Chemical Properties of Dodecane (CAS 112-40-3)

InChI

InChI=1S/C12H26/c1-3-5-7-9-11-12-10-8-6-4-2/h3-12H2,1-2H3

InChI Key

SNRUBQQJIBEYMU-UHFFFAOYSA-N

Formula

C12H26

SMILES

CCCCCCCCCCCC

Molecular Weight¹

170.33

CAS

112-40-3

Other Names

• Adakane 12
• BIHEXYL
• Ba 51-090453
• CH3(CH2)10CH3
• Dihexyl
• Duodecane
• NSC 8714
• n-Dodecane

• ω : Acentric Factor.
• 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).
• 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_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.
• D^*_i : Self diffusion coefficient (m²/s).
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• 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 : Liquid thermal conductivity (W/m×K).
• α_diff : Thermal diffusivity (m²/s).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	0.5750		KDB
ΔcH°liquid	[-8090.60; -7901.74]	kJ/mol
ΔcH°liquid	-7901.74	kJ/mol	NIST
ΔcH°liquid	-8086.00 ± 1.20	kJ/mol	NIST
ΔcH°liquid	-8083.20	kJ/mol	NIST
ΔcH°liquid	-8090.60 ± 7.90	kJ/mol	NIST
μ	0.00	debye	KDB
ΔfG°	50.07	kJ/mol	KDB
ΔfH°gas	[-291.10; -288.10]	kJ/mol
ΔfH°gas	-291.10	kJ/mol	KDB
ΔfH°gas	-290.90 ± 1.40	kJ/mol	NIST
ΔfH°gas	-288.10 ± 3.30	kJ/mol	NIST
ΔfH°liquid	[-352.10; -349.30]	kJ/mol
ΔfH°liquid	-352.10 ± 1.40	kJ/mol	NIST
ΔfH°liquid	-349.30 ± 3.20	kJ/mol	NIST
ΔfusH°	26.84	kJ/mol	Joback Calculated Property
ΔsubH°	100.20	kJ/mol	NIST
ΔvapH°	42.31	kJ/mol	Joback Calculated Property
log10WS	-4.85		Crippen Calculated Property
logPoct/wat	4.927		Crippen Calculated Property
McVol	179.940	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
Pc	[1800.00; 1860.00]	kPa
Pc	1820.00	kPa	KDB
Pc	1800.00 ± 100.00	kPa	NIST
Pc	1810.00 ± 20.00	kPa	NIST
Pc	1834.00	kPa	NIST
Pc	1860.00 ± 13.78	kPa	NIST
Pc	1824.00 ± 10.00	kPa	NIST
ρc	[221.44; 226.55]	kg/m3
ρc	221.44 ± 17.03	kg/m3	NIST
ρc	226.55 ± 6.81	kg/m3	NIST
Inp	[200.12; 209.90]
Inp	200.12		NIST
Inp	202.83		NIST
Inp	209.90		NIST
S°gas	622.50	J/mol×K	NIST
S°liquid	[490.66; 497.10]	J/mol×K
S°liquid	490.66	J/mol×K	NIST
S°liquid	497.10	J/mol×K	NIST
Tboil	[479.15; 489.47]	K
Tboil	489.47	K	KDB
Tboil	479.15	K	Determi...
Tc	658.00	K	KDB
Tfus	[263.50; 264.95]	K
Tfus	263.50	K	KDB
Tfus	263.70	K	Determi...
Tfus	264.95	K	Density...
Vc	[0.754; 0.754]	m3/kmol
Vc	0.754	m3/kmol	KDB
Vc	0.754	m3/kmol	NIST
Zc	0.2508300		KDB
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[406.83; 498.37]	J/mol×K	[473.96; 634.98]
Cp,gas	406.83	J/mol×K	473.96	Joback Calculated Property
