Chemical Properties of Ethanol, 2-(2-ethoxyethoxy)- (CAS 111-90-0)

InChI

InChI=1S/C6H14O3/c1-2-8-5-6-9-4-3-7/h7H,2-6H2,1H3

InChI Key

XXJWXESWEXIICW-UHFFFAOYSA-N

Formula

C6H14O3

SMILES

CCOCCOCCO

Molecular Weight¹

134.17

CAS

111-90-0

Other Names

• (Ethoxyethoxy)ethanol
• 1-hydroxy-3,6-dioxaoctane
• 2-(2'-ethoxyethoxy)ethanol
• 2-(2-ethoxyethoxy)ethanol
• 2-(Ethoxyethoxy)ethanol
• 2-(«beta»-Ethoxyethoxy)ethanol
• 2-(«beta»-Ethoxyethoxy)ethanol diglycol
• 2-2-Ethoxyethoxy;ethanol
• 3,6-Dioxa-1-oktanol
• 3,6-Dioxaoctan-1-ol
• 3,6-dioxa-1-octanol
• 3-oxa-1,5-pentanediol, ethyl ether
• APV
• Carbitol cellosolve
• Carbitol low gravity
• Carbitol solvent
• DEGEE
• DEGMEE
• Diethoxol
• Diethylene Glycol ethyl ether
• Diethylene glycol monoethyl ether
• Diethylene glycol monomethyl ether
• Diglycol
• Dioxitol-low gravity
• Dowanol
• Dowanol 17
• Eastman DE
• Ehanol, 2,2'-oxybis-, monoethyl ether
• Ektasolve DE
• Ektasolve DE, DE-HG
• Ethoxy diglycol
• Ethyl Di-Icinol
• Ethyl diethylene glycol
• Ethyldiglycol
• Karbitol
• Losungsmittel apv
• Monoethyl ether of diethylene glycol
• O-ethyldigol
• Poly-Solv
• Poly-Solv DE
• Poly-solv DE ethanol, 2,2'-oxybis-, monoethyl ether
• Solvent APV Spec
• Solvolsol
• Transcutol
• Transcutol P
• carbitol
• diethylene glycol, ethyl ether
• diethylene glycol, monoethyl ether
• diglycol monoethyl ether
• dioxitol
• dowanol DE
• ethanol, 2,2'-oxybis-, monoethyl ether
• ethyl carbitol
• ethyl digol
• ethyldiethylene glycol
• ethylene diglycol monoethyl ether

