Chemical Properties of Ethanol, 2-propoxy- (CAS 2807-30-9)

InChI

InChI=1S/C5H12O2/c1-2-4-7-5-3-6/h6H,2-5H2,1H3

InChI Key

YEYKMVJDLWJFOA-UHFFFAOYSA-N

Formula

C5H12O2

SMILES

CCCOCCO

Molecular Weight¹

104.15

CAS

2807-30-9

Other Names

• 2-Propyloxyethanol
• 2-propoxyethanol
• 3-Oxa-1-hexanol
• Eastman EP
• Ektasolve EP
• Ethyleneglycol mono-n-propyl ether
• Monopropyl ether of ethylene glycol
• Propoxyethanol
• Propyl glycol
• ethylene glycol monopropyl ether
• ethylene glycol propyl ether
• propyl cellosolve

• 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).
• ε_r : Dielectric Constant (Relative permittivity).
• 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).
• 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_boilr : Boiling point at reduced pressure (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	0.6373		Relay (1.0) Calculated Property
ΔfG°	-250.60	kJ/mol	Joback Calculated Property
ΔfH°gas	-453.62	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	13.98	kJ/mol	Joback Calculated Property
ΔvapH°	[52.10; 52.13]	kJ/mol
ΔvapH°	52.13	kJ/mol	NIST
ΔvapH°	52.10 ± 0.10	kJ/mol	NIST
IE	9.82	eV	Relay (1.0) Calculated Property
log10WS	0.25		Relay (1.0) Calculated Property
logPoct/wat	0.405		Crippen Calculated Property
McVol	93.050	ml/mol	McGowan Calculated Property
Pc	3650.00 ± 20.00	kPa	NIST
ρc	286.41 ± 6.25	kg/m3	NIST
Inp	[790.00; 819.00]
Inp	819.00		NIST
Inp	800.70		NIST
Inp	802.00		NIST
Inp	809.00		NIST
Inp	790.00		NIST
Inp	816.00		NIST
Inp	802.00		NIST
Inp	819.00		NIST
Inp	809.00		NIST
Inp	816.00		NIST
Inp	800.70		NIST
I	[1325.90; 1325.90]
I	1325.90		NIST
I	1325.90		NIST
Tboil	[422.90; 424.50]	K
Tboil	422.90	K	NIST
Tboil	424.50 ± 0.60	K	NIST
Tc	[614.60; 615.20]	K
Tc	615.20 ± 1.00	K	NIST
Tc	614.60 ± 0.50	K	NIST
Tfus	197.71	K	Relay (1.0) Calculated Property
Vc	0.340	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[231.60; 259.90]	J/mol×K	[275.15; 339.15]
Cp,liquid	231.60	J/mol×K	275.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	232.40	J/mol×K	277.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	233.30	J/mol×K	279.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	234.10	J/mol×K	281.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	235.00	J/mol×K	283.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	235.80	J/mol×K	285.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	236.60	J/mol×K	287.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	237.50	J/mol×K	289.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	238.30	J/mol×K	291.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	239.20	J/mol×K	293.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	240.10	J/mol×K	295.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	240.90	J/mol×K	297.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	241.40	J/mol×K	298.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	241.78	J/mol×K	298.15	NIST
Cp,liquid	241.60	J/mol×K	298.15	NIST
Cp,liquid	244.30	J/mol×K	298.15	NIST
Cp,liquid	241.80	J/mol×K	299.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	242.70	J/mol×K	301.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	243.50	J/mol×K	303.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	244.40	J/mol×K	305.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	245.30	J/mol×K	307.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	246.20	J/mol×K	309.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	247.10	J/mol×K	311.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	248.00	J/mol×K	313.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	248.90	J/mol×K	315.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	249.80	J/mol×K	317.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	250.70	J/mol×K	319.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	251.60	J/mol×K	321.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	252.50	J/mol×K	323.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	253.40	J/mol×K	325.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	254.30	J/mol×K	327.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	255.20	J/mol×K	329.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	256.10	J/mol×K	331.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	257.10	J/mol×K	333.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	258.00	J/mol×K	335.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	258.90	J/mol×K	337.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Cp,liquid	259.90	J/mol×K	339.15	Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
εr	[11.19; 11.76]		[293.15; 303.15]
