Chemical Properties of 3-Pentanol (CAS 584-02-1)

InChI

InChI=1S/C5H12O/c1-3-5(6)4-2/h5-6H,3-4H2,1-2H3

InChI Key

AQIXEPGDORPWBJ-UHFFFAOYSA-N

Formula

C5H12O

SMILES

CCC(O)CC

Molecular Weight¹

88.15

CAS

584-02-1

Other Names

• (C2H5)2CHOH
• 1-Ethyl-1-propanol
• 3-Pentyl alcohol
• Diethyl carbinol
• Isoamyl alcohol
• NSC 8654
• Pentan-3-ol
• Pentanol-3
• UN 2706
• sec-Amyl alcohol
• sec-Pentanol
• sec-Pentyl alcohol

• ω : Acentric Factor.
• α_p : Isobaric thermal expansion coefficient (1/K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (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).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.5470		Relay (1.0) Calculated Property
ΔcH°liquid	-3312.30 ± 0.46	kJ/mol	NIST
Cp,liquid	254.60	J/mol×K	Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K
ΔfG°	-148.04	kJ/mol	Joback Calculated Property
ΔfH°gas	[-318.60; -314.70]	kJ/mol
ΔfH°gas	-317.20	kJ/mol	NIST
ΔfH°gas	-314.70 ± 1.10	kJ/mol	NIST
ΔfH°gas	-318.60 ± 1.50	kJ/mol	NIST
ΔfH°liquid	[-370.30; -368.90]	kJ/mol
ΔfH°liquid	-368.90 ± 0.79	kJ/mol	NIST
ΔfH°liquid	-370.30 ± 0.59	kJ/mol	NIST
ΔfusH°	1.66	kJ/mol	Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
ΔvapH°	[51.70; 54.03]	kJ/mol
ΔvapH°	54.03	kJ/mol	NIST
ΔvapH°	53.20 ± 0.10	kJ/mol	NIST
ΔvapH°	51.70 ± 1.30	kJ/mol	NIST
ΔvapH°	52.90	kJ/mol	NIST
IE	[9.73; 10.25]	eV
IE	9.76 ± 0.02	eV	NIST
IE	9.78 ± 0.07	eV	NIST
IE	9.78	eV	NIST
IE	9.78	eV	NIST
IE	9.73	eV	NIST
IE	Outlier 10.25	eV	NIST
log10WS	[-0.24; -0.24]
log10WS	-0.24		Aq. Solubility Prediction
log10WS	-0.24		Estimated Solubility
logPoct/wat	1.167		Crippen Calculated Property
McVol	87.180	ml/mol	McGowan Calculated Property
Pc	3916.03	kPa	Joback Calculated Property
ρc	[270.61; 270.61]	kg/m3
ρc	270.61	kg/m3	NIST
ρc	270.61 ± 20.27	kg/m3	NIST
Inp	[661.00; 712.00]
Inp	669.20		NIST
Inp	676.50		NIST
Inp	671.00		NIST
Inp	682.00		NIST
Inp	689.00		NIST
Inp	685.00		NIST
Inp	685.00		NIST
Inp	665.00		NIST
Inp	685.00		NIST
Inp	Outlier 661.00		NIST
Inp	687.00		NIST
Inp	688.00		NIST
Inp	703.00		NIST
Inp	Outlier 710.00		NIST
Inp	Outlier 712.00		NIST
Inp	689.00		NIST
Inp	687.00		NIST
Inp	693.00		NIST
Inp	689.00		NIST
Inp	683.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	690.00		NIST
Inp	684.00		NIST
Inp	687.00		NIST
Inp	669.00		NIST
Inp	678.00		NIST
Inp	680.00		NIST
Inp	687.00		NIST
Inp	683.00		NIST
Inp	669.20		NIST
Inp	685.00		NIST
Inp	Outlier 712.00		NIST
I	[1087.00; 1128.00]
I	1097.00		NIST
I	1102.00		NIST
I	1111.00		NIST
I	Outlier 1124.00		NIST
I	1108.00		NIST
I	1108.00		NIST
I	1110.00		NIST
I	1096.00		NIST
I	1100.00		NIST
I	Outlier 1087.00		NIST
I	1112.00		NIST
I	1113.00		NIST
I	1110.00		NIST
I	1098.00		NIST
I	1103.00		NIST
I	1111.00		NIST
I	1116.00		NIST
I	Outlier 1093.00		NIST
I	1101.00		NIST
I	1110.00		NIST
I	Outlier 1128.00		NIST
I	1109.00		NIST
I	1120.00		NIST
I	1111.00		NIST
I	1106.00		NIST
I	1108.00		NIST
I	1109.00		NIST
I	1104.00		NIST
I	1112.00		NIST
I	1112.00		NIST
I	1108.00		NIST
I	1116.00		NIST
I	1118.00		NIST
I	1110.00		NIST
I	1116.00		NIST
I	1112.00		NIST
I	1119.00		NIST
I	1110.00		NIST
I	1108.00		NIST
I	1112.00		NIST
I	1113.00		NIST
I	1113.00		NIST
I	1109.00		NIST
I	1111.00		NIST
I	1104.00		NIST
I	1107.00		NIST
I	1110.00		NIST
I	1104.00		NIST
I	1112.00		NIST
I	1108.00		NIST
I	1113.00		NIST
I	1107.00		NIST
I	1103.00		NIST
I	1110.00		NIST
I	1106.00		NIST
S°gas	382.21	J/mol×K	NIST
Tboil	[361.90; 391.10]	K
Tboil	389.40	K	KDB
Tboil	389.30	K	NIST
Tboil	Outlier 361.90 ± 1.50	K	NIST
Tboil	388.75 ± 2.00	K	NIST
Tboil	386.65 ± 2.00	K	NIST
Tboil	388.15 ± 3.00	K	NIST
Tboil	385.15 ± 3.00	K	NIST
Tboil	387.65 ± 1.50	K	NIST
Tboil	388.65 ± 0.30	K	NIST
Tboil	389.35 ± 0.50	K	NIST
Tboil	389.40 ± 1.00	K	NIST
Tboil	388.85 ± 0.50	K	NIST
Tboil	387.15 ± 2.00	K	NIST
Tboil	387.65 ± 2.00	K	NIST
Tboil	388.45 ± 1.00	K	NIST
Tboil	389.15 ± 1.00	K	NIST
Tboil	385.65 ± 3.00	K	NIST
Tboil	389.15 ± 0.70	K	NIST
Tboil	387.95 ± 2.00	K	NIST
Tboil	391.10 ± 2.00	K	NIST
Tboil	388.15 ± 2.00	K	NIST
Tboil	387.15 ± 2.00	K	NIST
Tboil	388.80 ± 0.50	K	NIST
Tboil	388.80 ± 0.20	K	NIST
Tboil	386.15 ± 3.00	K	NIST
Tboil	387.90 ± 2.00	K	NIST
Tboil	390.15 ± 2.00	K	NIST
Tboil	388.65 ± 1.00	K	NIST
Tboil	389.25 ± 0.30	K	NIST
Tboil	390.15 ± 2.00	K	NIST
Tboil	389.15 ± 2.00	K	NIST
Tboil	389.05 ± 0.50	K	NIST
Tboil	388.15 ± 0.50	K	NIST
Tboil	388.50 ± 0.30	K	NIST
Tboil	387.65 ± 2.00	K	NIST
Tboil	388.50 ± 0.50	K	NIST
Tboil	389.15 ± 2.00	K	NIST
Tboil	386.70 ± 2.00	K	NIST
Tc	[559.60; 559.60]	K
Tc	559.60	K	KDB
Tc	559.60 ± 0.50	K	NIST
Tc	559.60	K	NIST
Tc	559.60 ± 0.25	K	NIST
Tfus	[202.10; 204.00]	K
Tfus	204.00	K	KDB
Tfus	202.10	K	Aq. Solubility Prediction
Vc	[0.325; 0.325]	m3/kmol
Vc	0.325	m3/kmol	KDB
Vc	0.325	m3/kmol	NIST

