Chemical Properties of 1-Decanol (CAS 112-30-1)

InChI

InChI=1S/C10H22O/c1-2-3-4-5-6-7-8-9-10-11/h11H,2-10H2,1H3

InChI Key

MWKFXSUHUHTGQN-UHFFFAOYSA-N

Formula

C10H22O

SMILES

CCCCCCCCCCO

Molecular Weight¹

158.28

CAS

112-30-1

Other Names

• 1-Hydroxydecane
• Agent 504
• Alcohol C10
• Alfol 10
• Antak
• C 10 alcohol
• Capric alcohol
• Caprinic alcohol
• Conol 10N
• Decan-1-ol
• Decanol
• Decanol-(1)
• Decyl alcohol
• Decyl, n- alcohol
• Decylic Alcohol
• Dytol S-91
• Epal 10
• Kalcohl 10H
• Lorol 22
• Lorol C10
• NSC 406313
• Nacol 10-99
• Nonylcacarbinol
• Nonylcarbinol
• Primary decyl alcohol
• Royaltac
• Royaltac M-2
• Royaltac-85
• Sipol L10
• T-148
• n-Decan-1-ol
• n-Decanol
• n-Decyl alcohol

• 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).
• 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_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_subH° : Enthalpy of sublimation at standard conditions (kJ/mol).
• Δ_subH : Enthalpy of sublimation 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).
• 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.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point 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.
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• 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).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• 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
ΔcH°liquid	[-6619.00; -6593.10]	kJ/mol
ΔcH°liquid	-6619.00 ± 8.00	kJ/mol	NIST
ΔcH°liquid	-6601.10 ± 1.10	kJ/mol	NIST
ΔcH°liquid	-6599.63 ± 0.75	kJ/mol	NIST
ΔcH°liquid	-6593.30 ± 3.30	kJ/mol	NIST
ΔcH°liquid	-6593.10	kJ/mol	NIST
μ	1.80	debye	KDB
η	0.0111922	Pa×s	Volumet...
Tflash,cc	355.37	K	KDB
ΔfG°	-104.30	kJ/mol	KDB
ΔfH°gas	[-404.60; -387.20]	kJ/mol
ΔfH°gas	-401.90	kJ/mol	KDB
ΔfH°gas	-387.20	kJ/mol	NIST
ΔfH°gas	-396.60 ± 1.40	kJ/mol	NIST
ΔfH°gas	-388.80	kJ/mol	NIST
ΔfH°gas	-398.20 ± 1.20	kJ/mol	NIST
ΔfH°gas	-395.20 ± 2.40	kJ/mol	NIST
ΔfH°gas	-404.60 ± 3.10	kJ/mol	NIST
ΔfH°liquid	[-486.10; -478.10]	kJ/mol
ΔfH°liquid	-478.10 ± 1.10	kJ/mol	NIST
ΔfH°liquid	-479.74 ± 0.96	kJ/mol	NIST
ΔfH°liquid	-486.10 ± 3.30	kJ/mol	NIST
ΔfH°liquid	-486.10 ± 3.00	kJ/mol	NIST
ΔfusH°	[31.40; 33.67]	kJ/mol
ΔfusH°	33.67	kJ/mol	Heat Ca...
ΔfusH°	31.40	kJ/mol	Measure...
ΔsubH°	112.50 ± 6.30	kJ/mol	NIST
ΔvapH°	[77.80; 90.90]	kJ/mol
ΔvapH°	81.50	kJ/mol	NIST
ΔvapH°	80.90	kJ/mol	NIST
ΔvapH°	81.70	kJ/mol	NIST
ΔvapH°	79.30	kJ/mol	NIST
ΔvapH°	81.49 ± 0.78	kJ/mol	NIST
ΔvapH°	81.50 ± 0.80	kJ/mol	NIST
ΔvapH°	81.50 ± 0.75	kJ/mol	NIST
ΔvapH°	81.50 ± 0.80	kJ/mol	NIST
ΔvapH°	77.80 ± 0.80	kJ/mol	NIST
ΔvapH°	82.90 ± 2.10	kJ/mol	NIST
ΔvapH°	Outlier 90.90	kJ/mol	NIST
log10WS	[-3.63; -3.63]
log10WS	-3.63		Aq. Sol...
log10WS	-3.63		Estimat...
logPoct/wat	3.119		Crippen Calculated Property
McVol	157.630	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
Pc	[2310.00; 2320.00]	kPa
Pc	2315.00	kPa	KDB
Pc	2320.00 ± 50.00	kPa	NIST
Pc	2310.00 ± 60.00	kPa	NIST
Pc	2320.00 ± 20.00	kPa	NIST
Pc	2320.00 ± 20.00	kPa	NIST
Ptriple	1.00e-04 ± 1.30e-05	kPa	NIST
ρc	[243.75; 264.33]	kg/m3
ρc	243.75 ± 7.91	kg/m3	NIST
ρc	264.33	kg/m3	NIST
ρc	243.75 ± 6.33	kg/m3	NIST
ρc	264.33 ± 3.17	kg/m3	NIST
Inp	[215.20; 1287.00]
