Chemical Properties of 1-(1-methyl-2-propoxyethoxy)-2-propanol

InChI

InChI=1S/C9H20O3/c1-4-5-11-7-9(3)12-6-8(2)10/h8-10H,4-7H2,1-3H3

InChI Key

WEZPLQKRXDBPEP-UHFFFAOYSA-N

Formula

C9H20O3

SMILES

CCCOCC(C)OCC(C)O

Molecular Weight¹

176.26

Other Names

• 2-propanol, 1-(1-methyl-2-propoxyethoxy)-
• dipropylene glycol, monopropyl ether
• dipropylene glycol, propyl ether
• dowanol dpnP
• 1-(1-propoxypropan-2-yloxy)propan-2-ol

• 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_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• c_sound,fluid : Speed of sound in fluid (m/s).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Cheméo can also estimate Critical Volume, Enthalpy of formation at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, Ionization energy, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[374.40; 411.80]	J/mol×K	[275.15; 339.15]
Cp,liquid	374.40	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	375.30	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	376.20	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	377.10	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	378.00	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	378.90	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	379.80	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	380.70	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	381.60	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	382.50	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	383.30	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	384.20	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	385.10	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	386.00	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	386.90	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	387.80	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	388.10	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	388.60	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	389.50	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	390.40	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	391.30	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	392.20	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	393.00	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	393.90	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	394.80	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	395.70	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	396.50	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	397.40	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	398.30	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	399.20	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	400.00	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	400.90	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	401.80	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	402.60	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	403.50	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	404.40	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	405.20	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	406.10	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	406.90	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	407.80	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	408.70	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	409.50	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	410.40	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	411.20	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	411.80	J/mol×K	339.15	Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
ρl	[915.65; 920.14]	kg/m3	[293.15; 298.15]
ρl	920.14	kg/m3	293.15	Liquid-liquid equilibria for the ternary system (water + hexadecane + dipropylene glycol n-propyl ether)
ρl	915.65	kg/m3	298.15	Liquid-liquid equilibria for the ternary system (water + hexadecane + dipropylene glycol n-propyl ether)
csound,fluid	[1234.06; 1306.26]	m/s	[288.15; 308.15]
csound,fluid	1306.26	m/s	288.15	Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1287.90	m/s	293.15	Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1269.88	m/s	298.15	Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1251.68	m/s	303.15	Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
csound,fluid	1234.06	m/s	308.15	Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[239.09; 540.39]	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			4.76340e+01
Coefficient B			7.78260e-01
Coefficient C			-2.80600e-04
Coefficient D			-4.90000e-09
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	239.09	J/mol×K	273.00	Calculated Property
Cp,gas	287.63	J/mol×K	353.78	Calculated Property
Cp,gas	332.44	J/mol×K	434.56	Calculated Property
Cp,gas	373.51	J/mol×K	515.33	Calculated Property
Cp,gas	410.81	J/mol×K	596.11	Calculated Property
Cp,gas	444.34	J/mol×K	676.89	Calculated Property
Cp,gas	474.08	J/mol×K	757.67	Calculated Property
Cp,gas	500.01	J/mol×K	838.44	Calculated Property
Cp,gas	522.12	J/mol×K	919.22	Calculated Property
Cp,gas	540.39	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0178003; 0.0001267]	Pa×s	[280.23; 494.61]	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			-1.54381e+01
Coefficient B			3.19729e+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.			280.23
Temperature range, max.			494.61
η	0.0178003	Pa×s	280.23	Calculated Property
η	0.0072817	Pa×s	304.05	Calculated Property
η	0.0033919	Pa×s	327.87	Calculated Property
η	0.0017522	Pa×s	351.69	Calculated Property
η	0.0009843	Pa×s	375.51	Calculated Property
η	0.0005923	Pa×s	399.33	Calculated Property
η	0.0003774	Pa×s	423.15	Calculated Property
η	0.0002523	Pa×s	446.97	Calculated Property
η	0.0001757	Pa×s	470.79	Calculated Property
η	0.0001267	Pa×s	494.61	Calculated Property

Similar Compounds

Find more compounds similar to 1-(1-methyl-2-propoxyethoxy)-2-propanol.

Mixtures

• Tetradecane + Water + 1-(1-methyl-2-propoxyethoxy)-2-propanol
• Hexadecane + Water + 1-(1-methyl-2-propoxyethoxy)-2-propanol
• Water + 1-(1-methyl-2-propoxyethoxy)-2-propanol
• 1-Butanamine + 1-(1-methyl-2-propoxyethoxy)-2-propanol
• 1-Butanamine, N-butyl- + 1-(1-methyl-2-propoxyethoxy)-2-propanol
• Tributylamine + 1-(1-methyl-2-propoxyethoxy)-2-propanol
• Dodecane + Water + 1-(1-methyl-2-propoxyethoxy)-2-propanol

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).
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
• Liquid-liquid equilibria for the ternary system (water + hexadecane + dipropylene glycol n-propyl ether)
• Liquid-liquid equilibria for the ternary system (water + tetradecane + 1-methyl-2-propoxyethoxy-2-propanol)
• Heat capacity of dowanols within a temperature range of (275.15 to 339.15) K. Measurements and prediction.
• Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems
• Liquid Liquid Equilibria for the Ternary System Water + Dodecane + 1-(1-Methyl-2-propoxyethoxy)-2-propanol
• Joback Method
• McGowan Method

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