Chemical Properties of 2-Propanol, 1-methoxy- (CAS 107-98-2)

InChI

InChI=1S/C4H10O2/c1-4(5)3-6-2/h4-5H,3H2,1-2H3

InChI Key

ARXJGSRGQADJSQ-UHFFFAOYSA-N

Formula

C4H10O2

SMILES

COCC(C)O

Molecular Weight¹

90.12

CAS

107-98-2

Other Names

• 1-Methoxy-2-hydroxypropane
• 1-Methoxypropan-2-ol
• 1-methoxy-2-propanol
• 2-Methoxy-1-methylethanol
• Closol
• Dowanol-33B
• Dowtherm 209
• Glycol ether pm
• Icinol PM
• Methoxyisopropanol
• Methoxypropanol, «alpha» isomer
• NSC 2409
• PGME
• Poly-solv MPM
• Poly-solve MPM
• Propan-1-methoxy-2-ol
• Propan-2-ol, 1-methoxy-
• Propasol solvent M
• Propylene glycol 1-methyl ether
• Solvent PM
• Ucar solvent lm
• propylene glycol monomethyl ether
• «alpha»-Propylene glycol monomethyl ether

• 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).
• 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.
• c_sound,fluid : Speed of sound in fluid (m/s).
• 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	[0.4427; 0.4480]
ω	0.4480		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4427		ChemSep v8.3 pure component data Compiled value
Tig	551.15	K	NCMS SOLV-DB
μ	2.40	debye	ChemSep v8.3 pure component data Compiled value
Tflash,cc	305.15	K	NCMS SOLV-DB
ΔfG°	-247.40	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-397.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	3.61	kJ/mol	Solid-Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
ΔvapH°	[46.20; 46.40]	kJ/mol
ΔvapH°	46.20	kJ/mol	NIST
ΔvapH°	46.40	kJ/mol	NIST
IE	9.93	eV	Relay (1.0) Calculated Property
logPoct/wat	-0.490		NCMS SOLV-DB
McVol	78.960	ml/mol	McGowan Calculated Property
NFPA Fire	3		NCMS SOLV-DB
NFPA Health	0		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[4110.00; 4113.00]	kPa
Pc	4110.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc	4113.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4113.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4113.00 ± 10.00	kPa	NIST
Ptriple	3.21e-06	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[634.00; 673.40]
Inp	636.00		NIST
Inp	634.00		NIST
Inp	673.20		NIST
Inp	673.40		NIST
Inp	669.00		NIST
Inp	658.00		NIST
Inp	672.00		NIST
Inp	649.00		NIST
Inp	673.00		NIST
Inp	673.00		NIST
Inp	673.20		NIST
Inp	669.00		NIST
Inp	636.00		NIST
Ip	[1108.00; 1160.00]
Ip	1131.00		NIST
Ip	1160.00		NIST
Ip	1146.90		NIST
Ip	1131.00		NIST
Ip	1108.00		NIST
Ip	1135.00		NIST
Ip	1160.00		NIST
Tboil	[391.15; 394.15]	K
Tboil	393.30	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	393.15	K	Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa
Tboil	393.25	K	ChemSep v8.3 pure component data Compiled value
Tboil	391.15	K	NCMS SOLV-DB
Tboil	391.70	K	NIST
Tboil	394.15	K	NIST
Tc	[579.80; 579.80]	K
Tc	579.80	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc	579.80	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	579.80	K	ChemSep v8.3 pure component data Compiled value
Tc	579.80 ± 0.30	K	NIST
Tfus	[131.15; 176.48]	K
Tfus	176.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	176.48	K	ChemSep v8.3 pure component data Compiled value
Tfus	131.15	K	NCMS SOLV-DB
Ttriple	176.48	K	ChemSep v8.3 pure component data Compiled value
UQi	3.90		ChemSep v8.3 pure component data Compiled value
URi	4.17		ChemSep v8.3 pure component data Compiled value
Vc	[0.280; 0.284]	m3/kmol
Vc	0.280	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.284	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2420000		ChemSep v8.3 pure component data Compiled value