Inp	1271.19		NIST
Inp	1255.70		NIST
Inp	1280.00		NIST
Inp	1262.00		NIST
Inp	1254.00		NIST
Inp	1254.00		NIST
Inp	1254.00		NIST
Inp	1255.00		NIST
Inp	1255.00		NIST
Inp	1255.00		NIST
Inp	1255.00		NIST
Inp	1256.00		NIST
Inp	1262.00		NIST
Inp	1262.00		NIST
Inp	1262.00		NIST
Inp	1249.00		NIST
Inp	1247.00		NIST
Inp	1247.00		NIST
Inp	1244.00		NIST
Inp	1247.00		NIST
Inp	1241.00		NIST
Inp	1256.00		NIST
Inp	1246.00		NIST
Inp	1252.00		NIST
Inp	1260.00		NIST
Inp	1253.00		NIST
Inp	1264.00		NIST
Inp	1262.00		NIST
Inp	1264.00		NIST
Inp	1276.00		NIST
Inp	1263.00		NIST
Inp	1259.00		NIST
Inp	1255.00		NIST
Inp	1257.00		NIST
Inp	1257.00		NIST
Inp	1272.00		NIST
Inp	1256.00		NIST
Inp	1272.00		NIST
Inp	1275.00		NIST
Inp	1275.00		NIST
Inp	1279.00		NIST
Inp	1272.00		NIST
Inp	1255.20		NIST
Inp	1273.80		NIST
Inp	1258.00		NIST
Inp	1281.00		NIST
Inp	1272.00		NIST
Inp	1272.00		NIST
Inp	1285.00		NIST
Inp	1259.00		NIST
Inp	1273.00		NIST
Inp	1274.00		NIST
Inp	1267.00		NIST
Inp	1256.90		NIST
Inp	1258.90		NIST
Inp	1269.00		NIST
Inp	1274.00		NIST
Inp	1282.50		NIST
Inp	1264.00		NIST
Inp	1254.00		NIST
Inp	1259.00		NIST
Inp	1271.00		NIST
Inp	1269.00		NIST
Inp	1267.00		NIST
Inp	1267.00		NIST
Inp	1273.00		NIST
Inp	1274.00		NIST
Inp	1275.00		NIST
Inp	1271.00		NIST
Inp	1273.00		NIST
Inp	1273.00		NIST
Inp	1273.00		NIST
Inp	1274.00		NIST
Inp	1274.00		NIST
Inp	1274.00		NIST
Inp	1274.00		NIST
Inp	1274.00		NIST
Inp	1275.00		NIST
Inp	1276.00		NIST
Inp	1278.00		NIST
Inp	1274.00		NIST
Inp	1263.00		NIST
Inp	1278.00		NIST
Inp	1272.00		NIST
Inp	1272.00		NIST
Inp	1255.00		NIST
Inp	1255.00		NIST
Inp	1270.00		NIST
Inp	1270.00		NIST
Inp	1275.00		NIST
Inp	1275.00		NIST
Inp	1272.00		NIST
Inp	1270.00		NIST
Inp	1272.00		NIST
Inp	1263.00		NIST
Inp	1266.00		NIST
Inp	1272.00		NIST
Inp	1266.00		NIST
Inp	1269.00		NIST
Inp	1254.00		NIST
Inp	1263.00		NIST
Inp	1257.00		NIST
Inp	1255.00		NIST
Inp	1266.00		NIST
Inp	1275.00		NIST
Inp	1279.00		NIST
Inp	1283.00		NIST
Inp	1259.00		NIST
Inp	1279.00		NIST
Inp	1281.00		NIST
Inp	1285.00		NIST
Inp	1261.00		NIST
Inp	1269.00		NIST
Inp	1263.00		NIST
Inp	1272.00		NIST
Inp	1272.00		NIST
Inp	1287.00		NIST
Inp	1270.00		NIST
Inp	1281.00		NIST
Inp	1284.00		NIST
Inp	1287.00		NIST
Inp	1261.00		NIST
Inp	1269.00		NIST
Inp	1272.00		NIST
Inp	1264.00		NIST
Inp	1263.00		NIST
Inp	1256.00		NIST
Inp	1272.10		NIST
Inp	1259.00		NIST
Inp	1259.00		NIST
Inp	1257.00		NIST
Inp	1257.00		NIST
Inp	1263.00		NIST
Inp	1283.00		NIST
Inp	1257.00		NIST
Inp	1249.00		NIST
Inp	1261.00		NIST
Inp	Outlier 215.20		NIST
Inp	Outlier 216.62		NIST
Inp	Outlier 216.09		NIST
Inp	1259.00		NIST
Inp	1266.00		NIST
Inp	1279.00		NIST
Inp	1263.00		NIST
Inp	1281.00		NIST
Inp	1272.00		NIST
Inp	1283.00		NIST
Inp	Outlier 215.20		NIST
Inp	1273.00		NIST
Inp	1269.00		NIST
Inp	1274.00		NIST
Inp	1271.00		NIST
Inp	1271.19		NIST
Inp	1254.00		NIST
Inp	1255.00		NIST
Inp	1249.00		NIST
Inp	1241.00		NIST
Inp	1253.00		NIST
I	[1714.00; 1783.00]
I	1724.00		NIST
I	1769.00		NIST
I	1746.00		NIST
I	1726.00		NIST
I	1760.00		NIST
I	1759.00		NIST
I	1753.00		NIST
I	1764.00		NIST
I	1783.00		NIST
I	1750.00		NIST
I	1740.00		NIST
I	1732.00		NIST
I	1736.00		NIST
I	1740.00		NIST
I	1757.00		NIST
I	1757.00		NIST
I	1769.00		NIST
I	1759.00		NIST
I	1763.00		NIST
I	1767.00		NIST
I	1760.00		NIST