εr	11.76		293.15	Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
εr	11.50		298.15	Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
εr	11.19		303.15	Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
ΔvapH	[41.40; 46.30]	kJ/mol	[386.00; 422.90]
ΔvapH	46.30	kJ/mol	386.00	NIST
ΔvapH	41.40	kJ/mol	422.90	NIST
Pvap	[0.45; 100.00]	kPa	[303.15; 422.75]
Pvap	0.45	kPa	303.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	0.87	kPa	313.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	0.89	kPa	313.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	1.59	kPa	323.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	1.61	kPa	323.15	Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
Pvap	60.00	kPa	406.13	Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
Pvap	60.00	kPa	406.15	Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
Pvap	60.00	kPa	406.15	Isobaric Vapor Liquid Equilibria for the 1-Propanol + Ethylene Glycol Monopropyl Ether and 1-Butanol + Ethylene Glycol Monopropyl Ether Systems
Pvap	80.00	kPa	415.28	Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
Pvap	80.00	kPa	415.30	Isobaric Vapor Liquid Equilibria for the 1-Propanol + Ethylene Glycol Monopropyl Ether and 1-Butanol + Ethylene Glycol Monopropyl Ether Systems
Pvap	80.00	kPa	415.30	Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
Pvap	100.00	kPa	422.73	Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
Pvap	100.00	kPa	422.75	Isobaric Vapor Liquid Equilibria for the 1-Propanol + Ethylene Glycol Monopropyl Ether and 1-Butanol + Ethylene Glycol Monopropyl Ether Systems
Pvap	100.00	kPa	422.75	Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
ρl	[881.49; 915.95]	kg/m3	[288.15; 328.15]
ρl	915.95	kg/m3	288.15	Static permittivity, density, speed of sound, and refractive index of 2-propoxyethanol mixtures with water in a wide temperature range
ρl	911.59	kg/m3	293.15	Static permittivity, density, speed of sound, and refractive index of 2-propoxyethanol mixtures with water in a wide temperature range
ρl	907.21	kg/m3	298.15	Static permittivity, density, speed of sound, and refractive index of 2-propoxyethanol mixtures with water in a wide temperature range
ρl	908.31	kg/m3	298.15	Study of thermophysical properties of the binary mixtures of ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate and 2-propoxyethanol from T = (298.15 to 328.15) K at atmospheric pressure
ρl	907.88	kg/m3	298.15	Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
ρl	908.00	kg/m3	298.15	An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
ρl	907.23	kg/m3	298.15	Thermodynamic properties and sPC-SAFT modeling of 2-ethoxyethanol, 2-propoxyethanol and 2-butoxyethanol from T = (293.15-413.15) K and pressure up to 30 MPa
ρl	902.81	kg/m3	303.15	Static permittivity, density, speed of sound, and refractive index of 2-propoxyethanol mixtures with water in a wide temperature range
ρl	903.00	kg/m3	303.15	An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
ρl	898.37	kg/m3	308.15	Static permittivity, density, speed of sound, and refractive index of 2-propoxyethanol mixtures with water in a wide temperature range
ρl	899.00	kg/m3	308.15	An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
ρl	899.50	kg/m3	308.15	Study of thermophysical properties of the binary mixtures of ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate and 2-propoxyethanol from T = (298.15 to 328.15) K at atmospheric pressure
ρl	893.91	kg/m3	313.15	Static permittivity, density, speed of sound, and refractive index of 2-propoxyethanol mixtures with water in a wide temperature range
ρl	895.00	kg/m3	313.15	An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
ρl	889.41	kg/m3	318.15	Static permittivity, density, speed of sound, and refractive index of 2-propoxyethanol mixtures with water in a wide temperature range
ρl	890.56	kg/m3	318.15	Study of thermophysical properties of the binary mixtures of ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate and 2-propoxyethanol from T = (298.15 to 328.15) K at atmospheric pressure
ρl	890.00	kg/m3	318.15	An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
ρl	881.49	kg/m3	328.15	Study of thermophysical properties of the binary mixtures of ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate and 2-propoxyethanol from T = (298.15 to 328.15) K at atmospheric pressure
csound,fluid	[1281.14; 1316.61]	m/s	[293.15; 303.15]
csound,fluid	1316.61	m/s	293.15	Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
csound,fluid	1298.58	m/s	298.15	Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
csound,fluid	1281.14	m/s	303.15	Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems