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
η	[0.0010690; 0.0019000]	Pa×s	[298.15; 318.15]
η	0.0017070	Pa×s	298.15	Excess Molar Volumes and Viscosities for Binary Mixtures of Propylene Glycol Monomethyl Ether with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
η	0.0019000	Pa×s	298.15	NCMS SOLV-DB
η	0.0013060	Pa×s	308.15	Excess Molar Volumes and Viscosities for Binary Mixtures of Propylene Glycol Monomethyl Ether with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
η	0.0010690	Pa×s	318.15	Excess Molar Volumes and Viscosities for Binary Mixtures of Propylene Glycol Monomethyl Ether with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
Pvap	[1.67; 739.81]	kPa	[298.15; 473.15]
Pvap	1.67	kPa	298.15	NCMS SOLV-DB
Pvap	3.61	kPa	313.15	Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
Pvap	9.25	kPa	331.47	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	10.01	kPa	333.15	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	13.11	kPa	339.12	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	15.00	kPa	342.30	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	15.79	kPa	343.15	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	19.25	kPa	347.62	Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
Pvap	19.25	kPa	347.71	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	22.64	kPa	351.56	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	23.50	kPa	352.50	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	23.74	kPa	352.64	Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
Pvap	24.25	kPa	353.15	Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
Pvap	24.18	kPa	353.15	Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
Pvap	24.17	kPa	353.15	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	26.69	kPa	355.59	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	26.70	kPa	355.83	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	29.35	kPa	357.89	Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
Pvap	29.57	kPa	358.15	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	32.00	kPa	360.10	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	32.79	kPa	360.78	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	35.72	kPa	362.93	Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
Pvap	35.74	kPa	363.01	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	36.03	kPa	363.15	Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
Pvap	40.00	kPa	365.99	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	42.10	kPa	367.40	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	43.29	kPa	368.03	Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
Pvap	43.48	kPa	368.23	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	49.10	kPa	371.60	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	48.55	kPa	373.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	48.26	kPa	373.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	50.45	kPa	373.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	52.16	kPa	373.15	Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
Pvap	52.30	kPa	373.22	Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
Pvap	52.31	kPa	373.31	Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
Pvap	53.30	kPa	373.87	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	57.60	kPa	376.00	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	61.89	kPa	378.01	Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
Pvap	66.10	kPa	380.00	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	66.70	kPa	380.27	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	74.60	kPa	383.50	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	80.00	kPa	385.71	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	83.30	kPa	386.90	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	92.60	kPa	390.10	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	93.30	kPa	390.45	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	392.20	Isobaric vapor liquid equilibria for water + propylene glycol monomethyl ether (PGME), water + propyleneglycol monomethyl ether acetate (PGMEA), and PGME+PGMEA at reduced pressures
Pvap	99.90	kPa	392.80	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	101.30	kPa	393.15	Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa