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_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).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• 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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.6986		Relay (1.0) Calculated Property
ΔfG°	-347.18	kJ/mol	Joback Calculated Property
ΔfH°gas	-597.30	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	17.76	kJ/mol	Joback Calculated Property
ΔvapH°	61.54	kJ/mol	Relay (1.0) Calculated Property
IE	9.77	eV	Relay (1.0) Calculated Property
log10WS	0.54		Relay (1.0) Calculated Property
logPoct/wat	0.032		Crippen Calculated Property
McVol	113.010	ml/mol	McGowan Calculated Property
Pc	3167.00 ± 26.00	kPa	NIST
Inp	[951.00; 1011.00]
Inp	982.90		NIST
Inp	Outlier 951.00		NIST
Inp	985.00		NIST
Inp	985.00		NIST
Inp	1006.00		NIST
Inp	1001.00		NIST
Inp	1003.00		NIST
Inp	1007.00		NIST
Inp	1009.10		NIST
Inp	1011.00		NIST
Inp	999.00		NIST
Inp	976.00		NIST
Inp	1007.10		NIST
Inp	986.00		NIST
Inp	979.00		NIST
Inp	985.00		NIST
Inp	1009.10		NIST
Inp	1006.00		NIST
Inp	982.90		NIST
Inp	976.00		NIST
I	[1577.00; 1636.00]
I	1589.00		NIST
I	1577.00		NIST
I	1579.00		NIST
I	1619.00		NIST
I	1615.00		NIST
I	1622.00		NIST
I	1636.00		NIST
I	1583.00		NIST
I	1628.00		NIST
I	1619.00		NIST
I	1589.00		NIST
Tboil	[468.00; 475.20]	K
Tboil	475.20	K	NIST
Tboil	468.00 ± 2.00	K	NIST
Tc	670.00 ± 4.00	K	NIST
Tfus	232.52	K	Relay (1.0) Calculated Property
Vc	0.426	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[252.66; 304.54]	J/mol×K	[473.70; 635.03]
Cp,gas	252.66	J/mol×K	473.70	Joback Calculated Property
Cp,gas	261.94	J/mol×K	500.59	Joback Calculated Property
Cp,gas	270.97	J/mol×K	527.48	Joback Calculated Property
Cp,gas	279.75	J/mol×K	554.37	Joback Calculated Property
Cp,gas	288.27	J/mol×K	581.26	Joback Calculated Property
Cp,gas	296.54	J/mol×K	608.15	Joback Calculated Property
Cp,gas	304.54	J/mol×K	635.03	Joback Calculated Property
Cp,liquid	[296.50; 316.10]	J/mol×K	[275.15; 339.15]
Cp,liquid	296.50	J/mol×K	275.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	296.80	J/mol×K	277.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	297.20	J/mol×K	279.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	297.60	J/mol×K	281.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	298.00	J/mol×K	283.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	298.50	J/mol×K	285.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	298.90	J/mol×K	287.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	299.40	J/mol×K	289.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	299.90	J/mol×K	291.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	300.40	J/mol×K	293.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	300.90	J/mol×K	295.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	301.40	J/mol×K	297.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	301.70	J/mol×K	298.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	301.90	J/mol×K	299.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	302.50	J/mol×K	301.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	303.10	J/mol×K	303.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	303.70	J/mol×K	305.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	304.30	J/mol×K	307.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	304.90	J/mol×K	309.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	305.50	J/mol×K	311.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	306.20	J/mol×K	313.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	306.90	J/mol×K	315.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	307.50	J/mol×K	317.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	308.20	J/mol×K	319.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	309.00	J/mol×K	321.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	309.70	J/mol×K	323.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	310.40	J/mol×K	325.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	311.20	J/mol×K	327.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	312.00	J/mol×K	329.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	312.80	J/mol×K	331.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	313.60	J/mol×K	333.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	314.40	J/mol×K	335.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	315.20	J/mol×K	337.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	316.10	J/mol×K	339.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
η	[0.0035310; 0.0044640]	Pa×s	[293.15; 303.15]
η	0.0044640	Pa×s	293.15	Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