Pressure Dependent Properties

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[139.46; 314.45]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.91340e+01
Coefficient B			4.49620e-01
Coefficient C			-1.67600e-04
Coefficient D			3.30000e-09
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	139.46	J/mol×K	273.00	Calculated Property
Cp,gas	167.37	J/mol×K	353.78	Calculated Property
Cp,gas	193.14	J/mol×K	434.56	Calculated Property
Cp,gas	216.78	J/mol×K	515.33	Calculated Property
Cp,gas	238.30	J/mol×K	596.11	Calculated Property
Cp,gas	257.71	J/mol×K	676.89	Calculated Property
Cp,gas	275.02	J/mol×K	757.67	Calculated Property
Cp,gas	290.24	J/mol×K	838.44	Calculated Property
Cp,gas	303.38	J/mol×K	919.22	Calculated Property
Cp,gas	314.45	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0464966; 0.0002203]	Pa×s	[229.16; 430.43]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.45142e+01
Coefficient B			2.62292e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			229.16
Temperature range, max.			430.43
η	0.0464966	Pa×s	229.16	Calculated Property
η	0.0168057	Pa×s	251.52	Calculated Property
η	0.0071724	Pa×s	273.89	Calculated Property
η	0.0034810	Pa×s	296.25	Calculated Property
η	0.0018699	Pa×s	318.61	Calculated Property
η	0.0010898	Pa×s	340.98	Calculated Property
η	0.0006787	Pa×s	363.34	Calculated Property
η	0.0004466	Pa×s	385.70	Calculated Property
η	0.0003077	Pa×s	408.07	Calculated Property
η	0.0002203	Pa×s	430.43	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[325.70; 445.45]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.64940e+01
Coefficient B			-4.31962e+03
Coefficient C			-5.91610e+01
Temperature range, min.			325.70
Temperature range, max.			445.45
Pvap	1.33	kPa	325.70	Calculated Property
Pvap	2.88	kPa	339.01	Calculated Property
Pvap	5.81	kPa	352.31	Calculated Property
Pvap	11.01	kPa	365.62	Calculated Property
Pvap	19.79	kPa	378.92	Calculated Property
Pvap	33.94	kPa	392.23	Calculated Property
Pvap	55.86	kPa	405.53	Calculated Property
Pvap	88.61	kPa	418.84	Calculated Property
Pvap	136.00	kPa	432.14	Calculated Property
Pvap	202.67	kPa	445.45	Calculated Property
Pvap	[6.81; 97.59]	kPa	[350.30; 421.90]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46791e+01
Coefficient B			-3.46530e+03
Coefficient C			-7.87440e+01
Reference			Dykyj, Seprakova, et al., 1957, 2
Temperature range, min.			350.30
Temperature range, max.			421.90
Pvap	6.81	kPa	350.30	Calculated Property
Pvap	9.79	kPa	358.26	Calculated Property
Pvap	13.80	kPa	366.21	Calculated Property
Pvap	19.09	kPa	374.17	Calculated Property
Pvap	25.96	kPa	382.12	Calculated Property
Pvap	34.76	kPa	390.08	Calculated Property
Pvap	45.88	kPa	398.03	Calculated Property
Pvap	59.73	kPa	405.99	Calculated Property
Pvap	76.79	kPa	413.94	Calculated Property
Pvap	97.59	kPa	421.90	Calculated Property
Pvap	[6.81; 97.59]	kPa	[350.30; 421.90]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46791e+01
Coefficient B			-3.46530e+03
Coefficient C			-7.87440e+01
Reference			Dykyj, Seprakova, et al., 1957
Temperature range, min.			350.30
Temperature range, max.			421.90
Pvap	6.81	kPa	350.30	Calculated Property
Pvap	9.79	kPa	358.26	Calculated Property
Pvap	13.80	kPa	366.21	Calculated Property
Pvap	19.09	kPa	374.17	Calculated Property
Pvap	25.96	kPa	382.12	Calculated Property
Pvap	34.76	kPa	390.08	Calculated Property
Pvap	45.88	kPa	398.03	Calculated Property
Pvap	59.73	kPa	405.99	Calculated Property
Pvap	76.79	kPa	413.94	Calculated Property
Pvap	97.59	kPa	421.90	Calculated Property

