Cyclopropyl carbinol (CAS 2516-33-8)

InChI

InChI=1S/C4H8O/c5-3-4-1-2-4/h4-5H,1-3H2

InChI Key

GUDMZGLFZNLYEY-UHFFFAOYSA-N

Formula

C4H8O

SMILES

OCC1CC1

Molecular Weight¹

72.11

CAS

2516-33-8

Other Names

Cyclopropanemethanol
Cyclopropanemethyl alcohol
Cyclopropylcarbinyl alcohol
Cyclopropylmethanol
Cyclopropylmethyl alcohol
Hydroxymethylcyclopropane

C_p,gas : Ideal gas heat capacity (J/mol×K).
η : Dynamic viscosity (Pa×s).
Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
logP_oct/wat : Octanol/Water partition coefficient.
McVol : McGowan's characteristic volume (ml/mol).
ρ_l : Liquid Density (kg/m³).
I_np : Non-polar retention indices.
T_boil : Normal Boiling Point Temperature (K).
T_boilr : Boiling point at reduced pressure (K).
T_fus : Normal melting (fusion) point (K).
¹: Molecular weight from the IUPAC atomic weights tables.

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Physical Properties

Property	Value	Unit	Source
Δ_fusH°	8.34	kJ/mol	Joback Calculated Property
logP_oct/wat	0.389		Crippen Calculated Property
McVol	62.230	ml/mol	McGowan Calculated Property
I_np	[648.00; 656.00]
I_np	648.00		NIST
I_np	648.00		NIST
I_np	656.00		NIST
T_boil	394.79	K	Relay (1.0) Calculated Property
T_fus	263.28	K	Relay (1.0) Calculated Property

Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Enthalpy of formation at standard conditions, Enthalpy of vaporization 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
ρ_l	[870.62; 913.02]	kg/m³	[293.15; 343.15]

ρ_l	913.02	kg/m³	293.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	912.99	kg/m³	293.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	908.94	kg/m³	298.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	908.96	kg/m³	298.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	904.85	kg/m³	303.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	904.87	kg/m³	303.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	900.74	kg/m³	308.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	900.74	kg/m³	308.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	896.58	kg/m³	313.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	896.59	kg/m³	313.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	892.38	kg/m³	318.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	892.38	kg/m³	318.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	888.13	kg/m³	323.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	888.17	kg/m³	323.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	883.84	kg/m³	328.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	883.86	kg/m³	328.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	879.49	kg/m³	333.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	879.52	kg/m³	333.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	875.07	kg/m³	338.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	875.10	kg/m³	338.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	870.62	kg/m³	343.15	Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
ρ_l	870.62	kg/m³	343.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
T_boilr	396.70	K	98.40	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[79.40; 224.10]	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			-4.56990e+01
Coefficient B			5.68700e-01
Coefficient C			-4.44400e-04
Coefficient D			1.45500e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00

C_p,gas	79.40	J/mol×K	273.00	Calculated Property
C_p,gas	106.32	J/mol×K	353.78	Calculated Property
C_p,gas	129.45	J/mol×K	434.56	Calculated Property
C_p,gas	149.27	J/mol×K	515.33	Calculated Property
C_p,gas	166.21	J/mol×K	596.11	Calculated Property
C_p,gas	180.76	J/mol×K	676.89	Calculated Property
C_p,gas	193.36	J/mol×K	757.67	Calculated Property
C_p,gas	204.48	J/mol×K	838.44	Calculated Property
C_p,gas	214.57	J/mol×K	919.22	Calculated Property
C_p,gas	224.10	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0254091; 0.0004298]	Pa×s	[213.60; 396.18]	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			-1.25248e+01
Coefficient B			1.89083e+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.			213.60
Temperature range, max.			396.18

η	0.0254091	Pa×s	213.60	Calculated Property
η	0.0117903	Pa×s	233.89	Calculated Property
η	0.0061843	Pa×s	254.17	Calculated Property
η	0.0035685	Pa×s	274.46	Calculated Property
η	0.0022210	Pa×s	294.75	Calculated Property
η	0.0014694	Pa×s	315.04	Calculated Property
η	0.0010220	Pa×s	335.32	Calculated Property
η	0.0007409	Pa×s	355.61	Calculated Property
η	0.0005560	Pa×s	375.90	Calculated Property
η	0.0004298	Pa×s	396.18	Calculated Property

Similar Compounds

Find more compounds similar to Cyclopropyl carbinol.

Mixtures

Sources

Cheméo Relay (1.0)
Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
Crippen Method
Crippen Method
Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K
Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
Joback Method
McGowan Method
NIST Webbook

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Chemical Properties of Cyclopropyl carbinol (CAS 2516-33-8)