2,3-Dimethoxypropan-1-ol

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Physical Properties

Property	Value	Unit	Source
Δ_fH°_gas	-547.25	kJ/mol	Relay (1.0) Calculated Property
Δ_fusH°	11.65	kJ/mol	Joback Calculated Property
Δ_vapH°	64.40	kJ/mol	Relay (1.0) Calculated Property
IE	9.83	eV	Relay (1.0) Calculated Property
logP_oct/wat	-0.360		Crippen Calculated Property
McVol	98.920	ml/mol	McGowan Calculated Property
P_c	3754.57	kPa	Joback Calculated Property
I_np	[903.80; 903.80]
I_np	903.80		NIST
I_np	903.80		NIST
T_boil	459.64	K	Relay (1.0) Calculated Property
T_c	642.21	K	Relay (1.0) Calculated Property
T_fus	235.50	K	Relay (1.0) Calculated Property

Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation, Acentric Factor, 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
P_vap	[3.20; 100.79]	kPa	[337.95; 446.65]

P_vap	3.20	kPa	337.95	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	7.84	kPa	368.95	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	19.27	kPa	398.10	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	27.33	kPa	408.55	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	32.46	kPa	413.05	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	38.80	kPa	419.70	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	45.86	kPa	423.55	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	59.80	kPa	431.55	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	65.60	kPa	433.15	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	70.66	kPa	434.85	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	76.53	kPa	437.35	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	83.33	kPa	439.75	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	87.26	kPa	441.65	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	95.73	kPa	444.45	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa
P_vap	100.79	kPa	446.65	Isobaric Vapor Liquid Equilibria for the Binary and Ternary Systems of Methanol, Epichlorohydrin, and Glycerol Dimethyl Ether at 101.3 kPa

Correlations

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[154.55; 333.49]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is C_p,gas in J/mol×K, T in K
Coefficient A			5.29520e+01
Coefficient B			3.92340e-01
Coefficient C			-5.98000e-05
Coefficient D			-5.20000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00

C_p,gas	154.55	J/mol×K	273.00	Calculated Property
C_p,gas	181.97	J/mol×K	353.78	Calculated Property
C_p,gas	207.89	J/mol×K	434.56	Calculated Property
C_p,gas	232.14	J/mol×K	515.33	Calculated Property
C_p,gas	254.57	J/mol×K	596.11	Calculated Property
C_p,gas	275.00	J/mol×K	676.89	Calculated Property
C_p,gas	293.27	J/mol×K	757.67	Calculated Property
C_p,gas	309.22	J/mol×K	838.44	Calculated Property
C_p,gas	322.68	J/mol×K	919.22	Calculated Property
C_p,gas	333.49	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0441979; 0.0002163]	Pa×s	[236.39; 431.29]	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			-1.48913e+01
Coefficient B			2.78283e+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.			236.39
Temperature range, max.			431.29

η	0.0441979	Pa×s	236.39	Calculated Property
η	0.0164568	Pa×s	258.05	Calculated Property
η	0.0071405	Pa×s	279.70	Calculated Property
η	0.0034932	Pa×s	301.36	Calculated Property
η	0.0018809	Pa×s	323.01	Calculated Property
η	0.0010946	Pa×s	344.67	Calculated Property
η	0.0006792	Pa×s	366.32	Calculated Property
η	0.0004445	Pa×s	387.98	Calculated Property
η	0.0003042	Pa×s	409.63	Calculated Property
η	0.0002163	Pa×s	431.29	Calculated Property

Similar Compounds

2-[2-(2-hydroxypropoxy)propoxy]-1-propanol.

2-Propanol, 1-(2-methoxy-1-methylethoxy)-.

2-Propanol, 1-[2-(2-methoxy-1-methylethoxy)-1-methylethoxy]-.

Find more compounds similar to 2,3-Dimethoxypropan-1-ol.

Mixtures

Sources

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