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	239.70	J/mol×K	298.00	NIST
ΔfusH	[9.08; 9.08]	kJ/mol	[204.20; 204.20]
ΔfusH	9.08	kJ/mol	204.20	NIST
ΔfusH	9.08	kJ/mol	204.20	NIST
ΔvapH	[49.60; 59.90]	kJ/mol	[298.50; 353.00]
ΔvapH	53.60	kJ/mol	298.50	NIST
ΔvapH	59.90	kJ/mol	317.50	NIST
ΔvapH	50.20	kJ/mol	341.50	NIST
ΔvapH	49.60	kJ/mol	353.00	NIST
Pvap	[0.23; 97.99]	kPa	[279.05; 387.65]
Pvap	0.23	kPa	279.05	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.32	kPa	282.62	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.47	kPa	287.46	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.74	kPa	293.45	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	0.77	kPa	293.92	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	1.04	kPa	298.17	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	1.40	kPa	302.31	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	2.05	kPa	307.87	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	2.83	kPa	312.86	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	4.01	kPa	318.42	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap	14.66	kPa	342.02	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	17.33	kPa	345.41	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	20.00	kPa	348.40	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	22.66	kPa	351.07	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	26.00	kPa	354.07	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	29.33	kPa	356.77	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	32.66	kPa	359.24	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	34.66	kPa	360.62	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	38.00	kPa	362.79	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	41.33	kPa	364.81	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	45.33	kPa	367.06	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	49.33	kPa	369.16	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	53.33	kPa	371.13	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	57.33	kPa	372.99	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	61.33	kPa	374.75	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	66.66	kPa	376.95	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	71.99	kPa	379.02	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	77.33	kPa	380.97	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	82.66	kPa	382.82	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	89.33	kPa	385.00	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	95.99	kPa	387.06	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap	97.99	kPa	387.65	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
n0	[1.39810; 1.40870]		[298.15; 318.15]
n0	1.40870		298.15	Phase Equilibria in the Binary and Ternary Systems Composed of Diethyl ketone, 2-Pentanone and 3-Pentanol at 101.3 kPa
n0	1.40470		298.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
n0	1.40290		308.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
n0	1.39810		318.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
ρl	[806.90; 835.70]	kg/m3	[273.65; 308.15]
ρl	835.70	kg/m3	273.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	835.30	kg/m3	274.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	834.90	kg/m3	274.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	834.50	kg/m3	275.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	834.10	kg/m3	275.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	833.70	kg/m3	276.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	833.30	kg/m3	276.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	832.90	kg/m3	277.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	832.50	kg/m3	277.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	832.10	kg/m3	278.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	831.70	kg/m3	278.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	831.30	kg/m3	279.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	830.90	kg/m3	279.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	830.50	kg/m3	280.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	830.10	kg/m3	280.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	829.70	kg/m3	281.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	829.30	kg/m3	281.65	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	828.90	kg/m3	282.15	Temperature of maximum density for aqueous mixtures of three pentanol isomers
ρl	815.62	kg/m3	298.15	Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
ρl	815.80	kg/m3	298.15	Asymmetric liquid-liquid criticality in the ideal volumetric mixing approximation
ρl	806.90	kg/m3	308.15	Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	387.70	K	99.90	NIST