I	1771.00		NIST
I	Outlier 1714.00		NIST
I	1763.00		NIST
I	1748.00		NIST
I	1744.00		NIST
I	1745.00		NIST
I	1748.00		NIST
I	1748.00		NIST
I	1735.00		NIST
I	1735.00		NIST
I	1763.00		NIST
I	1764.90		NIST
I	1770.00		NIST
I	1765.00		NIST
I	1770.00		NIST
I	1752.00		NIST
I	1751.00		NIST
I	1726.00		NIST
I	1756.00		NIST
I	1729.00		NIST
I	1767.00		NIST
I	1761.00		NIST
I	1764.00		NIST
I	1760.00		NIST
I	1767.00		NIST
I	1778.00		NIST
I	1768.00		NIST
I	1769.00		NIST
I	1783.00		NIST
I	Outlier 1723.00		NIST
I	1766.00		NIST
I	1766.00		NIST
I	1753.00		NIST
I	1778.00		NIST
I	1781.00		NIST
I	1752.00		NIST
I	1752.00		NIST
I	1781.00		NIST
I	1781.00		NIST
I	1765.00		NIST
I	1781.00		NIST
I	1750.00		NIST
I	1766.00		NIST
I	1766.00		NIST
I	1735.00		NIST
I	1752.00		NIST
I	1767.00		NIST
I	1748.00		NIST
I	1735.00		NIST
I	1765.00		NIST
I	1757.00		NIST
I	1756.00		NIST
I	1760.00		NIST
I	1783.00		NIST
I	1724.00		NIST
I	1759.00		NIST
I	1740.00		NIST
Tboil	[502.95; 504.20]	K
Tboil	504.20	K	KDB
Tboil	503.70	K	Phase e...
Tboil	503.70	K	(Liquid...
Tboil	503.70	K	(Liquid...
Tboil	502.95	K	Study o...
Tc	[687.00; 708.00]	K
Tc	687.30	K	KDB
Tc	687.00 ± 1.00	K	NIST
Tc	687.70 ± 1.00	K	NIST
Tc	687.00 ± 0.70	K	NIST
Tc	687.00 ± 0.60	K	NIST
Tc	687.10	K	NIST
Tc	687.30 ± 1.30	K	NIST
Tc	687.00	K	NIST
Tc	Outlier 708.00 ± 2.00	K	NIST
Tfus	[276.15; 280.51]	K
Tfus	279.87	K	Aq. Sol...
Tfus	280.00	K	KDB
Tfus	280.15	K	Experim...
Tfus	280.19	K	SLE and...
Tfus	280.10	K	(Solid ...
Tfus	278.20	K	Phase e...
Tfus	Outlier 276.15	K	The man...
Tfus	278.67	K	Experim...
Tfus	280.51	K	Phase E...
Tfus	280.19	K	Solid-L...
Tfus	279.60 ± 0.50	K	NIST
Tfus	280.05 ± 0.40	K	NIST
Tfus	277.00 ± 3.00	K	NIST
Ttriple	[275.64; 279.65]	K
Ttriple	275.64	K	Solid-l...
Ttriple	279.65 ± 1.00	K	NIST
Vc	[0.649; 0.649]	m3/kmol
Vc	0.649	m3/kmol	KDB
Vc	0.649	m3/kmol	NIST
Zc	0.2629130		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[380.60; 452.73]	J/mol×K	[520.38; 678.87]
Cp,gas	380.60	J/mol×K	520.38	Joback Calculated Property
Cp,gas	393.83	J/mol×K	546.79	Joback Calculated Property
Cp,gas	406.56	J/mol×K	573.21	Joback Calculated Property
Cp,gas	418.80	J/mol×K	599.62	Joback Calculated Property
Cp,gas	430.56	J/mol×K	626.04	Joback Calculated Property
Cp,gas	441.87	J/mol×K	652.45	Joback Calculated Property
Cp,gas	452.73	J/mol×K	678.87	Joback Calculated Property
Cp,liquid	[369.96; 387.80]	J/mol×K	[298.15; 305.79]
Cp,liquid	372.98	J/mol×K	298.15	NIST
Cp,liquid	369.96	J/mol×K	298.15	NIST
Cp,liquid	377.00	J/mol×K	301.00	NIST
Cp,liquid	377.30	J/mol×K	303.15	NIST
Cp,liquid	387.80	J/mol×K	304.05	NIST
Cp,liquid	377.80	J/mol×K	305.79	NIST
η	[0.0023990; 0.0220640]	Pa×s	[283.15; 348.15]
η	0.0220640	Pa×s	283.15	Density...
η	0.0220640	Pa×s	283.15	Measure...
η	0.0179880	Pa×s	288.15	Measure...
η	0.0144990	Pa×s	293.15	Density...
η	0.0143870	Pa×s	293.15	Measure...
η	0.0110900	Pa×s	298.15	Density...
η	0.0114710	Pa×s	298.15	Density...
η	0.0118250	Pa×s	298.15	Acousti...
η	0.0117350	Pa×s	298.15	Measure...
η	0.0103000	Pa×s	300.00	Tempera...
η	0.0095610	Pa×s	303.15	Measure...
η	0.0097540	Pa×s	303.15	Acousti...
η	0.0097150	Pa×s	303.15	Densiti...
η	0.0097160	Pa×s	303.15	Densiti...
η	0.0096100	Pa×s	303.15	Density...
η	0.0080000	Pa×s	308.15	Measure...
η	0.0081350	Pa×s	308.15	Acousti...
