Chemical Properties of 1-Methoxy-2-propyl acetate

InChI

InChI=1S/C6H12O3/c1-5(4-8-3)9-6(2)7/h5H,4H2,1-3H3

InChI Key

LLHKCFNBLRBOGN-UHFFFAOYSA-N

Formula

C6H12O3

SMILES

COCC(C)OC(C)=O

Molecular Weight¹

132.16

Other Names

• 1-Methoxy-2-propanol acetate
• 1-methoxy-2-acetoxypropane
• 2-(1-Methoxy)propyl acetate
• 2-Methoxy-1-methylethyl acetate
• 2-Propanol, 1-methoxy-, 2-acetate
• 2-acetoxy-1-methoxypropane
• 2-propanol, 1-methoxy-, acetate
• Acetic acid, 2-methoxy-1-methylethyl ester
• Arcosolv PMA
• Dowanol PMA
• Ektasolve PM Acetate
• NSC 2207
• PGMEA
• Propylene glycol 1-methyl ether 2-acetate
• Propylene glycol monomethyl ether acetate
• Propyleneglycol monomethyl ether acetate
• propylene glycol 1-monomethyl ether acetate

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4807		ChemSep v8.3 pure component data Compiled value
Tig	627.15	K	NCMS SOLV-DB
μ	1.80	debye	ChemSep v8.3 pure component data Compiled value
Tflash,cc	315.15	K	NCMS SOLV-DB
ΔfG°	-424.80	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-614.80	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	13.33	kJ/mol	Joback Calculated Property
ΔvapH°	51.18	kJ/mol	Relay (1.0) Calculated Property
IE	9.79	eV	Relay (1.0) Calculated Property
log10WS	-0.23		Relay (1.0) Calculated Property
logPoct/wat	0.430		NCMS SOLV-DB
McVol	108.710	ml/mol	McGowan Calculated Property
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	0		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[3009.00; 3010.00]	kPa
Pc	3009.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3010.00 ± 20.00	kPa	NIST
Ptriple	4.18e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[843.00; 914.00]
Inp	914.00		NIST
Inp	857.30		NIST
Inp	870.00		NIST
Inp	843.00		NIST
Ip	[1228.00; 1238.30]
Ip	1238.30		NIST
Ip	1228.00		NIST
Ip	1228.00		NIST
Tboil	[418.50; 419.15]	K
Tboil	419.00	K	Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
Tboil	418.65	K	Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
Tboil	418.65	K	ChemSep v8.3 pure component data Compiled value
Tboil	419.15	K	NCMS SOLV-DB
Tboil	418.50 ± 0.50	K	NIST
Tc	[597.60; 597.90]	K
Tc	597.60	K	ChemSep v8.3 pure component data Compiled value
Tc	597.90 ± 1.00	K	NIST
Tfus	[205.00; 218.15]	K
Tfus	205.00	K	ChemSep v8.3 pure component data Compiled value
Tfus	218.15	K	NCMS SOLV-DB
Ttriple	205.00	K	ChemSep v8.3 pure component data Compiled value
UQi	4.43		ChemSep v8.3 pure component data Compiled value
URi	5.07		ChemSep v8.3 pure component data Compiled value
Vc	0.409	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2550000		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	[0.0007770; 0.0011700]	Pa×s	[298.15; 318.15]
η	0.0010710	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Propylene Glycol Monomethyl Ether Acetate with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate between 298.15 K and 318.15 K
η	0.0011700	Pa×s	298.15	NCMS SOLV-DB
η	0.0009040	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Propylene Glycol Monomethyl Ether Acetate with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate between 298.15 K and 318.15 K
η	0.0007770	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of Propylene Glycol Monomethyl Ether Acetate with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate between 298.15 K and 318.15 K
Pvap	[0.49; 101.33]	kPa	[293.15; 418.65]
Pvap	0.49	kPa	293.15	NCMS SOLV-DB
Pvap	1.62	kPa	318.27	Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
Pvap	4.15	kPa	335.61	Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
Pvap	9.25	kPa	352.27	Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
Pvap	13.71	kPa	361.27	Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
Pvap	24.44	kPa	375.80	Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
Pvap	26.70	kPa	377.95	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	40.01	kPa	389.25	Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
Pvap	40.00	kPa	389.37	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	53.30	kPa	398.01	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	66.70	kPa	405.04	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	72.49	kPa	407.15	Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
Pvap	80.00	kPa	411.02	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	93.30	kPa	416.25	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	98.70	kPa	418.18	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	101.33	kPa	418.65	Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
n0	1.40000		298.15	NCMS SOLV-DB
ρl	[961.52; 989.20]	kg/m3	[273.15; 298.15]
ρl	989.20	kg/m3	273.15	Below the room temperature measurements of CO2 solubilities in six physical absorbents
ρl	978.20	kg/m3	283.15	Below the room temperature measurements of CO2 solubilities in six physical absorbents
ρl	961.52	kg/m3	298.15	Isobaric Vapor Liquid Equilibria for Two Binary Systems {Propylene Glycol Methyl Ether Acetate + Methanol} and {Propylene Glycol Methyl Ether Acetate + N,N-Dimethylformamide} at p = 30.0, 50.0, and 70.0 kPa
γ	0.03	N/m	298.15	NCMS SOLV-DB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[148.79; 409.76]	J/mol×K	[255.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			8.50000e+01
Coefficient B			-5.00000e+02
Coefficient C			6.11640e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			255.00
Temperature range, max.			1500.00
Cp,gas	148.79	J/mol×K	255.00	Calculated Property
Cp,gas	212.13	J/mol×K	393.33	Calculated Property
Cp,gas	261.97	J/mol×K	531.67	Calculated Property
Cp,gas	299.89	J/mol×K	670.00	Calculated Property
Cp,gas	329.17	J/mol×K	808.33	Calculated Property
Cp,gas	352.26	J/mol×K	946.67	Calculated Property
Cp,gas	370.88	J/mol×K	1085.00	Calculated Property
Cp,gas	386.17	J/mol×K	1223.33	Calculated Property
Cp,gas	398.94	J/mol×K	1361.67	Calculated Property
Cp,gas	409.76	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[231.52; 329.54]	J/mol×K	[298.95; 448.42]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.01070e+02
Coefficient B			2.90070e-01