Datasets

1. Isobaric coefficient of expansion, 1/K (1)
2. Speed of sound, m/s (1)

Isobaric coefficient of expansion, 1/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Isobaric coefficient of expansion, 1/K - Liquid
278.15	5000.00	0.0009
278.15	10000.00	0.0009
278.15	15000.00	0.0009
278.15	20000.00	0.0008
278.15	25000.00	0.0008
278.15	30000.00	0.0008
278.15	35000.00	0.0008
278.15	40000.00	0.0008
278.15	45000.00	0.0008
278.15	50000.00	0.0008
278.15	55000.00	0.0007
288.15	5000.00	0.0009
288.15	10000.00	0.0009
288.15	15000.00	0.0009
288.15	20000.00	0.0009
288.15	25000.00	0.0009
288.15	30000.00	0.0009
288.15	35000.00	0.0008
288.15	40000.00	0.0008
288.15	45000.00	0.0008
288.15	50000.00	0.0008
288.15	55000.00	0.0008
298.15	5000.00	0.0010
298.15	10000.00	0.0010
298.15	15000.00	0.0009
298.15	20000.00	0.0009
298.15	25000.00	0.0009
298.15	30000.00	0.0009
298.15	35000.00	0.0009
298.15	40000.00	0.0009
298.15	45000.00	0.0008
298.15	50000.00	0.0008
298.15	55000.00	0.0008
308.15	5000.00	0.0010
308.15	10000.00	0.0010
308.15	15000.00	0.0010
308.15	20000.00	0.0010
308.15	25000.00	0.0009
308.15	30000.00	0.0009
308.15	35000.00	0.0009
308.15	40000.00	0.0009
308.15	45000.00	0.0009
308.15	50000.00	0.0009
308.15	55000.00	0.0008
318.15	5000.00	0.0011
318.15	10000.00	0.0010
318.15	15000.00	0.0010
318.15	20000.00	0.0010
318.15	25000.00	0.0010
318.15	30000.00	0.0010
318.15	35000.00	0.0009
318.15	40000.00	0.0009
318.15	45000.00	0.0009
318.15	50000.00	0.0009
318.15	55000.00	0.0009
328.15	5000.00	0.0011
328.15	10000.00	0.0011
328.15	15000.00	0.0010
328.15	20000.00	0.0010
328.15	25000.00	0.0010
328.15	30000.00	0.0010
328.15	35000.00	0.0010
328.15	40000.00	0.0009
328.15	45000.00	0.0009
328.15	50000.00	0.0009
328.15	55000.00	0.0009
338.15	5000.00	0.0011
338.15	10000.00	0.0011
338.15	15000.00	0.0011
338.15	20000.00	0.0011
338.15	25000.00	0.0010
338.15	30000.00	0.0010
338.15	35000.00	0.0010
338.15	40000.00	0.0010
338.15	45000.00	0.0010
338.15	50000.00	0.0009
338.15	55000.00	0.0009
348.15	5000.00	0.0012
348.15	10000.00	0.0012
348.15	15000.00	0.0011
348.15	20000.00	0.0011
348.15	25000.00	0.0011
348.15	30000.00	0.0011
348.15	35000.00	0.0010
348.15	40000.00	0.0010
348.15	45000.00	0.0010
348.15	50000.00	0.0010
348.15	55000.00	0.0009
Reference