Cp,gas	423.59	J/mol×K	500.80	Joback Calculated Property
Cp,gas	439.73	J/mol×K	527.63	Joback Calculated Property
Cp,gas	455.26	J/mol×K	554.47	Joback Calculated Property
Cp,gas	470.20	J/mol×K	581.30	Joback Calculated Property
Cp,gas	484.57	J/mol×K	608.14	Joback Calculated Property
Cp,gas	498.37	J/mol×K	634.98	Joback Calculated Property
Cp,liquid	[368.47; 388.29]	J/mol×K	[283.15; 323.15]
Cp,liquid	368.47	J/mol×K	283.15	Heat Ca...
Cp,liquid	371.38	J/mol×K	288.15	Thermod...
Cp,liquid	370.48	J/mol×K	288.15	Heat Ca...
Cp,liquid	372.74	J/mol×K	293.15	Heat Ca...
Cp,liquid	371.10	J/mol×K	297.70	NIST
Cp,liquid	374.50	J/mol×K	298.00	NIST
Cp,liquid	375.26	J/mol×K	298.15	NIST
Cp,liquid	370.72	J/mol×K	298.15	NIST
Cp,liquid	374.82	J/mol×K	298.15	NIST
Cp,liquid	375.93	J/mol×K	298.15	NIST
Cp,liquid	375.94	J/mol×K	298.15	Thermod...
Cp,liquid	374.93	J/mol×K	298.15	NIST
Cp,liquid	375.30	J/mol×K	298.15	NIST
Cp,liquid	376.00	J/mol×K	298.15	NIST
Cp,liquid	372.12	J/mol×K	298.15	NIST
Cp,liquid	375.04	J/mol×K	298.15	Heat Ca...
Cp,liquid	376.09	J/mol×K	298.15	NIST
Cp,liquid	376.00	J/mol×K	298.15	NIST
Cp,liquid	375.37	J/mol×K	298.15	NIST
Cp,liquid	376.00	J/mol×K	298.15	NIST
Cp,liquid	373.30	J/mol×K	298.15	NIST
Cp,liquid	376.91	J/mol×K	298.15	NIST
Cp,liquid	373.30	J/mol×K	298.15	NIST
Cp,liquid	376.46	J/mol×K	298.15	NIST
Cp,liquid	377.43	J/mol×K	303.15	Heat Ca...
Cp,liquid	380.02	J/mol×K	308.15	Heat Ca...
Cp,liquid	380.92	J/mol×K	308.15	Thermod...
Cp,liquid	382.73	J/mol×K	313.15	Heat Ca...
Cp,liquid	385.48	J/mol×K	318.15	Heat Ca...
Cp,liquid	386.31	J/mol×K	318.15	Thermod...
Cp,liquid	388.29	J/mol×K	323.15	Heat Ca...
η	[0.0000551; 0.0015800]	Pa×s	[288.15; 673.20]
η	0.0015800	Pa×s	288.15	Physica...
η	0.0014540	Pa×s	293.15	Dynamic...
η	0.0014540	Pa×s	293.15	Dynamic...
η	0.0014700	Pa×s	293.15	Physica...
η	0.0013270	Pa×s	298.15	Dynamic...
η	0.0013500	Pa×s	298.15	Physica...
η	0.0013270	Pa×s	298.15	Dynamic...
η	0.0013360	Pa×s	298.15	Densiti...
η	0.0012190	Pa×s	303.15	Dynamic...
η	0.0012400	Pa×s	303.15	Physica...
η	0.0012190	Pa×s	303.15	Dynamic...
η	0.0012210	Pa×s	303.15	Densiti...
η	0.0013335	Pa×s	303.20	Viscosi...
η	0.0011400	Pa×s	308.15	Physica...
η	0.0011250	Pa×s	308.15	Densiti...
η	0.0010600	Pa×s	313.15	Physica...
η	0.0010390	Pa×s	313.15	Densiti...
η	0.0011221	Pa×s	313.20	Viscosi...
η	0.0009650	Pa×s	318.15	Densiti...
η	0.0009900	Pa×s	318.15	Physica...
η	0.0009700	Pa×s	323.00	Viscosi...
η	0.0008980	Pa×s	323.15	Densiti...