η	0.0076320	Pa×s	308.15	Density...
η	0.0070900	Pa×s	310.00	Tempera...
η	0.0069000	Pa×s	313.15	Density...
η	0.0068420	Pa×s	313.15	Acousti...
η	0.0068190	Pa×s	313.15	Densiti...
η	0.0068310	Pa×s	313.15	Measure...
η	0.0068200	Pa×s	313.15	Densiti...
η	0.0053750	Pa×s	318.15	Density...
η	0.0050000	Pa×s	320.00	Tempera...
η	0.0039280	Pa×s	328.15	Density...
η	0.0036700	Pa×s	330.00	Tempera...
η	0.0029640	Pa×s	338.15	Density...
η	0.0027400	Pa×s	340.00	Tempera...
η	0.0023990	Pa×s	348.15	Density...
ΔfusH	[33.67; 37.66]	kJ/mol	[280.00; 280.10]
ΔfusH	33.67	kJ/mol	280.00	NIST
ΔfusH	37.66	kJ/mol	280.10	NIST
ΔfusH	37.66	kJ/mol	280.10	NIST
ΔsubH	115.50 ± 6.30	kJ/mol	268.50	NIST
ΔvapH	[50.21; 81.10]	kJ/mol	[304.00; 504.10]
ΔvapH	79.50	kJ/mol	304.00	NIST
ΔvapH	77.60	kJ/mol	311.50	NIST
ΔvapH	77.60	kJ/mol	311.50	NIST
ΔvapH	78.20 ± 0.80	kJ/mol	323.00	NIST
ΔvapH	78.18	kJ/mol	323.15	NIST
ΔvapH	81.10	kJ/mol	328.00	NIST
ΔvapH	75.40	kJ/mol	335.50	NIST
ΔvapH	71.60	kJ/mol	379.50	NIST
ΔvapH	69.60	kJ/mol	412.50	NIST
ΔvapH	69.50	kJ/mol	441.00	NIST
ΔvapH	62.60	kJ/mol	466.50	NIST
ΔvapH	53.90	kJ/mol	501.50	NIST
ΔvapH	50.21	kJ/mol	504.10	KDB
Pvap	[1.00e-03; 94.90]	kPa	[308.15; 501.05]
Pvap	1.00e-03	kPa	308.15	Vapor L...
Pvap	4.00e-03	kPa	313.15	Isother...
Pvap	4.00e-03	kPa	313.15	Vapor L...
Pvap	7.00e-03	kPa	318.15	Isother...
Pvap	7.00e-03	kPa	318.15	Vapor L...
Pvap	0.01	kPa	323.15	Isother...
Pvap	0.01	kPa	323.15	Vapor L...
Pvap	13.32	kPa	436.56	Isobari...
Pvap	40.00	kPa	469.23	Low-Pre...
Pvap	39.99	kPa	469.52	Isobari...
Pvap	40.03	kPa	469.83	Low-Pre...
Pvap	44.40	kPa	472.98	Low-Pre...
Pvap	47.97	kPa	475.40	Low-Pre...
Pvap	50.19	kPa	476.80	Low-Pre...
Pvap	54.07	kPa	479.42	Low-Pre...
Pvap	57.04	kPa	481.36	Low-Pre...
Pvap	61.26	kPa	484.05	Low-Pre...
Pvap	66.66	kPa	487.85	Isobari...
Pvap	67.43	kPa	487.90	Low-Pre...
Pvap	73.44	kPa	491.16	Low-Pre...
Pvap	76.32	kPa	492.56	Low-Pre...
Pvap	79.92	kPa	494.46	Low-Pre...
Pvap	85.24	kPa	496.88	Low-Pre...
Pvap	94.90	kPa	501.05	Isobari...
n0	[1.43050; 1.43706]		[293.15; 308.15]
n0	1.43706		293.15	Densiti...
n0	1.43700		293.15	Effect ...
n0	1.43706		293.15	Excess ...
n0	1.43694		293.15	Densiti...
n0	1.43456		298.15	Densiti...
n0	1.43460		298.15	Densiti...
n0	1.43436		298.15	Liquid ...
n0	1.43440		298.20	Tie-lin...
n0	1.43490		298.20	Solubil...
n0	1.43440		298.20	Ternary...
n0	1.43302		303.15	Densiti...
n0	1.43364		303.15	Densiti...
n0	1.43260		303.15	Densiti...
n0	1.43256		303.15	Densiti...
n0	1.43266		303.15	Densiti...
n0	1.43050		308.15	Densiti...
n0	1.43050		308.15	Densiti...
ρl	[780.34; 836.51]	kg/m3	[283.15; 363.15]
ρl	836.51	kg/m3	283.15	Densiti...
ρl	833.14	kg/m3	288.15	Densiti...
ρl	830.00	kg/m3	293.00	KDB
ρl	829.50	kg/m3	293.15	Investi...
ρl	829.99	kg/m3	293.15	Thermop...
ρl	829.76	kg/m3	293.15	Densiti...
ρl	829.97	kg/m3	293.15	Thermod...
ρl	829.95	kg/m3	293.15	Thermod...
ρl	829.76	kg/m3	293.15	Speeds ...
ρl	829.50	kg/m3	293.15	Correla...
ρl	826.58	kg/m3	298.15	Thermod...
ρl	826.36	kg/m3	298.15	Volumet...
ρl	826.10	kg/m3	298.15	Correla...
ρl	826.10	kg/m3	298.15	Investi...
ρl	826.49	kg/m3	298.15	Thermod...
ρl	826.90	kg/m3	298.15	Viscosi...
ρl	826.37	kg/m3	298.15	Speeds ...
ρl	826.41	kg/m3	298.15	Densiti...
ρl	826.95	kg/m3	298.15	Thermod...