Coefficient C			4.89360e-04
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidHeatCapacityCp
Temperature range, min.			298.95
Temperature range, max.			448.42
Cp,liquid	231.52	J/mol×K	298.95	Calculated Property
Cp,liquid	241.33	J/mol×K	315.56	Calculated Property
Cp,liquid	251.41	J/mol×K	332.17	Calculated Property
Cp,liquid	261.77	J/mol×K	348.77	Calculated Property
Cp,liquid	272.39	J/mol×K	365.38	Calculated Property
Cp,liquid	283.28	J/mol×K	381.99	Calculated Property
Cp,liquid	294.44	J/mol×K	398.60	Calculated Property
Cp,liquid	305.87	J/mol×K	415.20	Calculated Property
Cp,liquid	317.57	J/mol×K	431.81	Calculated Property
Cp,liquid	329.54	J/mol×K	448.42	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0139071; 0.0002063]	Pa×s	[205.00; 418.65]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.24520e+01
Coefficient B			1.68830e+03
Coefficient C			-1.10780e-02
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			205.00
Temperature range, max.			418.65
η	0.0139071	Pa×s	205.00	Calculated Property
η	0.0059090	Pa×s	228.74	Calculated Property
η	0.0029488	Pa×s	252.48	Calculated Property
η	0.0016582	Pa×s	276.22	Calculated Property
η	0.0010213	Pa×s	299.96	Calculated Property
η	0.0006753	Pa×s	323.69	Calculated Property
η	0.0004725	Pa×s	347.43	Calculated Property
η	0.0003460	Pa×s	371.17	Calculated Property
η	0.0002631	Pa×s	394.91	Calculated Property
η	0.0002063	Pa×s	418.65	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[53.76; 0.00]	kJ/mol	[205.00; 597.60]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			6.32290e+01
Coefficient B			3.86090e-01
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			5.97600e+02
Comment			ChemSep eq 106, HeatOfVaporization, ChemSep Tmax 597.9 K
Temperature range, min.			205.00
Temperature range, max.			597.60
ΔvapH	53.76	kJ/mol	205.00	Calculated Property
ΔvapH	51.37	kJ/mol	248.62	Calculated Property
ΔvapH	48.79	kJ/mol	292.24	Calculated Property
ΔvapH	45.97	kJ/mol	335.87	Calculated Property
ΔvapH	42.85	kJ/mol	379.49	Calculated Property
ΔvapH	39.31	kJ/mol	423.11	Calculated Property
ΔvapH	35.18	kJ/mol	466.73	Calculated Property
ΔvapH	30.08	kJ/mol	510.36	Calculated Property
ΔvapH	23.02	kJ/mol	553.98	Calculated Property
ΔvapH	0.00	kJ/mol	597.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[4.18e-05; 3072.49]	kPa	[205.00; 597.90]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			8.18192e+01
Coefficient B			-8.40960e+03
Coefficient C			-9.59430e+00
Coefficient D			4.52230e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			205.00
Temperature range, max.			597.90
Pvap	4.18e-05	kPa	205.00	Calculated Property
Pvap	9.62e-03	kPa	248.66	Calculated Property
Pvap	0.35	kPa	292.31	Calculated Property
Pvap	4.43	kPa	335.97	Calculated Property
Pvap	28.11	kPa	379.62	Calculated Property
Pvap	113.87	kPa	423.28	Calculated Property
Pvap	339.20	kPa	466.93	Calculated Property
Pvap	813.98	kPa	510.59	Calculated Property
Pvap	1672.95	kPa	554.24	Calculated Property
Pvap	3072.49	kPa	597.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1055.52; 313.92]	kg/m3	[205.00; 597.90]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			7.99939e+01
Coefficient B			2.54820e-01
Coefficient C			5.97900e+02
Coefficient D			2.85710e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			205.00
Temperature range, max.			597.90
ρl	1055.52	kg/m3	205.00	Calculated Property
ρl	1014.01	kg/m3	248.66	Calculated Property
ρl	970.46	kg/m3	292.31	Calculated Property
ρl	924.40	kg/m3	335.97	Calculated Property
ρl	875.09	kg/m3	379.62	Calculated Property
ρl	821.40	kg/m3	423.28	Calculated Property
ρl	761.36	kg/m3	466.93	Calculated Property
ρl	691.04	kg/m3	510.59	Calculated Property
ρl	599.70	kg/m3	554.24	Calculated Property
ρl	313.92	kg/m3	597.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.00]	N/m	[205.00; 597.60]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K
Coefficient A			6.42660e-02
Coefficient B			1.27200e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			5.97600e+02
Comment			ChemSep eq 106, SurfaceTension, ChemSep Tmax 597.9 K
Temperature range, min.			205.00
Temperature range, max.			597.60
γ	0.04	N/m	205.00	Calculated Property
γ	0.03	N/m	248.62	Calculated Property
γ	0.03	N/m	292.24	Calculated Property
γ	0.02	N/m	335.87	Calculated Property
γ	0.02	N/m	379.49	Calculated Property
γ	0.01	N/m	423.11	Calculated Property
γ	0.01	N/m	466.73	Calculated Property
γ	0.01	N/m	510.36	Calculated Property
γ	0.00	N/m	553.98	Calculated Property
γ	0.00	N/m	597.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.07]	W/m×K	[418.65; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			2.10770e-04
Coefficient B			9.08340e-01
Coefficient C			6.70620e+02
Coefficient D			0.00000e+00
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			418.65
Temperature range, max.			1000.00
λgas	0.02	W/m×K	418.65	Calculated Property
λgas	0.02	W/m×K	483.24	Calculated Property
λgas	0.03	W/m×K	547.84	Calculated Property
λgas	0.03	W/m×K	612.43	Calculated Property
λgas	0.04	W/m×K	677.03	Calculated Property
λgas	0.04	W/m×K	741.62	Calculated Property
λgas	0.05	W/m×K	806.22	Calculated Property
λgas	0.06	W/m×K	870.81	Calculated Property
λgas	0.06	W/m×K	935.41	Calculated Property
λgas	0.07	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.10]	W/m×K	[205.00; 418.65]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K
Coefficient A			1.96900e-01
Coefficient B			-2.33400e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			ChemSep eq 100, LiquidThermalConductivity
Temperature range, min.			205.00
Temperature range, max.			418.65
λliquid	0.15	W/m×K	205.00	Calculated Property
λliquid	0.14	W/m×K	228.74	Calculated Property
λliquid	0.14	W/m×K	252.48	Calculated Property
λliquid	0.13	W/m×K	276.22	Calculated Property
λliquid	0.13	W/m×K	299.96	Calculated Property
λliquid	0.12	W/m×K	323.69	Calculated Property
λliquid	0.12	W/m×K	347.43	Calculated Property
λliquid	0.11	W/m×K	371.17	Calculated Property
λliquid	0.10	W/m×K	394.91	Calculated Property
λliquid	0.10	W/m×K	418.65	Calculated Property