η	0.0009300	Pa×s	323.15	Physica...
η	0.0009225	Pa×s	323.15	Liquid ...
η	0.0008700	Pa×s	328.15	Physica...
η	0.0008430	Pa×s	328.15	Densiti...
η	0.0008519	Pa×s	333.10	Viscosi...
η	0.0008200	Pa×s	333.15	Physica...
η	0.0007442	Pa×s	343.30	Viscosi...
η	0.0006763	Pa×s	348.15	Liquid ...
η	0.0006736	Pa×s	353.30	Viscosi...
η	0.0006075	Pa×s	363.20	Viscosi...
η	0.0005070	Pa×s	373.15	Liquid ...
η	0.0005467	Pa×s	373.30	Viscosi...
η	0.0004902	Pa×s	383.20	Viscosi...
η	0.0004472	Pa×s	393.20	Viscosi...
η	0.0004003	Pa×s	398.15	Liquid ...
η	0.0004112	Pa×s	403.20	Viscosi...
η	0.0003785	Pa×s	413.20	Viscosi...
η	0.0003223	Pa×s	423.15	Liquid ...
η	0.0003508	Pa×s	423.20	Viscosi...
η	0.0003277	Pa×s	433.20	Viscosi...
η	0.0002974	Pa×s	443.40	Viscosi...
η	0.0002595	Pa×s	448.15	Liquid ...
η	0.0002822	Pa×s	453.10	Viscosi...
η	0.0002604	Pa×s	463.20	Viscosi...
η	0.0002156	Pa×s	473.15	Liquid ...
η	0.0002440	Pa×s	473.20	Viscosi...
η	0.0002250	Pa×s	483.10	Viscosi...
η	0.0002250	Pa×s	483.10	Viscosi...
η	0.0002076	Pa×s	493.20	Viscosi...
η	0.0001821	Pa×s	498.15	Liquid ...
η	0.0001964	Pa×s	503.20	Viscosi...
η	0.0001846	Pa×s	513.10	Viscosi...
η	0.0001532	Pa×s	523.15	Liquid ...
η	0.0001722	Pa×s	523.20	Viscosi...
η	0.0001608	Pa×s	533.10	Viscosi...
η	0.0001489	Pa×s	543.20	Viscosi...
η	0.0001277	Pa×s	548.15	Liquid ...
η	0.0001375	Pa×s	553.20	Viscosi...
η	0.0001297	Pa×s	563.20	Viscosi...
η	0.0001051	Pa×s	573.15	Liquid ...
η	0.0001201	Pa×s	573.20	Viscosi...
η	0.0001126	Pa×s	583.30	Viscosi...
η	0.0001031	Pa×s	593.20	Viscosi...
η	0.0000974	Pa×s	603.20	Viscosi...
η	0.0000913	Pa×s	613.20	Viscosi...
η	0.0000839	Pa×s	623.10	Viscosi...
η	0.0000767	Pa×s	633.20	Viscosi...
η	0.0000694	Pa×s	643.10	Viscosi...
η	0.0000657	Pa×s	653.20	Viscosi...
η	0.0000605	Pa×s	663.20	Viscosi...
η	0.0000551	Pa×s	673.20	Viscosi...
η	0.0000551	Pa×s	673.20	Viscosi...
ΔfusH	[35.70; 36.84]	kJ/mol	[263.10; 263.60]
ΔfusH	35.70	kJ/mol	263.10	NIST
ΔfusH	36.58	kJ/mol	263.50	NIST
ΔfusH	36.84	kJ/mol	263.59	NIST
ΔfusH	36.82	kJ/mol	263.60	NIST
ΔfusH	36.82	kJ/mol	263.60	NIST
ΔsubH	101.70	kJ/mol	263.00	NIST
ΔvapH	[43.64; 65.70]	kJ/mol	[299.00; 488.60]
ΔvapH	61.40	kJ/mol	299.00	NIST
ΔvapH	65.70	kJ/mol	317.00	NIST
ΔvapH	58.10	kJ/mol	334.00	NIST
ΔvapH	61.80	kJ/mol	339.00	NIST
ΔvapH	61.10	kJ/mol	343.50	NIST
ΔvapH	57.40	kJ/mol	344.00	NIST
ΔvapH	51.60	kJ/mol	446.00	NIST
ΔvapH	43.64	kJ/mol	488.60	KDB
Pvap	[4.21e-03; 241.00]	kPa	[284.15; 509.15]
Pvap	4.21e-03	kPa	284.15	Determi...
Pvap	6.46e-03	kPa	289.15	Determi...