ρl	826.58	kg/m3	298.15	Thermod...
ρl	826.56	kg/m3	298.15	Physico...
ρl	827.21	kg/m3	298.15	Thermod...
ρl	826.38	kg/m3	298.15	Densiti...
ρl	826.47	kg/m3	298.15	Studies...
ρl	826.38	kg/m3	298.15	Phase b...
ρl	826.64	kg/m3	298.15	Experim...
ρl	826.38	kg/m3	298.15	Phase b...
ρl	826.31	kg/m3	298.15	Excess ...
ρl	826.74	kg/m3	298.15	Effect ...
ρl	826.41	kg/m3	298.20	Optimiz...
ρl	826.86	kg/m3	298.20	Experim...
ρl	822.95	kg/m3	303.15	Speeds ...
ρl	822.88	kg/m3	303.15	Volumet...
ρl	822.89	kg/m3	303.15	Effect ...
ρl	822.95	kg/m3	303.15	Excess ...
ρl	822.70	kg/m3	303.15	Correla...
ρl	822.70	kg/m3	303.15	Investi...
ρl	823.76	kg/m3	303.15	Thermod...
ρl	822.98	kg/m3	303.15	Densiti...
ρl	823.13	kg/m3	303.15	Thermod...
ρl	823.15	kg/m3	303.15	Thermod...
ρl	819.57	kg/m3	308.15	Speeds ...
ρl	820.31	kg/m3	308.15	Thermod...
ρl	819.43	kg/m3	308.15	Volumet...
ρl	819.30	kg/m3	308.15	Correla...
ρl	819.30	kg/m3	308.15	Investi...
ρl	820.00	kg/m3	308.15	Viscosi...
ρl	819.51	kg/m3	308.15	Effect ...
ρl	819.57	kg/m3	308.15	Densiti...
ρl	815.95	kg/m3	313.15	Effect ...
ρl	816.12	kg/m3	313.15	Speeds ...
ρl	815.97	kg/m3	313.15	Volumet...
ρl	816.15	kg/m3	313.15	Densiti...
ρl	816.83	kg/m3	313.15	Thermod...
ρl	815.80	kg/m3	313.15	Correla...
ρl	815.80	kg/m3	313.15	Investi...
ρl	813.34	kg/m3	318.15	Thermod...
ρl	812.40	kg/m3	318.15	Correla...
ρl	812.49	kg/m3	318.15	Volumet...
ρl	812.63	kg/m3	318.15	Speeds ...
ρl	812.40	kg/m3	318.15	Investi...
ρl	812.71	kg/m3	318.15	Densiti...
ρl	813.00	kg/m3	318.15	Viscosi...
ρl	809.03	kg/m3	323.15	Volumet...
ρl	809.24	kg/m3	323.15	Densiti...
ρl	808.90	kg/m3	323.15	Investi...
ρl	808.90	kg/m3	323.15	Correla...
ρl	809.82	kg/m3	323.15	Thermod...
ρl	806.00	kg/m3	328.15	Viscosi...
ρl	805.74	kg/m3	328.15	Densiti...
ρl	802.21	kg/m3	333.15	Densiti...
ρl	798.65	kg/m3	338.15	Densiti...
ρl	798.90	kg/m3	338.15	Viscosi...
ρl	795.06	kg/m3	343.15	Densiti...
ρl	791.43	kg/m3	348.15	Densiti...
ρl	787.77	kg/m3	353.15	Densiti...
ρl	784.07	kg/m3	358.15	Densiti...
ρl	780.34	kg/m3	363.15	Densiti...
csound,fluid	[1311.69; 1410.60]	m/s	[288.15; 318.18]
csound,fluid	1410.60	m/s	288.15	Ultraso...
csound,fluid	1397.23	m/s	293.10	Excess ...
csound,fluid	1393.60	m/s	293.15	Ultraso...
csound,fluid	1396.65	m/s	293.15	Thermod...
csound,fluid	1396.00	m/s	293.15	Densiti...
csound,fluid	1379.96	m/s	298.07	Excess ...
csound,fluid	1379.43	m/s	298.15	Thermod...
csound,fluid	1380.58	m/s	298.15	Micella...
csound,fluid	1377.30	m/s	298.15	Ultraso...
csound,fluid	1362.82	m/s	303.04	Excess ...
csound,fluid	1359.80	m/s	303.15	Ultraso...
csound,fluid	1362.00	m/s	303.15	Densiti...
csound,fluid	1363.52	m/s	303.15	Micella...
csound,fluid	1362.40	m/s	303.15	Thermod...
csound,fluid	1345.82	m/s	308.04	Excess ...
csound,fluid	1345.70	m/s	308.15	Ultraso...
csound,fluid	1345.62	m/s	308.15	Thermod...
csound,fluid	1346.58	m/s	308.15	Micella...
csound,fluid	1329.03	m/s	313.01	Excess ...
csound,fluid	1329.07	m/s	313.15	Thermod...
csound,fluid	1326.70	m/s	313.15	Ultraso...
csound,fluid	1329.00	m/s	313.15	Densiti...
csound,fluid	1312.10	m/s	318.15	Ultraso...
csound,fluid	1311.69	m/s	318.18	Excess ...
γ	0.03	N/m	293.20	KDB
ΔvapS	241.93	J/mol×K	323.15	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	380.70	K	0.90	NIST

