Chemical Properties of 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol

InChI

InChI=1S/C9H20O4/c1-7(11)5-12-9(3)6-13-8(2)4-10/h7-11H,4-6H2,1-3H3

InChI Key

LCZVSXRMYJUNFX-UHFFFAOYSA-N

Formula

C9H20O4

SMILES

CC(O)COC(C)COC(C)CO

Molecular Weight¹

192.26

Other Names

• 2-(2-(2-hydroxypropoxy)propoxy)propan-1-ol
• tripropylene glycol

• C_p,gas : Ideal gas heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• 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).
• 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).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_liquid : Liquid thermal conductivity (W/m×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

Cheméo can also estimate 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
Pvap	[0.02; 0.91]	kPa	[340.15; 405.15]
Pvap	0.02	kPa	340.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.04	kPa	350.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap	0.04	kPa	350.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.06	kPa	355.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.06	kPa	357.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap	0.08	kPa	360.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.10	kPa	364.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap	0.14	kPa	370.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.15	kPa	371.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap	0.19	kPa	375.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.21	kPa	377.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.22	kPa	378.15	Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap	0.25	kPa	380.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.33	kPa	385.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.43	kPa	390.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.56	kPa	395.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.71	kPa	400.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
Pvap	0.91	kPa	405.15	Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
ρl	[976.90; 1017.50]	kg/m3	[293.15; 343.15]
ρl	1017.50	kg/m3	293.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	1009.50	kg/m3	303.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	1001.50	kg/m3	313.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	993.40	kg/m3	323.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	985.20	kg/m3	333.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
ρl	976.90	kg/m3	343.15	Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
λliquid	[0.14; 0.15]	W/m×K	[298.10; 449.60]
λliquid	0.15	W/m×K	298.10	Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λliquid	0.15	W/m×K	326.10	Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λliquid	0.15	W/m×K	351.10	Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λliquid	0.15	W/m×K	376.20	Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λliquid	0.14	W/m×K	399.40	Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λliquid	0.14	W/m×K	424.90	Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
λliquid	0.14	W/m×K	449.60	Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[251.27; 559.60]	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			5.12430e+01
Coefficient B			8.18160e-01
Coefficient C			-3.14200e-04
Coefficient D			4.40000e-09
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	251.27	J/mol×K	273.00	Calculated Property
Cp,gas	301.56	J/mol×K	353.78	Calculated Property
Cp,gas	347.81	J/mol×K	434.56	Calculated Property
Cp,gas	390.03	J/mol×K	515.33	Calculated Property
Cp,gas	428.24	J/mol×K	596.11	Calculated Property
Cp,gas	462.45	J/mol×K	676.89	Calculated Property
Cp,gas	492.68	J/mol×K	757.67	Calculated Property
Cp,gas	518.94	J/mol×K	838.44	Calculated Property
Cp,gas	541.24	J/mol×K	919.22	Calculated Property
Cp,gas	559.60	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0425755; 0.0000389]	Pa×s	[312.29; 558.73]	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			-1.90222e+01
Coefficient B			4.95470e+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.			312.29
Temperature range, max.			558.73
η	0.0425755	Pa×s	312.29	Calculated Property
η	0.0118495	Pa×s	339.67	Calculated Property
η	0.0039913	Pa×s	367.05	Calculated Property
η	0.0015637	Pa×s	394.44	Calculated Property
η	0.0006919	Pa×s	421.82	Calculated Property
η	0.0003381	Pa×s	449.20	Calculated Property
η	0.0001794	Pa×s	476.58	Calculated Property
η	0.0001020	Pa×s	503.97	Calculated Property
η	0.0000614	Pa×s	531.35	Calculated Property
η	0.0000389	Pa×s	558.73	Calculated Property

Similar Compounds

Find more compounds similar to 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol.

Mixtures

• Magnesium chloride + Water + 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol
• Water + 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol
• Toluene + 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol
• Benzene, ethyl- + 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol
• o-Xylene + 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol
• Benzene, 1,3-dimethyl- + 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol
• p-Xylene + 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol
• Tromethamine + Water + 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
• Molar heat capacities of some aqueous 2-amino-2-hydroxymethyl-1,3-propanediol + glycol systems
• Thermophysical characterization of aqueous ternary system containing n-tris-[hydroxymethyl]methyl-3-amino propanesulfonic acid and glycol (PG or DPG or TPG)
• Density and vapour pressure of mixed-solvent desiccant systems (propylene glycol or dipropylene glycol or tripropylene glycol + magnesium chloride + water)
• Heat Capacity of Several Mixed-Solvent Desiccants Containing Glycol + Water + MgCl2
• Molar heat capacity of several aqueous solutions of n-[tris(hydroxymethyl)methyl-3-amino]- propanesulfonic acid (TAPS) + glycol
• Density, Viscosity and Thermal Conductivity of Aqueous Solutions of Propylene Glycol, Dipropylene Glycol, and Tripropylene Glycol between 290 K and 460 K
• Vapor Liquid Equilibria for Water + Propylene Glycols Binary Systems: Experimental Data and Regression
• Joback Method
• McGowan Method

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