Pvap	9.78e-03	kPa	294.15	Determi...
Pvap	0.01	kPa	299.15	Determi...
Pvap	0.02	kPa	304.15	Determi...
Pvap	0.03	kPa	309.15	Determi...
Pvap	0.06	kPa	313.15	Vapor-L...
Pvap	0.06	kPa	313.15	Vapor L...
Pvap	0.04	kPa	314.15	Determi...
Pvap	0.06	kPa	319.15	Determi...
Pvap	0.20	kPa	323.15	Isother...
Pvap	0.09	kPa	324.15	Determi...
Pvap	0.12	kPa	329.15	Determi...
Pvap	0.17	kPa	334.15	Determi...
Pvap	0.23	kPa	339.15	Determi...
Pvap	0.36	kPa	342.18	P-x dat...
Pvap	0.40	kPa	343.15	Bubble ...
Pvap	0.32	kPa	344.15	Determi...
Pvap	0.42	kPa	349.15	Determi...
Pvap	0.75	kPa	352.68	P-x dat...
Pvap	0.70	kPa	353.15	Bubble ...
Pvap	0.56	kPa	354.15	Determi...
Pvap	0.75	kPa	359.15	Determi...
Pvap	1.20	kPa	363.15	Bubble ...
Pvap	0.98	kPa	364.15	Determi...
Pvap	1.27	kPa	369.15	Determi...
Pvap	2.00	kPa	373.15	Bubble ...
Pvap	1.64	kPa	374.15	Determi...
Pvap	2.10	kPa	379.15	Determi...
Pvap	3.20	kPa	383.15	Bubble ...
Pvap	2.67	kPa	384.15	Determi...
Pvap	3.38	kPa	389.15	Determi...
Pvap	4.90	kPa	393.15	Bubble ...
Pvap	4.25	kPa	394.15	Determi...
Pvap	5.32	kPa	399.15	Determi...
Pvap	6.62	kPa	404.15	Determi...
Pvap	8.19	kPa	409.15	Determi...
Pvap	10.10	kPa	414.15	Determi...
Pvap	12.40	kPa	419.15	Determi...
Pvap	15.10	kPa	424.15	Determi...
Pvap	18.30	kPa	429.15	Determi...
Pvap	20.90	kPa	432.23	Isobari...
Pvap	22.10	kPa	434.15	Determi...
Pvap	26.60	kPa	439.15	Determi...
Pvap	31.80	kPa	444.15	Determi...
Pvap	31.00	kPa	444.86	Isobari...
Pvap	38.00	kPa	449.15	Determi...
Pvap	40.00	kPa	453.92	Low-Pre...
Pvap	40.08	kPa	453.92	Low-Pre...
Pvap	45.10	kPa	454.15	Determi...
Pvap	42.70	kPa	455.87	Isobari...
Pvap	43.58	kPa	456.87	Low-Pre...
Pvap	53.40	kPa	459.15	Determi...
Pvap	46.71	kPa	459.31	Low-Pre...
Pvap	49.93	kPa	461.72	Low-Pre...
Pvap	50.80	kPa	462.05	Isobari...
Pvap	63.00	kPa	464.15	Determi...
Pvap	55.35	kPa	465.47	Low-Pre...
Pvap	58.41	kPa	467.52	Low-Pre...
Pvap	74.10	kPa	469.15	Determi...
Pvap	62.30	kPa	469.67	Isobari...
Pvap	63.63	kPa	470.69	Low-Pre...
Pvap	86.80	kPa	474.15	Determi...
Pvap	70.20	kPa	474.19	Isobari...
Pvap	69.97	kPa	474.33	Low-Pre...
Pvap	77.75	kPa	478.47	Low-Pre...
Pvap	101.00	kPa	479.15	Determi...
Pvap	81.00	kPa	479.82	Isobari...
Pvap	118.00	kPa	484.15	Determi...
Pvap	90.80	kPa	484.34	Isobari...
Pvap	100.60	kPa	488.50	Isobari...
Pvap	137.00	kPa	489.15	Determi...
Pvap	158.00	kPa	494.15	Determi...
Pvap	183.00	kPa	499.15	Determi...
Pvap	210.00	kPa	504.15	Determi...
Pvap	241.00	kPa	509.15	Determi...
