1232
315.56	20200.00	0.1289
315.91	20100.00	0.1287
335.02	5100.00	0.1127
335.13	20300.00	0.1222
335.21	5100.00	0.1127
335.28	200.00	0.1093
335.30	30200.00	0.1275
335.33	10200.00	0.1159
335.33	19900.00	0.1217
335.63	5200.00	0.1126
335.71	20400.00	0.1224
335.72	10100.00	0.1162
335.72	30000.00	0.1271
335.78	200.00	0.1091
336.08	200.00	0.1092
336.13	30200.00	0.1269
336.17	10100.00	0.1159
354.59	30000.00	0.1208
354.75	5000.00	0.1044
355.05	10000.00	0.1084
355.05	30000.00	0.1206
355.08	500.00	0.1001
355.18	20000.00	0.1150
355.32	10100.00	0.1082
355.37	5000.00	0.1048
355.39	30000.00	0.1204
355.52	500.00	0.1001
355.52	20000.00	0.1148
355.74	5000.00	0.1045
355.80	10000.00	0.1079
355.82	500.00	0.1002
356.03	20000.00	0.1147
374.62	10000.00	0.1004
374.70	5200.00	0.0974
374.92	30000.00	0.1132
375.01	29700.00	0.1131
375.06	10000.00	0.1011
375.22	20000.00	0.1081
375.25	5100.00	0.0973
375.40	5000.00	0.0973
375.46	10000.00	0.1008
375.51	29800.00	0.1135
375.62	20000.00	0.1082
375.72	700.00	0.0926
376.18	700.00	0.0925
376.28	20000.00	0.1076
376.80	700.00	0.0923
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[93.08; 292.31]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			8.17270e+01
Coefficient B			-6.60700e+02
Coefficient C			5.70224e+00
Coefficient D			1.69790e-04
Coefficient E			-7.40280e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	93.08	J/mol×K	200.00	Calculated Property
Cp,gas	127.96	J/mol×K	344.44	Calculated Property
Cp,gas	164.50	J/mol×K	488.89	Calculated Property
Cp,gas	195.80	J/mol×K	633.33	Calculated Property
Cp,gas	221.50	J/mol×K	777.78	Calculated Property
Cp,gas	242.41	J/mol×K	922.22	Calculated Property
Cp,gas	259.36	J/mol×K	1066.67	Calculated Property
Cp,gas	273.01	J/mol×K	1211.11	Calculated Property
Cp,gas	283.87	J/mol×K	1355.56	Calculated Property
Cp,gas	292.31	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[149.90; 334.27]	J/mol×K	[156.92; 460.00]	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			1.45290e+02
Coefficient B			-2.82080e+00
Coefficient C			-9.35555e-01
Coefficient D			1.70410e-02
Coefficient E			-7.82380e-06
Temperature range, min.			156.92
Temperature range, max.			460.00
Cp,liquid	149.90	J/mol×K	156.92	Calculated Property
Cp,liquid	152.78	J/mol×K	190.60	Calculated Property
Cp,liquid	157.23	J/mol×K	224.27	Calculated Property
Cp,liquid	163.99	J/mol×K	257.95	Calculated Property
Cp,liquid	174.05	J/mol×K	291.62	Calculated Property
Cp,liquid	188.73	J/mol×K	325.30	Calculated Property
Cp,liquid	209.73	J/mol×K	358.97	Calculated Property
Cp,liquid	239.18	J/mol×K	392.65	Calculated Property
Cp,liquid	279.69	J/mol×K	426.32	Calculated Property
Cp,liquid	334.27	J/mol×K	460.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0007365; 0.0001142]	Pa×s	[200.00; 373.15]	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			1.01390e+01
Coefficient B			-6.17070e+01
Coefficient C			-3.21680e+00
Coefficient D			-9.50220e-09
Coefficient E			2.00000e+00
Temperature range, min.			200.00
Temperature range, max.			373.15
η	0.0007365	Pa×s	200.00	Calculated Property
η	0.0005631	Pa×s	219.24	Calculated Property
η	0.0004395	Pa×s	238.48	Calculated Property
η	0.0003491	Pa×s	257.72	Calculated Property
η	0.0002815	Pa×s	276.96	Calculated Property
η	0.0002301	Pa×s	296.19	Calculated Property
η	0.0001903	Pa×s	315.43	Calculated Property
η	0.0001591	Pa×s	334.67	Calculated Property
η	0.0001342	Pa×s	353.91	Calculated Property
η	0.0001142	Pa×s	373.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[37.54; 0.00]	kJ/mol	[156.85; 466.70]	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			5.33157e+01
Coefficient B			8.76213e-01
Coefficient C			4.75413e-01
Coefficient D			-1.94468e+00
Coefficient E			1.06163e+00
Critical temperature, Tc (K)			4.66700e+02
Temperature range, min.			156.85
Temperature range, max.			466.70
ΔvapH	37.54	kJ/mol	156.85	Calculated Property
ΔvapH	34.64	kJ/mol	191.28	Calculated Property
ΔvapH	32.02	kJ/mol	225.71	Calculated Property
ΔvapH	29.63	kJ/mol	260.13	Calculated Property
ΔvapH	27.37	kJ/mol	294.56	Calculated Property
ΔvapH	25.11	kJ/mol	328.99	Calculated Property