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (4)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	2000.00	0.0113
298.15	3990.00	0.0115
298.15	6010.00	0.0118
298.15	8010.00	0.0121
298.15	10010.00	0.0123
298.15	13010.00	0.0127
298.15	16010.00	0.0132
298.15	19010.00	0.0136
298.15	22010.00	0.0140
298.15	25000.00	0.0145
298.15	28000.00	0.0149
298.15	29990.00	0.0152
303.15	1990.00	0.0089
303.15	4000.00	0.0091
303.15	5980.00	0.0093
303.15	8010.00	0.0096
303.15	10020.00	0.0098
303.15	12980.00	0.0101
303.15	15970.00	0.0104
303.15	19020.00	0.0108
303.15	22000.00	0.0111
303.15	24980.00	0.0114
303.15	27980.00	0.0118
303.15	30010.00	0.0120
313.15	2030.00	0.0062
313.15	4020.00	0.0064
313.15	6000.00	0.0065
313.15	7980.00	0.0067
313.15	9980.00	0.0068
313.15	12990.00	0.0071
313.15	15990.00	0.0073
313.15	18990.00	0.0075
313.15	22010.00	0.0078
313.15	25020.00	0.0080
313.15	28020.00	0.0082
313.15	29980.00	0.0084
323.15	2000.00	0.0047
323.15	4010.00	0.0049
323.15	6010.00	0.0050
323.15	8010.00	0.0051
323.15	9990.00	0.0052
323.15	13010.00	0.0054
323.15	16010.00	0.0055
323.15	19020.00	0.0057
323.15	22020.00	0.0059
323.15	25010.00	0.0061
323.15	28000.00	0.0062
323.15	30010.00	0.0064
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	826.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	832.3
288.15	1000.00	832.8
288.15	5000.00	835.2
288.15	10000.00	838.0
288.15	15000.00	840.8
288.15	20000.00	843.5
288.15	25000.00	846.1
288.15	30000.00	848.6
288.15	35000.00	851.1
288.15	40000.00	853.5
288.15	45000.00	855.9
288.15	50000.00	858.2
288.15	55000.00	860.4
288.15	60000.00	862.7
298.15	100.00	825.5
298.15	1000.00	826.0
298.15	5000.00	828.5
298.15	10000.00	831.5
298.15	15000.00	834.4
298.15	20000.00	837.2
298.15	25000.00	839.8
298.15	30000.00	842.5
298.15	35000.00	845.1
298.15	40000.00	847.6
298.15	45000.00	850.0
298.15	50000.00	852.4
298.15	55000.00	854.7
298.15	60000.00	856.8
308.15	100.00	818.7
308.15	1000.00	819.3
308.15	5000.00	821.9
308.15	10000.00	825.0
308.15	15000.00	828.0
308.15	20000.00	830.9
308.15	25000.00	833.7
308.15	30000.00	836.4
308.15	35000.00	839.1
308.15	40000.00	841.7
308.15	45000.00	844.2
308.15	50000.00	846.6
308.15	55000.00	849.0
308.15	60000.00	851.2
318.15	100.00	811.9
318.15	1000.00	812.5
318.15	5000.00	815.3
318.15	10000.00	818.5
318.15	15000.00	821.7
318.15	20000.00	824.7
318.15	25000.00	827.6
318.15	30000.00	830.4
318.15	35000.00	833.2
318.15	40000.00	835.8
318.15	45000.00	838.5
318.15	50000.00	841.0
318.15	55000.00	843.4
318.15	60000.00	845.7
328.15	100.00	805.0
328.15	1000.00	805.7
328.15	5000.00	808.5
328.15	10000.00	811.9
328.15	15000.00	815.2
328.15	20000.00	818.3
328.15	25000.00	821.4
328.15	30000.00	824.3
328.15	35000.00	827.1
328.15	40000.00	829.9
328.15	45000.00	832.6
328.15	50000.00	835.2
328.15	55000.00	837.7
328.15	60000.00	840.2
338.15	100.00	798.0
338.15	1000.00	798.7
338.15	5000.00	801.7
338.15	10000.00	805.2
338.15	15000.00	808.7
338.15	20000.00	812.0
338.15	25000.00	815.1
338.15	30000.00	818.1
338.15	35000.00	821.1
338.15	40000.00	824.0
338.15	45000.00	826.7
338.15	50000.00	829.4
338.15	55000.00	832.1
338.15	60000.00	834.5
348.15	100.00	790.9
348.15	1000.00	791.6
348.15	5000.00	794.8
348.15	10000.00	798.5
348.15	15000.00	802.0
348.15	20000.00	805.5
348.15	25000.00	808.8
348.15	30000.00	811.9
348.15	35000.00	815.0
348.15	40000.00	817.9
348.15	45000.00	820.8
348.15	50000.00	823.6
348.15	55000.00	826.4
348.15	60000.00	829.0
358.15	100.00	783.6
358.15	1000.00	784.3
358.15	5000.00	787.6
358.15	10000.00	791.6
358.15	15000.00	795.3
358.15	20000.00	798.9
358.15	25000.00	802.3
358.15	30000.00	805.6
358.15	35000.00	808.8
358.15	40000.00	811.9
358.15	45000.00	814.8
358.15	50000.00	817.7
358.15	55000.00	820.5
358.15	60000.00	822.9
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	826.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.12	1025.00	816.79
313.12	2002.00	817.46
313.12	2995.00	817.98
313.12	4013.00	818.58
313.12	5004.00	819.21
313.12	5994.00	819.86
313.12	7003.00	820.47
313.12	7997.00	821.19
313.12	9000.00	821.73
313.12	9994.00	822.38
313.12	10995.00	823.02
