Chemical Properties of 2-Propanol, 1-propoxy- (CAS 1569-01-3)

InChI

InChI=1S/C6H14O2/c1-3-4-8-5-6(2)7/h6-7H,3-5H2,1-2H3

InChI Key

FENFUOGYJVOCRY-UHFFFAOYSA-N

Formula

C6H14O2

SMILES

CCCOCC(C)O

Molecular Weight¹

118.17

CAS

1569-01-3

Other Names

• 1-propoxy-2-propanol
• 1-propoxypropan-2-ol
• Propasol solvent P
• Propylene glycol n-propyl ether
• Propylene glycol-n-monopropyl ether
• propane, 2-hydroxy-1-propoxy-
• propylene glycol, 1-propyl 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).
• 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_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : 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	0.4966		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ΔfG°	-244.62	kJ/mol	Joback Calculated Property
ΔfH°gas	-487.79	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	13.05	kJ/mol	Joback Calculated Property
ΔvapH°	55.24	kJ/mol	Relay (1.0) Calculated Property
IE	9.71	eV	Relay (1.0) Calculated Property
log10WS	-0.05		Relay (1.0) Calculated Property
logPoct/wat	0.794		Crippen Calculated Property
McVol	107.140	ml/mol	McGowan Calculated Property
Pc	[3000.00; 3051.00]	kPa
Pc	3000.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	3051.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Inp	[797.00; 840.10]
Inp	797.00		NIST
Inp	805.00		NIST
Inp	839.70		NIST
Inp	840.10		NIST
Ip	1263.80		NIST
Tboil	422.95	K	NIST
Tc	[605.00; 605.10]	K
Tc	605.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	605.10	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tfus	193.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Vc	0.398	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[237.41; 314.70]	J/mol×K	[193.19; 373.15]
Cp,liquid	237.41	J/mol×K	193.19	Melting Point, Enthalpy of Fusion, and Heat Capacity Measurements of Several Polyfunctional, Industrially Important Compounds by Differential Scanning Calorimetry
Cp,liquid	247.93	J/mol×K	223.15	Melting Point, Enthalpy of Fusion, and Heat Capacity Measurements of Several Polyfunctional, Industrially Important Compounds by Differential Scanning Calorimetry
Cp,liquid	271.09	J/mol×K	273.16	Melting Point, Enthalpy of Fusion, and Heat Capacity Measurements of Several Polyfunctional, Industrially Important Compounds by Differential Scanning Calorimetry
Cp,liquid	271.60	J/mol×K	275.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	272.40	J/mol×K	276.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	273.20	J/mol×K	278.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	274.00	J/mol×K	279.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	274.80	J/mol×K	281.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	275.60	J/mol×K	282.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	276.40	J/mol×K	284.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	277.20	J/mol×K	285.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	278.00	J/mol×K	287.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	278.80	J/mol×K	288.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	279.60	J/mol×K	290.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	280.30	J/mol×K	291.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	281.10	J/mol×K	293.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	281.90	J/mol×K	294.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	282.60	J/mol×K	296.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	283.40	J/mol×K	297.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	283.60	J/mol×K	298.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	284.10	J/mol×K	299.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	284.90	J/mol×K	300.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	285.60	J/mol×K	302.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	286.40	J/mol×K	303.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	287.10	J/mol×K	305.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	287.80	J/mol×K	306.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	288.50	J/mol×K	308.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	289.20	J/mol×K	309.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	290.00	J/mol×K	311.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	290.70	J/mol×K	312.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	291.40	J/mol×K	314.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	292.10	J/mol×K	315.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	292.80	J/mol×K	317.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	293.40	J/mol×K	318.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	294.10	J/mol×K	320.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	294.80	J/mol×K	321.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	295.50	J/mol×K	323.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	290.12	J/mol×K	323.16	Melting Point, Enthalpy of Fusion, and Heat Capacity Measurements of Several Polyfunctional, Industrially Important Compounds by Differential Scanning Calorimetry
Cp,liquid	296.10	J/mol×K	324.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	296.80	J/mol×K	326.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	297.50	J/mol×K	327.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	298.10	J/mol×K	329.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	298.80	J/mol×K	330.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	299.40	J/mol×K	332.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	300.00	J/mol×K	333.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	300.70	J/mol×K	335.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	301.30	J/mol×K	336.65	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	301.90	J/mol×K	338.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	302.40	J/mol×K	339.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
Cp,liquid	314.70	J/mol×K	373.15	Melting Point, Enthalpy of Fusion, and Heat Capacity Measurements of Several Polyfunctional, Industrially Important Compounds by Differential Scanning Calorimetry
Pvap	[0.34; 74.98]	kPa	[298.15; 413.15]