η	0.0039760	Pa×s	298.15	Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
η	0.0035310	Pa×s	303.15	Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
ΔvapH	52.10	kJ/mol	396.50	NIST
n0	[1.42500; 1.42530]		[298.15; 298.15]
n0	1.42530		298.15	Density and refractive index in mixtures of ionic liquids and organic solvents: Correlations and predictions
n0	1.42500		298.15	Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
n0	1.42530		298.15	Volumetric and viscometric study of aqueous binary mixtures of some glycol ethers at T = (275.15 and 283.15) K
ρl	[916.80; 997.10]	kg/m3	[283.15; 373.15]
ρl	997.10	kg/m3	283.15	Thermophysical properties of glycols and glymes
ρl	993.90	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	992.17	kg/m3	288.15	Density, Speed of Sound, and Viscosity of Diethylene Glycol Monoethyl Ether + N,N-Dimethylformamide (Ethanol, Water) at T = 288.15-318.15 K
ρl	992.60	kg/m3	288.15	Thermophysical properties of glycols and glymes
ρl	988.20	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	989.40	kg/m3	293.15	Thermophysical properties of glycols and glymes
ρl	984.90	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	983.70	kg/m3	298.15	Thermophysical properties of glycols and glymes
ρl	983.84	kg/m3	298.15	Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
ρl	983.11	kg/m3	298.15	Density, Speed of Sound, and Viscosity of Diethylene Glycol Monoethyl Ether + N,N-Dimethylformamide (Ethanol, Water) at T = 288.15-318.15 K
ρl	983.08	kg/m3	298.15	Density, Speed of Sound, and Viscosity of Diethylene Glycol Monoethyl Ether + N,N-Dimethylformamide (Ethanol, Water) at T = 288.15-318.15 K
ρl	979.30	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	980.40	kg/m3	303.15	Thermophysical properties of glycols and glymes
ρl	974.18	kg/m3	308.15	Density, Speed of Sound, and Viscosity of Diethylene Glycol Monoethyl Ether + N,N-Dimethylformamide (Ethanol, Water) at T = 288.15-318.15 K
ρl	974.27	kg/m3	308.15	Density, Speed of Sound, and Viscosity of Diethylene Glycol Monoethyl Ether + N,N-Dimethylformamide (Ethanol, Water) at T = 288.15-318.15 K
ρl	976.00	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	974.80	kg/m3	308.15	Thermophysical properties of glycols and glymes
ρl	974.67	kg/m3	308.50	Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
ρl	971.50	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	970.30	kg/m3	313.15	Thermophysical properties of glycols and glymes
ρl	965.33	kg/m3	318.15	Density, Speed of Sound, and Viscosity of Diethylene Glycol Monoethyl Ether + N,N-Dimethylformamide (Ethanol, Water) at T = 288.15-318.15 K
ρl	965.33	kg/m3	318.15	Density, Speed of Sound, and Viscosity of Diethylene Glycol Monoethyl Ether + N,N-Dimethylformamide (Ethanol, Water) at T = 288.15-318.15 K
ρl	967.00	kg/m3	318.15	Thermophysical properties of glycols and glymes
ρl	961.30	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	962.50	kg/m3	323.15	Thermophysical properties of glycols and glymes
ρl	958.10	kg/m3	328.15	Thermophysical properties of glycols and glymes
ρl	952.20	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	953.50	kg/m3	333.15	Thermophysical properties of glycols and glymes
ρl	949.00	kg/m3	338.15	Thermophysical properties of glycols and glymes
ρl	943.10	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	944.40	kg/m3	343.15	Thermophysical properties of glycols and glymes
ρl	939.90	kg/m3	348.15	Thermophysical properties of glycols and glymes
ρl	935.30	kg/m3	353.15	Thermophysical properties of glycols and glymes
ρl	930.70	kg/m3	358.15	Thermophysical properties of glycols and glymes
ρl	926.10	kg/m3	363.15	Thermophysical properties of glycols and glymes
ρl	921.40	kg/m3	368.15	Thermophysical properties of glycols and glymes
ρl	916.80	kg/m3	373.15	Thermophysical properties of glycols and glymes
csound,fluid	[1356.60; 1392.35]	m/s	[293.15; 303.15]
csound,fluid	1392.35	m/s	293.15	Thermodynamics of Mixtures Containing Alkoxyethanols. XXIV. Densities, Excess Molar Volumes, and Speeds of Sound at (293.15, 298.15, and 303.15) K and Isothermal Compressibilities at 298.15 K for 2-(2-Alkoxyethoxy)ethanol + 1-Butanol Systems
csound,fluid	1374.35	m/s	298.15	Thermodynamics of Mixtures Containing Alkoxyethanols. XXIV. Densities, Excess Molar Volumes, and Speeds of Sound at (293.15, 298.15, and 303.15) K and Isothermal Compressibilities at 298.15 K for 2-(2-Alkoxyethoxy)ethanol + 1-Butanol Systems
csound,fluid	1356.60	m/s	303.15	Thermodynamics of Mixtures Containing Alkoxyethanols. XXIV. Densities, Excess Molar Volumes, and Speeds of Sound at (293.15, 298.15, and 303.15) K and Isothermal Compressibilities at 298.15 K for 2-(2-Alkoxyethoxy)ethanol + 1-Butanol Systems