313.12	11995.00	823.67
313.12	12997.00	824.2
313.12	13996.00	824.82
313.12	14998.00	825.42
313.12	15990.00	826.01
313.12	16995.00	826.61
313.12	17986.00	827.14
313.12	18992.00	827.76
313.12	19993.00	828.31
313.12	20999.00	828.88
313.12	21509.00	829.19
323.09	1002.00	809.87
323.09	2011.00	810.59
323.09	3019.00	811.21
323.09	4014.00	811.83
323.09	5006.00	812.47
323.09	6012.00	813.18
323.09	7002.00	813.8
323.09	8003.00	814.42
323.09	9008.00	815.1
323.09	10006.00	815.7
323.09	11000.00	816.38
323.09	12002.00	816.97
323.09	13002.00	817.64
323.09	14000.00	818.21
323.09	15017.00	818.84
323.09	16003.00	819.4
323.09	17015.00	820.02
323.09	18006.00	820.61
323.09	19007.00	821.24
323.09	20007.00	821.84
323.09	21002.00	822.41
323.09	22014.00	823.01
333.04	1046.00	802.82
333.04	2018.00	803.5
333.04	3008.00	804.21
333.04	4012.00	804.88
333.04	5059.00	805.62
333.04	6016.00	806.29
333.04	7022.00	807.0
333.04	8014.00	807.64
333.04	9015.00	808.34
333.04	10015.00	808.97
333.04	11019.00	809.64
333.04	12007.00	810.31
333.04	13019.00	810.96
333.04	14019.00	811.6
333.04	15014.00	812.24
333.04	16021.00	812.88
333.04	17026.00	813.5
333.04	18023.00	814.11
333.04	19018.00	814.72
333.04	20025.00	815.35
333.04	21020.00	815.94
333.04	22032.00	816.58
342.98	1058.00	795.63
342.98	2045.00	796.4
342.98	3022.00	797.12
342.98	4035.00	797.9
342.98	5028.00	798.63
342.98	6030.00	799.37
342.98	7023.00	800.07
342.98	8028.00	800.78
342.98	9062.00	801.51
342.98	10035.00	802.22
342.98	11029.00	802.92
342.98	12064.00	803.64
342.98	13023.00	804.31
342.98	14042.00	805.0
342.98	15022.00	805.66
342.98	16022.00	806.36
342.98	17021.00	807.0
342.98	18034.00	807.7
342.98	19025.00	808.35
342.98	20038.00	808.98
342.98	21018.00	809.62
342.98	22035.00	810.28
352.86	1069.00	788.44
352.86	2043.00	789.24
352.86	3040.00	790.04
352.86	4048.00	790.78
352.86	5038.00	791.59
352.86	6043.00	792.34
352.86	7038.00	793.09
352.86	8039.00	793.84
352.86	9040.00	794.57
352.86	10038.00	795.32
352.86	11032.00	796.04
352.86	12032.00	796.74
352.86	13040.00	797.47
352.86	14046.00	798.18
352.86	15043.00	798.89
352.86	16037.00	799.59
352.86	17040.00	800.26
352.86	18046.00	800.95
352.86	19040.00	801.63
352.86	20064.00	802.32
352.86	21048.00	802.96
352.86	22049.00	803.62
362.89	1077.00	781.02
362.89	2027.00	781.83
362.89	3089.00	782.69
362.89	4047.00	783.49
362.89	5061.00	784.29
362.89	6060.00	785.12
362.89	7041.00	785.91
362.89	8049.00	786.7
362.89	9049.00	787.47
362.89	10052.00	788.25
362.89	11045.00	788.99
362.89	12044.00	789.75
362.89	13054.00	790.54
362.89	14053.00	791.25
362.89	15052.00	792.0
362.89	16056.00	792.77
362.89	17063.00	793.47
362.89	18062.00	794.2
362.89	19062.00	794.91
362.89	20068.00	795.64
362.89	21072.00	796.35
362.89	22063.00	797.03
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[390.26; 531.78]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.62798e+01
Coefficient B			-4.94119e+03
Coefficient C			-8.12810e+01
Temperature range, min.			390.26
Temperature range, max.			531.78
Pvap	1.33	kPa	390.26	Calculated Property
Pvap	2.89	kPa	405.98	Calculated Property
Pvap	5.84	kPa	421.71	Calculated Property
Pvap	11.09	kPa	437.43	Calculated Property
Pvap	19.94	kPa	453.16	Calculated Property
Pvap	34.18	kPa	468.88	Calculated Property
Pvap	56.19	kPa	484.61	Calculated Property
Pvap	88.98	kPa	500.33	Calculated Property
Pvap	136.30	kPa	516.06	Calculated Property
Pvap	202.67	kPa	531.78	Calculated Property
Pvap	[1.20e-04; 2421.30]	kPa	[280.05; 690.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			2.35419e+02
Coefficient B			-1.88148e+04
Coefficient C			-3.16474e+01
Coefficient D			1.36741e-05
Temperature range, min.			280.05
Temperature range, max.			690.00
Pvap	1.20e-04	kPa	280.05	Calculated Property
Pvap	0.02	kPa	325.60	Calculated Property
Pvap	0.53	kPa	371.15	Calculated Property
Pvap	5.66	kPa	416.70	Calculated Property
Pvap	31.38	kPa	462.25	Calculated Property
Pvap	112.99	kPa	507.80	Calculated Property
Pvap	304.78	kPa	553.35	Calculated Property
Pvap	678.49	kPa	598.90	Calculated Property
Pvap	1332.65	kPa	644.45	Calculated Property
Pvap	2421.30	kPa	690.00	Calculated Property