n0	[1.40018; 1.42750]		[293.10; 343.15]
n0	1.42200		293.10	Extract...
n0	1.42200		293.10	Phase e...
n0	1.42210		293.10	Extract...
n0	1.42200		293.10	Evaluat...
n0	1.42200		293.10	Liquid ...
n0	1.41920		293.15	Isother...
n0	1.42155		293.15	Liquid ...
n0	1.42100		293.15	Activit...
n0	1.42180		293.15	Experim...
n0	1.42218		293.15	Thermod...
n0	1.42100		293.15	Physica...
n0	1.42180		293.15	Vapor L...
n0	1.41860		298.15	Excess ...
n0	1.41920		298.15	Correla...
n0	1.42011		298.15	(Liquid...
n0	1.42011		298.15	Thiophe...
n0	1.41960		298.15	Liquid ...
n0	1.41720		298.15	Physica...
n0	1.42750		298.15	Liquid-...
n0	1.42750		298.15	Liquid-...
n0	1.41970		298.15	Measure...
n0	1.41970		298.15	Thermod...
n0	1.41960		298.20	Liquid-...
n0	1.41640		303.15	Excess ...
n0	1.41810		303.15	Liquid ...
n0	1.41350		303.15	Physica...
n0	1.41784		303.15	Thermod...
n0	1.41400		308.15	Excess ...
n0	1.41346		313.15	Thermod...
n0	1.41310		313.20	Liquid-...
n0	1.40914		323.15	Thermod...
n0	1.40479		333.15	Thermod...
n0	1.40018		343.15	Thermod...
ρl	[610.60; 752.44]	kg/m3	[288.15; 473.15]
ρl	752.35	kg/m3	288.15	Thermop...
ρl	752.44	kg/m3	288.15	Permitt...
ρl	752.41	kg/m3	288.15	Densiti...
ρl	748.00	kg/m3	293.00	KDB
ρl	748.73	kg/m3	293.15	Densiti...
ρl	748.83	kg/m3	293.15	Densiti...
ρl	748.72	kg/m3	293.15	Thermop...
ρl	748.79	kg/m3	293.15	Density...
ρl	748.83	kg/m3	293.15	Densiti...
ρl	748.80	kg/m3	293.15	Permitt...
ρl	748.79	kg/m3	293.15	Densiti...
ρl	749.00	kg/m3	293.15	Excess ...
ρl	748.81	kg/m3	293.15	Thermop...
ρl	748.89	kg/m3	293.15	Density...
ρl	745.38	kg/m3	298.15	Excess ...
ρl	745.28	kg/m3	298.15	Excess ...
ρl	745.38	kg/m3	298.15	Excess ...
ρl	745.38	kg/m3	298.15	Excess ...
ρl	745.52	kg/m3	298.15	Thermod...
ρl	745.28	kg/m3	298.15	Excess ...
ρl	745.27	kg/m3	298.15	Water/o...
ρl	745.20	kg/m3	298.15	(Liquid...
ρl	745.62	kg/m3	298.15	Thermod...
ρl	745.32	kg/m3	298.15	Solvent...
ρl	745.21	kg/m3	298.15	Binary ...
ρl	745.82	kg/m3	298.15	Solid L...
ρl	741.54	kg/m3	298.15	Thermod...
ρl	741.54	kg/m3	298.15	Thermod...
ρl	745.38	kg/m3	298.15	Excess ...
ρl	745.41	kg/m3	298.15	Mutual ...
ρl	745.32	kg/m3	298.15	Excess ...
ρl	745.19	kg/m3	298.15	Permitt...
ρl	745.52	kg/m3	298.15	Thermod...
ρl	745.09	kg/m3	298.15	Thermop...
ρl	745.28	kg/m3	298.15	Study o...
ρl	745.51	kg/m3	298.15	Liquid ...
ρl	745.22	kg/m3	298.15	Densiti...
ρl	741.52	kg/m3	298.15	Liquid ...
ρl	745.11	kg/m3	298.15	Densiti...
ρl	745.28	kg/m3	298.15	Excess ...
ρl	741.54	kg/m3	298.15	Liquid-...