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	997.7
283.15	1000.00	998.2
283.15	2500.00	999.1
283.15	5000.00	1000.6
283.15	7500.00	1002.0
283.15	10000.00	1003.4
283.15	15000.00	1006.1
283.15	20000.00	1008.8
283.15	25000.00	1011.3
293.15	100.00	988.4
293.15	1000.00	988.9
293.15	2500.00	989.8
293.15	5000.00	991.3
293.15	7500.00	992.8
293.15	10000.00	994.3
293.15	15000.00	997.2
293.15	20000.00	999.9
293.15	25000.00	1002.6
303.15	100.00	979.5
303.15	1000.00	980.1
303.15	2500.00	981.1
303.15	5000.00	982.6
303.15	7500.00	984.2
303.15	10000.00	985.8
303.15	15000.00	988.8
303.15	20000.00	991.7
303.15	25000.00	994.6
313.15	100.00	970.6
313.15	1000.00	971.2
313.15	2500.00	972.2
313.15	5000.00	973.9
313.15	7500.00	975.5
313.15	10000.00	977.1
313.15	15000.00	980.3
313.15	20000.00	983.4
313.15	25000.00	986.3
323.15	100.00	961.5
323.15	1000.00	962.1
323.15	2500.00	963.2
323.15	5000.00	965.0
323.15	7500.00	966.8
323.15	10000.00	968.5
323.15	15000.00	971.9
323.15	20000.00	975.1
323.15	25000.00	978.2
333.15	100.00	952.4
333.15	1000.00	953.1
333.15	2500.00	954.3
333.15	5000.00	956.1
333.15	7500.00	958.0
333.15	10000.00	959.7
333.15	15000.00	963.2
333.15	20000.00	966.5
333.15	25000.00	969.8
343.15	100.00	943.4
343.15	1000.00	944.1
343.15	2500.00	945.3
343.15	5000.00	947.3
343.15	7500.00	949.2
343.15	10000.00	951.1
343.15	15000.00	954.8
343.15	20000.00	958.3
343.15	25000.00	961.6
353.15	100.00	934.1
353.15	1000.00	934.9
353.15	2500.00	936.1
353.15	5000.00	938.2
353.15	7500.00	940.2
353.15	10000.00	942.2
353.15	15000.00	946.0
353.15	20000.00	949.7
353.15	25000.00	953.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[357.45; 502.40]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.63980e+01
Coefficient B			-5.15308e+03
Coefficient C			-3.75940e+01
Temperature range, min.			357.45
Temperature range, max.			502.40
Pvap	1.33	kPa	357.45	Calculated Property
Pvap	2.89	kPa	373.56	Calculated Property
Pvap	5.82	kPa	389.66	Calculated Property
Pvap	11.04	kPa	405.77	Calculated Property
Pvap	19.85	kPa	421.87	Calculated Property
Pvap	34.04	kPa	437.98	Calculated Property
Pvap	56.00	kPa	454.08	Calculated Property
Pvap	88.76	kPa	470.19	Calculated Property
Pvap	136.12	kPa	486.29	Calculated Property
Pvap	202.65	kPa	502.40	Calculated Property