Similar Compounds

Find more compounds similar to Ethanol, 2-propoxy-.

Mixtures

• Ethanol, 2-propoxy- + Heptane
• Ethanol, 2-propoxy- + Octane
• Ethanol, 2-propoxy- + Ethanol, 2,2'-oxybis-
• Ethanol, 2-propoxy- + Triethylene glycol
• Ethanol, 2-propoxy- + Tetraethylene glycol
• Ethanol, 2-propoxy- + sodium chloride + Water
• Diethyl carbonate + Ethanol, 2-propoxy-
• n-Hexane + Ethanol, 2-propoxy-
• Ethanol, 2-propoxy- + Water
• Ethanol, 2-propoxy- + 2-Propanol
• Ethanol, 2-propoxy- + PHOSPHONIC ACID, PHENYL-
• 1-Propanol + Ethanol, 2-propoxy-
• Ethanol, 2-propoxy- + 1-Butanol
• Ethanol, 2-propoxy- + n-Butyl ether

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Isobaric vapor-liquid equilibria for the n-heptane + ethylene glycol monopropyl ether and n-octane + ethylene glycol monopropyl ether systems
• Temperature dependence of ternary phase diagrams for water + sodium chloride + ethylene glycol monopropyl ether at atmospheric pressure
• Thermodynamic properties and sPC-SAFT modeling of 2-ethoxyethanol, 2-propoxyethanol and 2-butoxyethanol from T = (293.15-413.15) K and pressure up to 30 MPa
• Excess molar volumes and deviations of the relative permittivity of the binary mixtures of 2-propoxyethanol with diethylene, triethylene, and tetraethylene glycols at various temperatures
• Measurement and correlation of (vapor + liquid) equilibria for the {2-propoxyethanol (C3E1) + n-hexane} and the {2-propoxyethanol (C3E1) + n-heptane} systems
• Studies on intermolecular interactions in nitrobenzene + alkoxyethanol binary mixtures by relative permittivity measurements at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
• Study of thermophysical properties of the binary mixtures of ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate and 2-propoxyethanol from T = (298.15 to 328.15) K at atmospheric pressure
• Static permittivity, density, speed of sound, and refractive index of 2-propoxyethanol mixtures with water in a wide temperature range
• Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
• Partial molar volumes of organic solutes in water. XXIX. Four 2-alkoxyethanols at temperatures T = (298 K to 573) K and pressures up to 30 MPa
• An experimental investigation of molecular interactions between [Emim][triflate] ionic liquid & 2-alkoxyethanols and theoretical comparison by PFP theory
• Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
• Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
• Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
• Partial Molar Volumes and Partial Molar Isentropic Compressions of Four 2-Alkoxyethanols at Infinite Dilution in Water at Temperatures T = 278 343 K and Atmospheric Pressure
• Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
• Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
• Isobaric Vapor Liquid Equilibria for the 1-Propanol + Ethylene Glycol Monopropyl Ether and 1-Butanol + Ethylene Glycol Monopropyl Ether Systems
• Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
• Thermodynamics of Mixtures Containing Alkoxyethanols. Part XXVI. Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K, and Isentropic or Isothermal Compressibilities at 298.15 K for 2-Methoxyethanol + Alkoxyethanol or 2-Propoxyethanol + Dibutylether Systems
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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