Pvap	116.90	kPa	397.90	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	125.50	kPa	400.00	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	134.00	kPa	402.20	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	142.50	kPa	404.30	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	151.00	kPa	406.30	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	159.50	kPa	408.20	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	168.00	kPa	410.00	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	176.50	kPa	411.80	Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
Pvap	232.93	kPa	423.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	230.60	kPa	423.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	232.13	kPa	423.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	231.95	kPa	423.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
Pvap	739.81	kPa	473.15	Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
n0	[1.40100; 1.40200]		[298.15; 298.15]
n0	1.40100		298.15	Density, Speed of Sound, and Refractive Index of Aqueous Binary Mixtures of Some Glycol Ethers at T = 298.15 K
n0	1.40200		298.15	NCMS SOLV-DB
csound,fluid	[104.80; 1298.14]	m/s	[288.15; 577.92]
csound,fluid	1298.14	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	1280.08	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	1261.54	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	1243.03	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	1224.50	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
csound,fluid	828.20	m/s	412.24	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	744.50	m/s	434.19	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	670.70	m/s	453.43	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	572.30	m/s	479.45	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	486.90	m/s	500.92	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	384.10	m/s	524.99	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	304.10	m/s	542.86	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	260.70	m/s	553.70	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	231.80	m/s	558.23	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	204.20	m/s	563.74	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	158.10	m/s	570.21	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	138.70	m/s	573.29	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
csound,fluid	104.80	m/s	577.92	Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
γ	0.03	N/m	298.15	NCMS SOLV-DB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[112.20; 307.42]	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			8.04569e+01
Coefficient B			-6.04321e+02
Coefficient C			5.82767e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			255.00
Temperature range, max.			1500.00
Cp,gas	112.20	J/mol×K	255.00	Calculated Property
Cp,gas	153.52	J/mol×K	393.33	Calculated Property
Cp,gas	189.42	J/mol×K	531.67	Calculated Property
Cp,gas	218.24	J/mol×K	670.00	Calculated Property
Cp,gas	241.24	J/mol×K	808.33	Calculated Property
Cp,gas	259.80	J/mol×K	946.67	Calculated Property
Cp,gas	275.01	J/mol×K	1085.00	Calculated Property
Cp,gas	287.66	J/mol×K	1223.33	Calculated Property
Cp,gas	298.32	J/mol×K	1361.67	Calculated Property
Cp,gas	307.42	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[161.56; 330.84]	J/mol×K	[176.48; 393.25]	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			2.44100e+02
Coefficient B			-1.02800e+00
Coefficient C			3.17500e-03
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			176.48
Temperature range, max.			393.25
Cp,liquid	161.56	J/mol×K	176.48	Calculated Property
Cp,liquid	165.64	J/mol×K	200.57	Calculated Property
Cp,liquid	173.39	J/mol×K	224.65	Calculated Property
Cp,liquid	184.84	J/mol×K	248.74	Calculated Property
Cp,liquid	199.96	J/mol×K	272.82	Calculated Property
Cp,liquid	218.77	J/mol×K	296.91	Calculated Property
Cp,liquid	241.26	J/mol×K	320.99	Calculated Property
Cp,liquid	267.44	J/mol×K	345.08	Calculated Property
Cp,liquid	297.30	J/mol×K	369.16	Calculated Property
Cp,liquid	330.84	J/mol×K	393.25	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.2057771; 0.0003104]	Pa×s	[176.48; 393.25]	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			-1.33670e+01
Coefficient B			2.08000e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			176.48
Temperature range, max.			393.25
η	0.2057771	Pa×s	176.48	Calculated Property
η	0.0499703	Pa×s	200.57	Calculated Property
η	0.0164374	Pa×s	224.65	Calculated Property
η	0.0067061	Pa×s	248.74	Calculated Property
η	0.0032052	Pa×s	272.82	Calculated Property
η	0.0017268	Pa×s	296.91	Calculated Property
η	0.0010209	Pa×s	320.99	Calculated Property