Speed of sound, m/s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
303.15	100.00	1234.7
303.15	10000.00	1294.0
303.15	20000.00	1348.2
303.15	30000.00	1397.7
303.15	40000.00	1443.6
303.15	50000.00	1486.9
303.15	60000.00	1526.0
303.15	70000.00	1564.7
303.15	80000.00	1600.5
303.15	90000.00	1636.4
303.15	100000.00	1668.2
313.15	100.00	1194.7
313.15	10000.00	1257.0
313.15	20000.00	1313.0
313.15	30000.00	1364.7
313.15	40000.00	1411.9
313.15	50000.00	1456.0
313.15	60000.00	1498.1
313.15	70000.00	1537.4
313.15	80000.00	1574.5
313.15	90000.00	1610.2
313.15	100000.00	1644.1
323.15	100.00	1155.2
323.15	10000.00	1219.2
323.15	20000.00	1277.9
323.15	30000.00	1331.0
323.15	40000.00	1380.2
323.15	50000.00	1425.8
323.15	60000.00	1468.5
323.15	70000.00	1508.9
323.15	80000.00	1547.2
323.15	90000.00	1583.6
323.15	100000.00	1618.6
333.15	100.00	1115.9
333.15	10000.00	1182.2
333.15	20000.00	1243.1
333.15	30000.00	1298.2
333.15	40000.00	1348.6
333.15	50000.00	1395.9
333.15	60000.00	1439.4
333.15	70000.00	1480.7
333.15	80000.00	1519.8
333.15	90000.00	1556.9
333.15	100000.00	1592.2
343.15	100.00	1076.8
343.15	10000.00	1146.9
343.15	20000.00	1209.7
343.15	30000.00	1266.6
343.15	40000.00	1318.2
343.15	50000.00	1366.4
343.15	60000.00	1411.1
343.15	70000.00	1453.1
343.15	80000.00	1492.9
343.15	90000.00	1530.7
343.15	100000.00	1566.6
353.15	100.00	1036.7
353.15	10000.00	1110.4
353.15	20000.00	1176.2
353.15	30000.00	1234.1
353.15	40000.00	1287.8
353.15	50000.00	1337.3
353.15	60000.00	1383.1
353.15	70000.00	1425.8
353.15	80000.00	1466.6
353.15	90000.00	1505.0
353.15	100000.00	1541.4
363.15	100.00	997.3
363.15	10000.00	1075.3
363.15	20000.00	1143.2
363.15	30000.00	1203.5
363.15	40000.00	1258.2
363.15	50000.00	1308.3
363.15	60000.00	1355.1
363.15	70000.00	1399.6
363.15	80000.00	1440.8
363.15	90000.00	1479.7
363.15	100000.00	1516.9
373.15	100.00	957.2
373.15	10000.00	1038.9
373.15	20000.00	1109.6
373.15	30000.00	1171.5
373.15	40000.00	1228.3
373.15	50000.00	1280.1
373.15	60000.00	1328.2
373.15	70000.00	1373.1
373.15	80000.00	1415.0
373.15	90000.00	1454.6
373.15	100000.00	1492.5
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[123.74; 296.49]	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			1.95200e+00
Coefficient B			5.18740e-01
Coefficient C			-2.81800e-04
Coefficient D			5.76000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	123.74	J/mol×K	273.00	Calculated Property
Cp,gas	152.75	J/mol×K	353.78	Calculated Property
Cp,gas	178.89	J/mol×K	434.56	Calculated Property
Cp,gas	202.32	J/mol×K	515.33	Calculated Property
Cp,gas	223.24	J/mol×K	596.11	Calculated Property
Cp,gas	241.83	J/mol×K	676.89	Calculated Property
Cp,gas	258.27	J/mol×K	757.67	Calculated Property
Cp,gas	272.73	J/mol×K	838.44	Calculated Property
Cp,gas	285.42	J/mol×K	919.22	Calculated Property
Cp,gas	296.49	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.1456754; 0.0003533]	Pa×s	[203.05; 391.72]	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			-1.44290e+01
Coefficient B			2.53865e+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.			203.05
Temperature range, max.			391.72
η	0.1456754	Pa×s	203.05	Calculated Property
η	0.0452128	Pa×s	224.01	Calculated Property
η	0.0171435	Pa×s	244.98	Calculated Property
η	0.0075742	Pa×s	265.94	Calculated Property
η	0.0037706	Pa×s	286.90	Calculated Property
η	0.0020642	Pa×s	307.87	Calculated Property
η	0.0012202	Pa×s	328.83	Calculated Property
η	0.0007683	Pa×s	349.79	Calculated Property
η	0.0005097	Pa×s	370.76	Calculated Property
η	0.0003533	Pa×s	391.72	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[299.83; 409.85]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44746e+01
Coefficient B			-2.84676e+03
Coefficient C			-9.91730e+01
Temperature range, min.			299.83
Temperature range, max.			409.85
Pvap	1.33	kPa	299.83	Calculated Property
Pvap	3.01	kPa	312.05	Calculated Property
Pvap	6.22	kPa	324.28	Calculated Property
Pvap	11.94	kPa	336.50	Calculated Property
Pvap	21.48	kPa	348.73	Calculated Property
Pvap	36.60	kPa	360.95	Calculated Property
Pvap	59.45	kPa	373.18	Calculated Property
Pvap	92.65	kPa	385.40	Calculated Property
Pvap	139.24	kPa	397.63	Calculated Property
Pvap	202.66	kPa	409.85	Calculated Property
Pvap	[4.93e-05; 3720.52]	kPa	[204.15; 547.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			9.10919e+01
Coefficient B			-9.04205e+03
Coefficient C			-1.06916e+01
Coefficient D			3.55838e-06
Coefficient E			0.00000e+00
Temperature range, min.			204.15
Temperature range, max.			547.00
Pvap	4.93e-05	kPa	204.15	Calculated Property
Pvap	8.90e-03	kPa	242.24	Calculated Property
Pvap	0.32	kPa	280.34	Calculated Property
Pvap	4.21	kPa	318.43	Calculated Property
Pvap	28.63	kPa	356.53	Calculated Property
Pvap	123.86	kPa	394.62	Calculated Property
Pvap	388.85	kPa	432.72	Calculated Property
Pvap	967.13	kPa	470.81	Calculated Property
Pvap	2024.12	kPa	508.91	Calculated Property
Pvap	3720.52	kPa	547.00	Calculated Property