ΔvapH	22.62	kJ/mol	363.42	Calculated Property
ΔvapH	19.49	kJ/mol	397.84	Calculated Property
ΔvapH	14.79	kJ/mol	432.27	Calculated Property
ΔvapH	0.00	kJ/mol	466.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[224.50; 328.55]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41959e+01
Coefficient B			-2.55920e+03
Coefficient C			-4.04930e+01
Temperature range, min.			224.50
Temperature range, max.			328.55
Pvap	1.33	kPa	224.50	Calculated Property
Pvap	3.03	kPa	236.06	Calculated Property
Pvap	6.30	kPa	247.62	Calculated Property
Pvap	12.10	kPa	259.18	Calculated Property
Pvap	21.78	kPa	270.74	Calculated Property
Pvap	37.06	kPa	282.31	Calculated Property
Pvap	60.06	kPa	293.87	Calculated Property
Pvap	93.33	kPa	305.43	Calculated Property
Pvap	139.78	kPa	316.99	Calculated Property
Pvap	202.67	kPa	328.55	Calculated Property
Pvap	[6.09e-04; 3586.22]	kPa	[156.85; 466.70]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			6.84897e+01
Coefficient B			-5.43685e+03
Coefficient C			-8.19387e+00
Coefficient D			7.81256e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 466.74 K.
Temperature range, min.			156.85
Temperature range, max.			466.70
Pvap	6.09e-04	kPa	156.85	Calculated Property
Pvap	0.07	kPa	191.28	Calculated Property
Pvap	1.48	kPa	225.71	Calculated Property
Pvap	12.81	kPa	260.13	Calculated Property
Pvap	61.81	kPa	294.56	Calculated Property
Pvap	203.87	kPa	328.99	Calculated Property
Pvap	519.98	kPa	363.42	Calculated Property
Pvap	1109.34	kPa	397.84	Calculated Property
Pvap	2086.30	kPa	432.27	Calculated Property
Pvap	3586.22	kPa	466.70	Calculated Property
Pvap	[4.07e-04; 3638.11]	kPa	[156.85; 466.70]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			9.51470e+01
Coefficient B			-6.34051e+03
Coefficient C			-1.24379e+01
Coefficient D			1.41292e-05
Coefficient E			0.00000e+00
Temperature range, min.			156.85
Temperature range, max.			466.70
Pvap	4.07e-04	kPa	156.85	Calculated Property
Pvap	0.06	kPa	191.28	Calculated Property
Pvap	1.45	kPa	225.71	Calculated Property
Pvap	12.93	kPa	260.13	Calculated Property
Pvap	62.31	kPa	294.56	Calculated Property
Pvap	203.00	kPa	328.99	Calculated Property
Pvap	511.78	kPa	363.42	Calculated Property
Pvap	1088.13	kPa	397.84	Calculated Property
Pvap	2065.30	kPa	432.27	Calculated Property
Pvap	3638.11	kPa	466.70	Calculated Property
Pvap	[6.94; 188.61]	kPa	[250.04; 328.57]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38662e+01
Coefficient B			-2.44682e+03
Coefficient C			-4.49300e+01
Reference			Ambrose, Sprake, et al., 1972
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			250.04
Temperature range, max.			328.57
Pvap	6.94	kPa	250.04	Calculated Property
Pvap	11.29	kPa	258.77	Calculated Property
Pvap	17.68	kPa	267.49	Calculated Property
Pvap	26.76	kPa	276.22	Calculated Property
Pvap	39.32	kPa	284.94	Calculated Property
Pvap	56.22	kPa	293.67	Calculated Property
Pvap	78.46	kPa	302.39	Calculated Property
Pvap	107.14	kPa	311.12	Calculated Property
Pvap	143.43	kPa	319.84	Calculated Property
Pvap	188.61	kPa	328.57	Calculated Property
Pvap	[345.20; 3404.37]	kPa	[350.14; 466.73]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.48974e+01
Coefficient B			-3.11980e+03
Coefficient C			-5.53700e+00
Reference			Ambrose, Sprake, et al., 1972
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			350.14
Temperature range, max.			466.73
Pvap	345.20	kPa	350.14	Calculated Property
Pvap	479.21	kPa	363.09	Calculated Property
Pvap	650.15	kPa	376.05	Calculated Property
Pvap	864.07	kPa	389.00	Calculated Property
Pvap	1127.23	kPa	401.96	Calculated Property
Pvap	1446.01	kPa	414.91	Calculated Property
Pvap	1826.80	kPa	427.87	Calculated Property
Pvap	2275.99	kPa	440.82	Calculated Property
Pvap	2799.82	kPa	453.78	Calculated Property
Pvap	3404.37	kPa	466.73	Calculated Property
Pvap	[0.52; 58.48]	kPa	[212.40; 293.02]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41235e+01
Coefficient B			-2.53947e+03
Coefficient C			-4.04600e+01
Reference			Taylor and Smith, 1922
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			212.40
Temperature range, max.			293.02