η	0.0006494	Pa×s	345.08	Calculated Property
η	0.0004383	Pa×s	369.16	Calculated Property
η	0.0003104	Pa×s	393.25	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[49.28; 0.00]	kJ/mol	[176.48; 579.80]	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			6.04800e+01
Coefficient B			9.01000e-01
Coefficient C			-1.39000e+00
Coefficient D			9.33000e-01
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			5.79800e+02
Temperature range, min.			176.48
Temperature range, max.			579.80
ΔvapH	49.28	kJ/mol	176.48	Calculated Property
ΔvapH	47.41	kJ/mol	221.29	Calculated Property
ΔvapH	45.60	kJ/mol	266.11	Calculated Property
ΔvapH	43.67	kJ/mol	310.92	Calculated Property
ΔvapH	41.37	kJ/mol	355.73	Calculated Property
ΔvapH	38.44	kJ/mol	400.55	Calculated Property
ΔvapH	34.51	kJ/mol	445.36	Calculated Property
ΔvapH	29.05	kJ/mol	490.17	Calculated Property
ΔvapH	21.02	kJ/mol	534.99	Calculated Property
ΔvapH	0.00	kJ/mol	579.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[3.22e-06; 4112.37]	kPa	[176.48; 579.80]	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			5.19062e+01
Coefficient B			-6.81200e+03
Coefficient C			-5.01700e+00
Coefficient D			2.26300e-18
Coefficient E			6.00000e+00
Temperature range, min.			176.48
Temperature range, max.			579.80
Pvap	3.22e-06	kPa	176.48	Calculated Property
Pvap	2.57e-03	kPa	221.29	Calculated Property
Pvap	0.18	kPa	266.11	Calculated Property
Pvap	3.33	kPa	310.92	Calculated Property
Pvap	26.87	kPa	355.73	Calculated Property
Pvap	126.82	kPa	400.55	Calculated Property
Pvap	415.85	kPa	445.36	Calculated Property
Pvap	1055.11	kPa	490.17	Calculated Property
Pvap	2226.68	kPa	534.99	Calculated Property
Pvap	4112.37	kPa	579.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1028.19; 316.92]	kg/m3	[176.48; 579.80]	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			8.58853e+01
Coefficient B			2.71000e-01
Coefficient C			5.79800e+02
Coefficient D			2.86000e-01
Temperature range, min.			176.48
Temperature range, max.			579.80
ρl	1028.19	kg/m3	176.48	Calculated Property
ρl	988.87	kg/m3	221.29	Calculated Property
ρl	947.60	kg/m3	266.11	Calculated Property
ρl	903.87	kg/m3	310.92	Calculated Property
ρl	857.00	kg/m3	355.73	Calculated Property
ρl	805.88	kg/m3	400.55	Calculated Property
ρl	748.61	kg/m3	445.36	Calculated Property
ρl	681.37	kg/m3	490.17	Calculated Property
ρl	593.75	kg/m3	534.99	Calculated Property
ρl	316.92	kg/m3	579.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.00]	N/m	[176.48; 579.80]	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			6.74000e-02
Coefficient B			1.22030e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			5.79800e+02
Temperature range, min.			176.48
Temperature range, max.			579.80
γ	0.04	N/m	176.48	Calculated Property
γ	0.04	N/m	221.29	Calculated Property
γ	0.03	N/m	266.11	Calculated Property
γ	0.03	N/m	310.92	Calculated Property
γ	0.02	N/m	355.73	Calculated Property
γ	0.02	N/m	400.55	Calculated Property
γ	0.01	N/m	445.36	Calculated Property
γ	0.01	N/m	490.17	Calculated Property
γ	0.00	N/m	534.99	Calculated Property
γ	0.00	N/m	579.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.13]	W/m×K	[393.25; 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			1.09600e+02
Coefficient B			1.00940e+00
Coefficient C			8.77040e+08
Coefficient D			0.00000e+00
Temperature range, min.			393.25
Temperature range, max.			1000.00
λgas	0.02	W/m×K	393.25	Calculated Property
λgas	0.03	W/m×K	460.67	Calculated Property
λgas	0.04	W/m×K	528.08	Calculated Property
λgas	0.05	W/m×K	595.50	Calculated Property
λgas	0.06	W/m×K	662.92	Calculated Property
λgas	0.07	W/m×K	730.33	Calculated Property
λgas	0.08	W/m×K	797.75	Calculated Property
λgas	0.10	W/m×K	865.17	Calculated Property
λgas	0.12	W/m×K	932.58	Calculated Property
λgas	0.13	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.21; 0.14]	W/m×K	[176.48; 393.25]	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			2.63000e-01
Coefficient B			-3.18800e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			176.48
Temperature range, max.			393.25
λliquid	0.21	W/m×K	176.48	Calculated Property
λliquid	0.20	W/m×K	200.57	Calculated Property
λliquid	0.19	W/m×K	224.65	Calculated Property
λliquid	0.18	W/m×K	248.74	Calculated Property
λliquid	0.18	W/m×K	272.82	Calculated Property
λliquid	0.17	W/m×K	296.91	Calculated Property
λliquid	0.16	W/m×K	320.99	Calculated Property
λliquid	0.15	W/m×K	345.08	Calculated Property
λliquid	0.15	W/m×K	369.16	Calculated Property
λliquid	0.14	W/m×K	393.25	Calculated Property