Similar Compounds

Find more compounds similar to 1-Methoxy-2-propyl acetate.

Mixtures

• 1-Methoxy-2-propyl acetate + Water
• 1-Methoxy-2-propyl acetate + 2-Propanol, 1-methoxy-
• 1-Methoxy-2-propyl acetate + Methyl Alcohol
• Carbon dioxide + 1-Methoxy-2-propyl acetate
• Formamide, N,N-dimethyl- + 1-Methoxy-2-propyl acetate
• 1-Methoxy-2-propyl acetate + Sulfuryl fluoride
• Benzyl methacrylate + 1-Methoxy-2-propyl acetate
• 1-Methoxy-2-propyl acetate + 2-Propenoic acid, 2-methyl-

Sources

• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
• Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
• Solubilities of carbon dioxide in 2-methoxyethyl acetate, 1-methoxy-2-propyl acetate and 3-methoxybutyl acetate
• Below the room temperature measurements of CO2 solubilities in six physical absorbents
• Isobaric Vapor Liquid Equilibria for Two Binary Systems {Propylene Glycol Methyl Ether Acetate + Methanol} and {Propylene Glycol Methyl Ether Acetate + N,N-Dimethylformamide} at p = 30.0, 50.0, and 70.0 kPa
• Solubilities of Sulfuryl Fluoride in 2-Butoxyethyl Acetate, 3-Methoxybutyl Acetate, 2-Methoxyethyl Acetate, 1-Methoxy-2-propyl Acetate, and 2-(2-Ethoxyethoxy)ethyl Acetate
• Densities and Viscosities of Binary Mixtures of Propylene Glycol Monomethyl Ether Acetate with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate between 298.15 K and 318.15 K
• Solubilities of Three Phosphorus Flame Retardants in Selected Organic Solvents
• Joback Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB

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