Pvap	0.52	kPa	212.40	Calculated Property
Pvap	1.09	kPa	221.36	Calculated Property
Pvap	2.11	kPa	230.32	Calculated Property
Pvap	3.86	kPa	239.27	Calculated Property
Pvap	6.69	kPa	248.23	Calculated Property
Pvap	11.09	kPa	257.19	Calculated Property
Pvap	17.66	kPa	266.15	Calculated Property
Pvap	27.14	kPa	275.10	Calculated Property
Pvap	40.40	kPa	284.06	Calculated Property
Pvap	58.48	kPa	293.02	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[851.45; 266.48]	kg/m3	[156.85; 466.70]	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			7.22530e+01
Coefficient B			2.71140e-01
Coefficient C			4.66700e+02
Coefficient D			2.84330e-01
Temperature range, min.			156.85
Temperature range, max.			466.70
ρl	851.45	kg/m3	156.85	Calculated Property
ρl	819.49	kg/m3	191.28	Calculated Property
ρl	785.90	kg/m3	225.71	Calculated Property
ρl	750.28	kg/m3	260.13	Calculated Property
ρl	712.05	kg/m3	294.56	Calculated Property
ρl	670.30	kg/m3	328.99	Calculated Property
ρl	623.46	kg/m3	363.42	Calculated Property
ρl	568.34	kg/m3	397.84	Calculated Property
ρl	496.33	kg/m3	432.27	Calculated Property
ρl	266.48	kg/m3	466.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.02]	N/m	[157.15; 307.75]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			4.37220e-02
Coefficient B			-9.08000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			157.15
Temperature range, max.			307.75
γ	0.03	N/m	157.15	Calculated Property
γ	0.03	N/m	173.88	Calculated Property
γ	0.03	N/m	190.62	Calculated Property
γ	0.02	N/m	207.35	Calculated Property
γ	0.02	N/m	224.08	Calculated Property
γ	0.02	N/m	240.82	Calculated Property
γ	0.02	N/m	257.55	Calculated Property
γ	0.02	N/m	274.28	Calculated Property
γ	0.02	N/m	291.02	Calculated Property
γ	0.02	N/m	307.75	Calculated Property
γ	[0.03; 5.20e-06]	N/m	[156.85; 463.60]	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			-8.62930e-03
Coefficient B			7.05130e+01
Coefficient C			-3.74350e+00
Coefficient D			2.82800e-03
Coefficient E			-1.15000e-05
Comment			Range stopped where the equation turns negative; ChemSep gives it to 466.7 K.
Temperature range, min.			156.85
Temperature range, max.			463.60
γ	0.03	N/m	156.85	Calculated Property
γ	0.03	N/m	190.93	Calculated Property
γ	0.03	N/m	225.02	Calculated Property
γ	0.02	N/m	259.10	Calculated Property
γ	0.02	N/m	293.18	Calculated Property
γ	0.01	N/m	327.27	Calculated Property
γ	0.01	N/m	361.35	Calculated Property
γ	0.01	N/m	395.43	Calculated Property
γ	0.00	N/m	429.52	Calculated Property
γ	5.20e-06	N/m	463.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.05]	W/m×K	[200.00; 600.00]	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			-4.49090e-03
Coefficient B			6.14940e-01
Coefficient C			-3.25830e+03
Coefficient D			8.58060e+01
Temperature range, min.			200.00
Temperature range, max.			600.00
λgas	0.01	W/m×K	200.00	Calculated Property
λgas	0.01	W/m×K	244.44	Calculated Property
λgas	0.01	W/m×K	288.89	Calculated Property
λgas	0.02	W/m×K	333.33	Calculated Property
λgas	0.02	W/m×K	377.78	Calculated Property
λgas	0.03	W/m×K	422.22	Calculated Property
λgas	0.03	W/m×K	466.67	Calculated Property
λgas	0.04	W/m×K	511.11	Calculated Property
λgas	0.04	W/m×K	555.56	Calculated Property
λgas	0.05	W/m×K	600.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.19; 0.07]	W/m×K	[156.85; 433.15]	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			-1.42210e-01
Coefficient B			3.00080e+01
Coefficient C			-1.31390e+00
Coefficient D			4.80130e-04
Coefficient E			-2.65720e-06
Temperature range, min.			156.85
Temperature range, max.			433.15
λliquid	0.19	W/m×K	156.85	Calculated Property
λliquid	0.17	W/m×K	187.55	Calculated Property
λliquid	0.16	W/m×K	218.25	Calculated Property
λliquid	0.15	W/m×K	248.95	Calculated Property
λliquid	0.14	W/m×K	279.65	Calculated Property
λliquid	0.12	W/m×K	310.35	Calculated Property
λliquid	0.11	W/m×K	341.05	Calculated Property
λliquid	0.10	W/m×K	371.75	Calculated Property
λliquid	0.09	W/m×K	402.45	Calculated Property
λliquid	0.07	W/m×K	433.15	Calculated Property

Similar Compounds

Find more compounds similar to Ethyl ether.