Similar Compounds

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

Mixtures

• 2-Propanol, 1-methoxy- + Water
• 1-Methoxy-2-propyl acetate + 2-Propanol, 1-methoxy-
• Acetic acid, methyl ester + 2-Propanol, 1-methoxy-
• Ethanol, 2-methoxy- + 2-Propanol, 1-methoxy-
• Dimethyl Sulfoxide + Sulfur dioxide + 2-Propanol, 1-methoxy-
• Sulfur dioxide + 2-Propanol, 1-methoxy-
• 1-Pentanamine + 2-Propanol, 1-methoxy-
• Monoethanolamine + 2-Propanol, 1-methoxy-
• Ethyl Acetate + 2-Propanol, 1-methoxy-
• Furfural + 2-Propanol, 1-methoxy-
• Acetic acid, butyl ester + 2-Propanol, 1-methoxy-
• Ethane, nitro- + 2-Propanol, 1-methoxy-
• 2-Propenoic acid, 2-methyl- + 2-Propanol, 1-methoxy-
• Benzyl methacrylate + 2-Propanol, 1-methoxy-
• Benzenamine, 4-chloro-2,5-dimethoxy- + 2-Propanol, 1-methoxy-
• 2-Propanol, 1-methoxy- + 2,5-dimethoxyaniline
• 1-Propanol, 2-methoxy- + 2-Propanol, 1-methoxy-
• Toluene + 2-Propanol, 1-methoxy-
• 2-Propanol, 1-methoxy- + Cyclohexane
• Benzene + 2-Propanol, 1-methoxy-

Find more mixtures with 2-Propanol, 1-methoxy-.

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)
• 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
• Supplementary vapor pressure data of the glycol ethers, 1-methoxy-2-propanol, and 2-methoxyethanol at a pressure range of (15 to 177) kPa
• Isobaric (vapor + liquid) equilibria for the binary systems (1-methoxy-2- propanol + 2-methoxyethanol), (2-butanone + 2-methoxyethanol) and (water + 2-methoxyethanol) at pressures of (74.5, 101.3, and 134.0) kPa
• Solubility Properties and Absorption Mechanism Investigation of Dilute SO2 in Propylene Glycol Monomethyl Ether + Dimethyl Sulfoxide System
• Isobaric Vapor Liquid Equilibria for (Water + 1-Methoxy-2-propanol), (Water + 2-Methoxy-1-propanol), and (1-Methoxy-2-propanol + 2-Methoxy-1-propanol) at 101.3 kPa
• Speed of Sound Measurement in 1-Methoxy-2-propanol from (306.81 to 648.29) K and up to 10 MPa
• Solubility of 4-Chloro-2,5-dimethoxynitrobenzene, 4-Chloro-2,5-dimethoxyaniline, and 2,5-Dimethoxyaniline in Binary and Pure Solvents: Determination and Modeling
• Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
• Vapor-Liquid Equilibrium for Propylene Glycol + 2-(2-Hexyloxyethoxy)ethanol and 1-Methyl-2-pyrrolidone + 1-Methoxypropan-2-ol
• Vapor-Liquid Equilibria on Four Binary Systems: 2-Phenylpropionaldehyde + Phenol, Propylene Glycol Monomethyl Ether + Nitroethane, Dimethyl Ether + Propylene, and N-Butyric Acid + Propionic Acid
• Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
• Solid-Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
• Excess Molar Volumes and Viscosities for Binary Mixtures of Propylene Glycol Monomethyl Ether with Methacrylic Acid, Benzyl Methacrylate, and 2-Hydroxyethyl Methacrylate at (298.15, 308.15, and 318.15) K
• 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
• Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
• Solubilities of Three Phosphorus Flame Retardants in Selected Organic Solvents
• Refined Flow Microcalorimetric Setup for Measurement of Mixing Enthalpies at High Dilutions: Determination of Infinite Dilution Dissolution Enthalpies of Some Alkanol and Ether Solutes in Water
• Density, Speed of Sound, and Refractive Index of Aqueous Binary Mixtures of Some Glycol Ethers at T = 298.15 K
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB

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