ρl	747.00	kg/m3	298.15	Ternary...
ρl	745.52	kg/m3	298.15	Liquid-...
ρl	745.23	kg/m3	298.15	Densiti...
ρl	741.54	kg/m3	298.15	Thermod...
ρl	745.51	kg/m3	298.15	Liquid-...
ρl	745.16	kg/m3	298.15	Densiti...
ρl	746.60	kg/m3	298.20	Ternary...
ρl	745.15	kg/m3	298.20	Apparen...
ρl	741.57	kg/m3	303.15	Permitt...
ρl	741.77	kg/m3	303.15	Densiti...
ρl	741.75	kg/m3	303.15	Excess ...
ρl	741.53	kg/m3	303.15	Densiti...
ρl	741.98	kg/m3	303.15	Thermod...
ρl	741.42	kg/m3	303.15	Thermop...
ρl	741.63	kg/m3	303.15	Density...
ρl	741.54	kg/m3	303.15	Density...
ρl	741.60	kg/m3	303.15	Densiti...
ρl	741.59	kg/m3	303.15	Densiti...
ρl	741.46	kg/m3	303.15	Thermop...
ρl	737.97	kg/m3	308.15	Densiti...
ρl	738.34	kg/m3	308.15	Thermod...
ρl	737.93	kg/m3	308.15	Permitt...
ρl	737.95	kg/m3	308.15	Densiti...
ρl	738.12	kg/m3	308.15	Excess ...
ρl	734.08	kg/m3	313.15	Thermop...
ρl	734.33	kg/m3	313.15	Densiti...
ρl	734.35	kg/m3	313.15	Density...
ρl	734.25	kg/m3	313.15	Density...
ρl	734.48	kg/m3	313.15	Excess ...
ρl	734.87	kg/m3	313.15	Densiti...
ρl	734.18	kg/m3	313.15	Thermop...
ρl	734.25	kg/m3	313.15	Densiti...
ρl	734.31	kg/m3	313.15	Densiti...
ρl	734.19	kg/m3	313.15	Thermop...
ρl	734.69	kg/m3	313.15	Thermod...
ρl	734.33	kg/m3	313.20	Apparen...
ρl	730.70	kg/m3	318.15	Permitt...
ρl	730.68	kg/m3	318.15	Densiti...
ρl	730.66	kg/m3	318.15	Densiti...
ρl	731.03	kg/m3	318.15	Thermod...
ρl	726.74	kg/m3	323.15	Thermop...
ρl	727.01	kg/m3	323.15	Densiti...
ρl	726.88	kg/m3	323.15	Densiti...
ρl	726.94	kg/m3	323.15	Density...
ρl	726.94	kg/m3	323.15	Densiti...
ρl	727.37	kg/m3	323.15	Thermod...
ρl	726.88	kg/m3	323.15	Thermop...
ρl	727.00	kg/m3	323.15	Densiti...
ρl	727.04	kg/m3	323.15	Density...
ρl	723.33	kg/m3	328.15	Densiti...
ρl	723.32	kg/m3	328.15	Permitt...
ρl	723.35	kg/m3	328.15	Densiti...
ρl	719.53	kg/m3	333.15	Thermop...
ρl	719.69	kg/m3	333.15	Density...
ρl	719.38	kg/m3	333.15	Thermop...
ρl	719.59	kg/m3	333.15	Densiti...
ρl	719.67	kg/m3	333.15	Densiti...
ρl	719.59	kg/m3	333.15	Density...
ρl	719.65	kg/m3	333.15	Densiti...
ρl	719.53	kg/m3	333.15	Densiti...
ρl	715.98	kg/m3	338.15	Densiti...
ρl	712.20	kg/m3	343.15	Density...
ρl	712.20	kg/m3	343.15	Density...
ρl	712.28	kg/m3	343.15	Densiti...
ρl	711.32	kg/m3	343.15	Thermop...
ρl	712.10	kg/m3	344.15	High-pr...
ρl	704.62	kg/m3	353.15	Thermop...
ρl	704.70	kg/m3	353.15	Density...
ρl	697.10	kg/m3	363.15	Density...
ρl	697.21	kg/m3	363.15	Thermop...
ρl	689.60	kg/m3	373.15	Density...
ρl	689.75	kg/m3	373.15	Thermop...