Similar Compounds

Find more compounds similar to Ethanol, 2-(2-ethoxyethoxy)-.

Mixtures

• Ethanol, 2-(2-ethoxyethoxy)- + Water
• Ethanol, 2-(2-ethoxyethoxy)- + 1-Hexanol
• Ethanol, 2-(2-ethoxyethoxy)- + 1-Octanol
• Ethanol, 2-(2-ethoxyethoxy)- + 1-Decanol
• Ethanol, 2-(2-ethoxyethoxy)- + Water + Reserpine
• Ethanol, 2-(2-ethoxyethoxy)- + Reserpine
• Ethanol, 2-(2-ethoxyethoxy)- + Propane, 2-ethoxy-2-methyl-
• Ethanol, 2-(2-ethoxyethoxy)- + Propylamine
• Ethanol, 2-(2-ethoxyethoxy)- + Acetaminophen + Water
• Ethanol, 2-(2-ethoxyethoxy)- + Acetaminophen
• Ethanol, 2-(2-ethoxyethoxy)- + tenoxicam
• Ethanol, 2-(2-ethoxyethoxy)- + Cialis
• Ethanol, 2-(2-ethoxyethoxy)- + 1H-Indole-2,3-dione
• Ethanol, 2-(2-ethoxyethoxy)- + 1-Butanol
• Ethanol, 2-(2-ethoxyethoxy)- + Benzyl alcohol
• Ethanol, 2-(2-ethoxyethoxy)- + Ethanol
• Ethanol, 2-(2-ethoxyethoxy)- + Formamide, N,N-dimethyl-

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
• Viscosities of binary mixtures of some n-ethoxyethanols with ethyl tert-butyl ether at T = (293.15, 298.15, and 303.15) K
• Density and refractive index in mixtures of ionic liquids and organic solvents: Correlations and predictions
• Thermodynamic and optical studies of some ethylene glycol ethers in aqueous solutions at T = 298.15 K
• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of diethylene glycol monomethyl ether with 1-alkanols at temperatures from (293.15 to 308.15) K
• Volumetric and viscometric study of aqueous binary mixtures of some glycol ethers at T = (275.15 and 283.15) K
• Thermodynamics of the solubility of reserpine in {{2-(2-ethoxyethoxy)ethanol + water}} mixed solvent systems at different temperatures
• Solubility and thermodynamic function of a new anticancer drug ibrutinib in 2-(2-ethoxyethoxy)ethanol + water mixtures at different temperatures
• Solubility and thermodynamic function of a bioactive compound bergenin in various pharmaceutically acceptable neat solvents at different temperatures
• Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
• Solubility and Thermodynamic Analysis of Tenoxicam in Different Pure Solvents at Different Temperatures
• Thermophysical properties of glycols and glymes
• Density, Speed of Sound, and Viscosity of Diethylene Glycol Monoethyl Ether + N,N-Dimethylformamide (Ethanol, Water) at T = 288.15-318.15 K
• Liquid Density Measurements of Diethylene Glycol Monoalkyl Ethers as a Function of Temperature and Pressure
• Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
• Solubilization Behavior of Paracetamol in Transcutol Water Mixtures at (298.15 to 333.15) K
• Measurement and Correlation of Tadalafil Solubility in Five Pure Solvents at (298.15 to 333.15) K
• Solubility of Metoclopramide Hydrochloride in Six Green Solvents at (298.15 to 338.15) K
• Solubility of N-(4-Chlorophenyl)-2-(pyridin-4-ylcarbonyl)hydrazinecarbothioamide (Isoniazid Analogue) in Transcutol + Water Cosolvent Mixtures at (298.15 to 338.15) K
• Solubility of (2Z)-N-Cyclohexyl-2-(3-hydroxybenzylidine) Hydrazine Carbothioamide in Different Pure Solvents at (298.15 to 338.15) K
• Solubility of N-(4-Chlorophenyl)-2-(pyridin-4-ylcarbonyl)hydrazinecarbothioamide (Isoniazid Analogue) in Five Pure Solvents at (298.15 to 338.15) K
• Correlation of Solubility of Bioactive Compound Reserpine in Eight Green Solvents at (298.15 to 338.15) K
• Measurement, Correlation, and Thermodynamics of Solubility of Isatin in Nine Different Green Solvents at (298.15 to 338.15) K
• Thermodynamics of Mixtures Containing Alkoxyethanols. XXIV. Densities, Excess Molar Volumes, and Speeds of Sound at (293.15, 298.15, and 303.15) K and Isothermal Compressibilities at 298.15 K for 2-(2-Alkoxyethoxy)ethanol + 1-Butanol Systems
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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