Similar Compounds

Find more compounds similar to 3-Pentanol.

Mixtures

• 3-Pentanol + Water
• Sodium nitrate + 3-Pentanol + Water
• Potassium nitrate + 3-Pentanol + Water
• Methane, nitro- + 3-Pentanol
• Carbon dioxide + 3-Pentanol
• 2-Butene, (Z)- + 3-Pentanol
• Dimethyl ether + 3-Pentanol
• Ethyl Chloride + 3-Pentanol
• Ethane, 1,1-difluoro- + 3-Pentanol
• Propane + 3-Pentanol
• Propene + 3-Pentanol
• Butane + 3-Pentanol
• 3-Pentanol + Isobutane
• 1-Butene + 3-Pentanol
• 1-Propene, 2-methyl- + 3-Pentanol
• 2-Butene, (E)- + 3-Pentanol
• 1,3-Butadiene + 3-Pentanol
• n-Butyl ether + 3-Pentanol
• 2-Butanone + 3-Pentanol
• 3-Pentanone + 3-Pentanol

Find more mixtures with 3-Pentanol.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
• The influence of cation, anion and temperature on the liquid-liquid equilibrium of some pentanols-water system
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-pentanol and 3-pentanol
• Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Study of the volumetric properties of weakly associated alcohols by means of high-pressure speed of sound measurements
• Isobaric thermal expansivity behaviour against temperature and pressure of associating fluids
• Measurement and modeling of high-pressure (vapor + liquid) equilibria of (CO2 + alkanol) binary systems
• Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
• Temperature of maximum density for aqueous mixtures of three pentanol isomers
• Asymmetric liquid-liquid criticality in the ideal volumetric mixing approximation
• Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
• Phase Equilibria in the Binary and Ternary Systems Composed of Diethyl ketone, 2-Pentanone and 3-Pentanol at 101.3 kPa
• Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K
• Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
• Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
• Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched Pentanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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