Pvap	0.34	kPa	298.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	0.48	kPa	303.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	0.67	kPa	308.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	0.94	kPa	313.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	1.27	kPa	318.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	1.71	kPa	323.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	2.26	kPa	328.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	2.97	kPa	333.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	3.84	kPa	338.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	4.95	kPa	343.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	6.29	kPa	348.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	7.96	kPa	353.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	9.95	kPa	358.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	12.38	kPa	363.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	15.27	kPa	368.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	18.70	kPa	373.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	22.65	kPa	378.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	27.42	kPa	383.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	32.80	kPa	388.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	39.18	kPa	393.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	46.38	kPa	398.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	54.75	kPa	403.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	64.10	kPa	408.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
Pvap	74.98	kPa	413.15	Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
ρl	[876.28; 894.46]	kg/m3	[283.15; 303.15]
ρl	894.46	kg/m3	283.15	Volumetric properties of (1-propoxypropan-2-ol + water) mixtures between (283 and 303) K: The effect of branching on alkoxyalcohols
ρl	889.96	kg/m3	288.15	Volumetric properties of (1-propoxypropan-2-ol + water) mixtures between (283 and 303) K: The effect of branching on alkoxyalcohols
ρl	885.46	kg/m3	293.15	Volumetric properties of (1-propoxypropan-2-ol + water) mixtures between (283 and 303) K: The effect of branching on alkoxyalcohols
ρl	880.84	kg/m3	298.15	Volumetric properties of (1-propoxypropan-2-ol + water) mixtures between (283 and 303) K: The effect of branching on alkoxyalcohols
ρl	876.28	kg/m3	303.15	Volumetric properties of (1-propoxypropan-2-ol + water) mixtures between (283 and 303) K: The effect of branching on alkoxyalcohols
csound,fluid	[1211.05; 1301.94]	m/s	[283.15; 308.15]
csound,fluid	1301.94	m/s	283.15	Ultrasound speeds and molar isentropic compressions of aqueous 1-propoxypropan-2-ol mixtures from T = (283.15 to 303.15) K. Influence of solute structure
csound,fluid	1283.21	m/s	288.15	Ultrasound speeds and molar isentropic compressions of aqueous 1-propoxypropan-2-ol mixtures from T = (283.15 to 303.15) K. Influence of solute structure
csound,fluid	1282.87	m/s	288.15	Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid	1264.52	m/s	293.15	Ultrasound speeds and molar isentropic compressions of aqueous 1-propoxypropan-2-ol mixtures from T = (283.15 to 303.15) K. Influence of solute structure
csound,fluid	1266.18	m/s	293.15	Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid	1245.79	m/s	298.15	Ultrasound speeds and molar isentropic compressions of aqueous 1-propoxypropan-2-ol mixtures from T = (283.15 to 303.15) K. Influence of solute structure
csound,fluid	1247.82	m/s	298.15	Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid	1227.33	m/s	303.15	Ultrasound speeds and molar isentropic compressions of aqueous 1-propoxypropan-2-ol mixtures from T = (283.15 to 303.15) K. Influence of solute structure
csound,fluid	1229.44	m/s	303.15	Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
csound,fluid	1211.05	m/s	308.15	Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	895.1
283.15	1000.00	895.7
283.15	2500.00	896.7
283.15	5000.00	898.5
283.15	7500.00	900.1
283.15	10000.00	901.8
283.15	15000.00	905.0
283.15	20000.00	908.1
283.15	25000.00	911.1
293.15	100.00	886.0
293.15	1000.00	886.6
293.15	2500.00	887.7
293.15	5000.00	889.6
293.15	7500.00	891.3
293.15	10000.00	893.1
293.15	15000.00	896.5
293.15	20000.00	899.8
293.15	25000.00	902.9
303.15	100.00	876.4
303.15	1000.00	877.2
303.15	2500.00	878.4
303.15	5000.00	880.3
303.15	7500.00	882.2
303.15	10000.00	884.0
303.15	15000.00	887.6
303.15	20000.00	891.1
303.15	25000.00	894.4
313.15	100.00	866.9
313.15	1000.00	867.6
313.15	2500.00	868.9
313.15	5000.00	871.0
313.15	7500.00	873.0
313.15	10000.00	875.0
313.15	15000.00	878.8
313.15	20000.00	882.4
313.15	25000.00	885.9
323.15	100.00	857.2
323.15	1000.00	858.0
323.15	2500.00	859.3
323.15	5000.00	861.4
323.15	7500.00	863.5
323.15	10000.00	865.6
323.15	15000.00	869.6
323.15	20000.00	873.5
323.15	25000.00	877.2
333.15	100.00	847.1
333.15	1000.00	847.9
333.15	2500.00	849.3
333.15	5000.00	851.7
333.15	7500.00	853.9
333.15	10000.00	856.1
333.15	15000.00	860.3
333.15	20000.00	864.3
333.15	25000.00	868.1
343.15	100.00	837.5
343.15	1000.00	838.4
343.15	2500.00	840.0
343.15	5000.00	842.4
343.15	7500.00	844.9
343.15	10000.00	847.2
343.15	15000.00	851.8
343.15	20000.00	856.0
343.15	25000.00	860.1
353.15	100.00	827.3
353.15	1000.00	828.3
353.15	2500.00	829.9
353.15	5000.00	832.6
353.15	7500.00	835.2
353.15	10000.00	837.7
353.15	15000.00	842.5
353.15	20000.00	847.0
353.15	25000.00	851.3
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[160.36; 366.58]	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			2.65430e+01
Coefficient B			5.50540e-01
Coefficient C			-2.25200e-04
Coefficient D			1.47000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	160.36	J/mol×K	273.00	Calculated Property
Cp,gas	193.78	J/mol×K	353.78	Calculated Property
Cp,gas	224.46	J/mol×K	434.56	Calculated Property
Cp,gas	252.46	J/mol×K	515.33	Calculated Property
Cp,gas	277.82	J/mol×K	596.11	Calculated Property
Cp,gas	300.57	J/mol×K	676.89	Calculated Property
Cp,gas	320.78	J/mol×K	757.67	Calculated Property
Cp,gas	338.49	J/mol×K	838.44	Calculated Property
Cp,gas	353.74	J/mol×K	919.22	Calculated Property
Cp,gas	366.58	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.6326633; 0.0002702]	Pa×s	[193.15; 423.53]	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			-1.47208e+01
Coefficient B			2.75490e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			193.15
Temperature range, max.			423.53
η	0.6326633	Pa×s	193.15	Calculated Property
η	0.1192062	Pa×s	218.75	Calculated Property
η	0.0318643	Pa×s	244.35	Calculated Property
η	0.0109391	Pa×s	269.94	Calculated Property
η	0.0045195	Pa×s	295.54	Calculated Property
η	0.0021498	Pa×s	321.14	Calculated Property
η	0.0011412	Pa×s	346.74	Calculated Property
η	0.0006609	Pa×s	372.34	Calculated Property
η	0.0004106	Pa×s	397.94	Calculated Property
η	0.0002702	Pa×s	423.53	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[323.58; 446.21]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.61743e+01
Coefficient B			-4.21246e+03
Coefficient C			-5.84240e+01
Temperature range, min.			323.58
Temperature range, max.			446.21
Pvap	1.33	kPa	323.58	Calculated Property
Pvap	2.90	kPa	337.21	Calculated Property
Pvap	5.86	kPa	350.83	Calculated Property
Pvap	11.13	kPa	364.46	Calculated Property
Pvap	20.01	kPa	378.08	Calculated Property
Pvap	34.30	kPa	391.71	Calculated Property
Pvap	56.35	kPa	405.33	Calculated Property
Pvap	89.16	kPa	418.96	Calculated Property
Pvap	136.44	kPa	432.58	Calculated Property
Pvap	202.65	kPa	446.21	Calculated Property