Mixtures

• Acetonitrile + Ethyl ether
• Acetone + Ethyl ether
• n-Hexane + Acetone + Ethyl ether
• Acetone + Ethyl ether + Methyl Alcohol
• Ethanol + Ethyl ether
• Ethanol + Ethyl ether + Water
• 1,3-Butadiene + Ethyl ether
• 1-Butanol + Ethyl ether
• 1-Butanol + Ethyl ether + Methyl Alcohol
• Acetic acid + Ethyl ether
• Benzene + Ethyl ether
• Benzene + Ethyl ether + Cyclohexane
• Trichloromethane + Ethyl ether
• Ethyl ether + Cyclohexane
• Ethyl ether + Ethyl Acetate
• n-Hexane + Ethyl ether
• n-Hexane + Ethyl ether + Methyl Alcohol
• Ethyl ether + Methyl Alcohol
• Ethyl ether + Tetrahydrofuran
• Ethyl ether + Water

Find more mixtures with Ethyl ether.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• 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.
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Experimental Study of the Thermodynamic Properties of Diethyl Ether (DEE) at Saturation
• Experimental Study of the Isochoric Heat Capacity of Diethyl Ether (DEE) in the Critical and Supercritical Regions
• Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
• Liquid liquid equilibria and partitioning in organic aqueous systems
• Temperature dependence of limiting activity coefficients and Henry s law constants of cyclic and open-chain ethers in water
• Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
• Thermodynamic study of perfluorohexane + ether mixtures VLE, LLE, and HE
• Density and viscosity measurements of diethyl ether from 243 to 373K and up to 20MPa
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Volumetric properties of (N,N-dimethylformamide + aliphatic diethers) at Temperatures ranging from (298.15 to 358.15) K
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Solubility of nicotinic acid in water, ethanol, acetone, diethyl ether, acetonitrile, and dimethyl sulfoxide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
• Thermodynamic of dissolution and hydrogen bond of the pyrrole, N-methylpyrrole with proton acceptors
• Enthalpies of solution and enthalpies of solvation of organic solutes in ethylene glycol at 298.15 K: Prediction and analysis of intermolecular interaction contributions
• Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Vapor Liquid Equilibria of Nitrogen + Diethyl Ether and Nitrogen + 1,1,1,2,2,4,5,5,5-Nonafluoro-4-(trifluoromethyl)-3-pentanone by Experiment, Peng Robinson and PC-SAFT Equations of State
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Experimental High-Pressure Isochoric/Isoplethic Equilibrium for the Systems Propane + n-Pentane and Propane + Diethyl Ether
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
• Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Solubilities of Phosphorus-Containing Compounds in Selected Solvents
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Experimental Study of Chemical Equilibria in the Liquid-Phase Reaction between 1-Octanol and Ethanol to 1-Ethoxyoctane
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Solubility of Atractylenolide III in Hexane, Ethyl Acetate, Diethyl Ether, and Ethanol from (283.2 to 323.2) K
• Refined Flow Microcalorimetric Setup for Measurement of Mixing Enthalpies at High Dilutions: Determination of Infinite Dilution Dissolution Enthalpies of Some Alkanol and Ether Solutes in Water
• Henry s Law Constants for Fragrance and Organic Solvent Compounds in Aqueous Industrial Surfactants
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Excess Enthalpies of Dibromomethane with Acetone, 1,4-Dioxane, Pyridine, Diethyl Ether, Ethyl Methyl Ketone, and Tetrahydrofuran at 303.15 K
• Thermal Conductivity of Liquid Diethyl Ether, Diisopropyl Ether, and Di-n-butyl Ether from (233 to 373) K at Pressures up to 30 MPa
• Measurement and Correlation of Solubility of Pimelic Acid in Ether, Tetrahydrofuran, Ethanol, and Methanol
• Surface Tension of Diethyl Ether, Diisopropyl Ether, and Dibutyl Ether
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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