Similar Compounds

Find more compounds similar to 1-Decanol.

Mixtures

• Benzene, 1-chloro-2-methyl- + 1-Decanol
• Benzene, 1-chloro-3-methyl- + 1-Decanol
• 1-Decanol + Benzene, 1-chloro-4-methyl-
• 1-Octene + 1-Decanol
• Pentanoic acid, 4-oxo- + 1-Decanol + Water
• Cholesterol + 1-Decanol
• Cholesterol + 1-Decanol + Cyclohexane
• Tributyl phosphate + 1-Decanol
• 1-Octanol + 1-Decanol
• Tridodecylamine + 1-Decanol
• Thymol + 1-Decanol
• 1-Decanol + Cyclohexane
• Tripalmitin + 1-Decanol
• Butane, 1-chloro- + 1-Decanol
• Ethane, 1,1,2,2-tetrabromo- + 1-Decanol
• 1-Decanol + Ethane, 1,1,2,2-tetrachloro-
• Heptane + 1-Decanol
• 1-Decanol + Propanoic acid + Water
• n-Butyl ether + 1-Decanol
• Lactic acid + 1-Decanol + Water

Find more mixtures with 1-Decanol.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 1-Decanol with Isomeric Chlorotoluenes
• Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
• The co-solubility of 2-ethylhexanoic acid and some liquid alcohols in supercritical carbon dioxide
• Phase behaviour of I-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium based ionic liquids with alcohols, water, ketones and hydrocarbons: The effect of cation and anion on solubility
• Phase equilibria of high molecular mass 1-alcohols in supercritical propane
• Excess molar enthalpy of 1-alkanol + 1-octene mixtures at 298.15K Experimental results and theoretical description by means of the ERAS and TB models
• Phase equilibria of (water + levunilic acid + alcohol) ternary systems
• (Solid + liquid) and (liquid + liquid) phase equilibria measurements and correlation of the binary systems {tri-iso-butyl(methyl)phosphonium tosylate + alcohol, or +hydrocarbon}
• Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
• (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
• SLE and LLE for tri-butylphosphate or tri-octylamine contained systems; extractive solvents of Molybdenum
• The solid-liquid phase diagrams of binary mixtures of even saturated fatty alcohols
• Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
• Solid-liquid equilibrium, excess molar volume, and deviations in the molar refractivity for the binary and ternary mixtures of Alamine 304-1 with 1-octanol, 2-octanol, and 1-decanol
• Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
• Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
• Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
• Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
• High pressure phase behaviour of the CO2 + 1-decanol + n-dodecane system
• (Solid + liquid) equilibrium phase diagrams in binary mixtures containing terpenes: New experimental data and analysis of several modelling strategies with modified UNIFAC (Dortmund) and PC-SAFT equation of state
• Reactive extraction of pimelic (heptanedioic) acid from dilute aqueous solutions using trioctylamine in decan-1-ol
• The behavior of mercury in water, alcohols, monoethylene glycol and triethylene glycol II. Elemental mercury solubility in alcohols, ethers and acetone; gas plant mercury distribution; and speciation in monoethylene glycol solution
• Measurement and modelling of high pressure bubble- and dew-point data for the CO2 + 1-decanol + 3,7-dimethyl-1-octanol system
• Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
• Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
• Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
• Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
• (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
• Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
• (Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
• Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
• (Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems
• Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
• Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of diethylene glycol monomethyl ether with 1-alkanols at temperatures from (293.15 to 308.15) K
• Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
• Measurement and correlation of the excess molar enthalpy of (1-nonanol, or 1-decanol + acetonitrile) mixtures at (298.15, 303.15, and 308.15) K and atmospheric pressure
• PrhoT measurements and derived properties of liquid 1-alkanols
• Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
• Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures
• Phase equilibria of ternary systems (water + pyruvic acid + high boiling alcohol). Thermodynamic modeling and optimization of extraction
• Physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol at different temperatures
• Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
• Thermodynamics of 1-alkanol + linear polyether mixtures
• Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
• Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
• Densities, speeds of sound and viscosities of binary mixtures of tetrahydrofuran with 1-hexanol, 1-octanol and 1-decanol at T = (298.15 to 313.15) K
• Effect of temperature and chain length on the viscosity and surface tension of binary systems of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol
• Thermodynamics of mixtures with strongly negative deviations from Raoult s law. XII. Densities, viscosities and refractive indices at T = (293.15 to 303.15) K for (1-heptanol, or 1-decanol + cyclohexylamine) systems. Application of the ERAS model to (1-alkanol + cyclohexylamine) mixtures
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
• Optimization and modeling of extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solvent)
• Studies on the importance of chain length of alkanols on the thermodynamic and transport properties of liquid mixtures at various temperatures
• Super- and near-critical fluid phase behavior and phenomena of the ternary system CO2 + 1-decanol + n-tetradecane
• FT-IR studies and excess thermodynamic properties of binary liquid mixtures 2-(2-butoxyethoxy) ethanol with 1-hexanol, 1-octanol and 1-decanol at different temperatures
• Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
• Temperature and composition dependence of the density and viscosity of binary mixtures of (1-decanol + fragrance material)
• Measurement and correlation of tie-line data in ternary aqueous mixtures of 1,3-butanediol with decanol at different temperatures
• Tie-line data for water- formic acid-1-decanol ternary system at T = (298.2, 303.2, 313.2, 323.2) K
• Solubility and Tie Line Data of the Water - Phosphoric Acid Solvents at T = (303.2 and 313.2) K: An Experimental and Correlational Study
• Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
• Thermodynamics of mixtures containing amines. XVI. CE pm of 1-butanol, 1-octanol or 1-decanol + benzylamine systems at (298.15, 308.15, 318.15 and 333.15) K
• Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
• The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
• Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
• Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
• Extraction of Citric Acid and Maleic Acid from Their Aqueous Solutions Using a Phosphorus-Bonded Extractant, Tri-n-octylphosphineoxide, and a Secondary Amine, Dioctylamine
• Experimental Data of Citric Acid Extraction from Aqueous Solution with 1-Decanol by Using Liquid-Liquid Equilibrium
• Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
• Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
• Twenty Years of Experimental Determinations of Thermophysical Properties with High Accuracy: Thermodynamics Laboratory, ESIQIE-IPN, Mexico
• Comparison of Extractability of Oxalic Acid from Dilute Aqueous Solutions Using Dioctylamine and Trioctylphosphine Oxide
• Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
• Thermodynamic Properties of 1-Hexyl-3-methylimidazolium Nitrate and 1-Alkanols Mixtures: PC-SAFT Model
• Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
• Experimental Solid + Liquid Equilibria and Excess Molar Volume of Alkanol + Octylamine Mixtures. Analysis in Terms of ERAS, DISQUAC, and Modified UNIFAC
• Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K
• Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
• Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
• Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Octan-1-ol and Decan-1-ol at (303.15 and 313.15) K
• Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
• Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
• Vapor-Liquid Equilibria of Binary Systems of Ethene Oxide + Dodecane, Ethene Oxide + 1-Decanol, and Ethene Oxide + 1-Dodecanol and Prediction with the Predictive Soave-Redlich-Kwong (PSRK) Equation of State
• Liquid-Liquid Phase Behavior of Solutions of 1-Dodecyl-3-methylimidazolium Bis(trifluoromethylsulphonyl)imide (C12mimNTf2) in n- Alkyl Alcohols
• Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
• Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
• Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
• Influence of the Temperature on the Liquid-Liquid-Solid Equilibria of the Ternary System Water + Ethanol + 1-Decanol
• Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
• Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
• Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
• Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
• Phase Equilibria of the Carbon Dioxide + 1-Decanol System at High Pressures
• Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
• Solubility Determination and Correlation of (2R,3S,4S,5S)-6-(Hydroxymethyl)-tetrahydro-2H-pyran-2,3,4, 5-tetraol in Fatty Alcohol
• Densities, Isothermal Compressibilities, and Isobaric Thermal Expansivities of Hexan-2-ol, Octan-1-ol, and Decan-1-ol from (313 to 363) K and Pressures up to 22 MPa
• Study of a Binary Liquid Mixture of Diethylamine and 1-Decanol and Validation of Theoretical Approaches of Sound Speed at Different Temperatures
• Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
• Experimental and Theoretical Study of the Phase Equilibria in Ternary Aqueous Mixtures of 1,4-Butanediol with Alcohols at 298.2 K
• Volumetric and Viscometric Properties of Binary Liquid Mixtures of Ethylene Glycol Monomethyl Ether + 1-Hexanol, 1-Octanol, and 1-Decanol at Temperatures of T = (293.15, 298.15, 303.15, and 308.15) K
• Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum
• Liquid-Liquid Phase Behavior of Solutions of 1-Octyl- and 1-Decyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide (C8,10mimNTf2) in n-Alkyl Alcohols
• Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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