Similar Compounds

Find more compounds similar to 2-Propanol, 1-propoxy-.

Mixtures

• 2-Propanol, 1-propoxy- + Water
• 2-Propanol, 1-propoxy- + Methyl Alcohol
• 2-Propanol, 1-propoxy- + Ethanol
• 2-Propanol, 1-propoxy- + 1-Hexanol
• 2-Propanol, 1-propoxy- + Dodecane + Water
• 2-Propanol, 1-propoxy- + Decane + Water
• 2-Propanol, 1-propoxy- + Hexadecane + Water
• 2-Propanol, 1-propoxy- + Acetic acid, methyl ester
• 2-Propanol, 1-propoxy- + Ethyl Acetate
• 2-Propanol, 1-propoxy- + Acetic acid, butyl ester
• 2-Propanol, 1-propoxy- + Tetradecane + Water
• 2-Propanol, 1-propoxy- + 2-Butanol

Sources

• 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).
• 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.
• 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.
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
• Phase behavior of glycol ether surfactant systems in the presence of brine and hydrocarbon: Experiment and modeling
• Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
• Volumetric properties of (1-propoxypropan-2-ol + water) mixtures between (283 and 303) K: The effect of branching on alkoxyalcohols
• Ultrasound speeds and molar isentropic compressions of aqueous 1-propoxypropan-2-ol mixtures from T = (283.15 to 303.15) K. Influence of solute structure
• (Liquid + liquid) equilibria for the ternary system (water + dodecane + propylene glycol n-propyl ether)
• Water activity in 1-propoxypropan-2-ol aqueous mixtures at T = 298 K
• Energetic characterisation of the system (water + 1-propoxypropan-2-ol) at T = 298.15 K
• Melting Point, Enthalpy of Fusion, and Heat Capacity Measurements of Several Polyfunctional, Industrially Important Compounds by Differential Scanning Calorimetry
• Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems
• PpT Measurements and EoS Predictions of Glycol Ethers from (283.15 to 353.15) K at Pressures up to 25 MPa
• Liquid-Liquid Equilibria for the Ternary System Water + Hexadecane + Propylene Glycol n-Propyl Ether
• Liquid Liquid Equilibria for the Ternary System Water + Tetradecane + Propylene Glycol n-Propyl Ether
• Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
• Solubilities of Three Phosphorus Flame Retardants in Selected Organic Solvents
• Joback Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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