ρl	682.25	kg/m3	383.15	Thermop...
ρl	674.68	kg/m3	393.15	Thermop...
ρl	667.04	kg/m3	403.15	Thermop...
ρl	659.32	kg/m3	413.15	Thermop...
ρl	651.53	kg/m3	423.15	Thermop...
ρl	643.60	kg/m3	433.15	Thermop...
ρl	635.55	kg/m3	443.15	Thermop...
ρl	627.38	kg/m3	453.15	Thermop...
ρl	619.09	kg/m3	463.15	Thermop...
ρl	610.60	kg/m3	473.15	Thermop...
D*i	[0.00; 0.00]	m2/s	[264.14; 364.54]
D*i	0.00	m2/s	264.14	Viscous...
D*i	0.00	m2/s	266.50	Viscous...
D*i	0.00	m2/s	268.03	Viscous...
D*i	0.00	m2/s	278.20	Viscous...
D*i	0.00	m2/s	278.52	Viscous...
D*i	0.00	m2/s	278.56	Viscous...
D*i	0.00	m2/s	278.72	Viscous...
D*i	0.00	m2/s	288.09	Viscous...
D*i	0.00	m2/s	288.49	Viscous...
D*i	0.00	m2/s	288.52	Viscous...
D*i	0.00	m2/s	298.15	Viscous...
D*i	0.00	m2/s	298.20	Viscous...
D*i	0.00	m2/s	298.21	Viscous...
D*i	0.00	m2/s	308.15	Viscous...
D*i	0.00	m2/s	308.16	Viscous...
D*i	0.00	m2/s	318.15	Viscous...
D*i	0.00	m2/s	318.16	Viscous...
D*i	0.00	m2/s	323.17	Viscous...
D*i	0.00	m2/s	328.17	Viscous...
D*i	0.00	m2/s	328.22	Viscous...
D*i	0.00	m2/s	328.25	Viscous...
D*i	0.00	m2/s	333.14	Viscous...
D*i	0.00	m2/s	337.93	Viscous...
D*i	0.00	m2/s	337.97	Viscous...
D*i	0.00	m2/s	337.99	Viscous...
D*i	0.00	m2/s	348.08	Viscous...
D*i	0.00	m2/s	352.75	Viscous...
D*i	0.00	m2/s	352.77	Viscous...
D*i	0.00	m2/s	364.53	Viscous...
D*i	0.00	m2/s	364.54	Viscous...
ΔfusS	[138.80; 139.75]	J/mol×K	[263.50; 263.59]
ΔfusS	138.80	J/mol×K	263.50	NIST
ΔfusS	139.75	J/mol×K	263.59	NIST
γ	[0.02; 0.03]	N/m	[293.15; 323.15]
γ	0.02	N/m	293.15	Density...
γ	0.02	N/m	293.15	Surface...
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	294.10	Density...
γ	0.02	N/m	298.15	Interfa...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	303.15	Interfa...
γ	0.02	N/m	303.15	Density...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	323.15	Surface...
λ	[0.13; 0.14]	W/m×K	[318.20; 352.80]
λ	0.14	W/m×K	318.20	Thermal...
λ	0.13	W/m×K	323.20	Thermal...
λ	0.13	W/m×K	328.10	Thermal...
λ	0.13	W/m×K	333.10	Thermal...
λ	0.13	W/m×K	337.70	Thermal...
λ	0.13	W/m×K	343.20	Thermal...
λ	0.13	W/m×K	347.90	Thermal...
λ	0.13	W/m×K	352.80	Thermal...
αdiff	[4.25e-08; 5.83e-08]	m2/s	[423.73; 523.18]
αdiff	5.83e-08	m2/s	423.73	Thermal...
αdiff	5.23e-08	m2/s	448.23	Thermal...
αdiff	4.87e-08	m2/s	473.10	Thermal...
αdiff	4.58e-08	m2/s	498.16	Thermal...
αdiff	4.25e-08	m2/s	523.18	Thermal...

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (3)
3. Mass density, kg/m3 (9)
4. Speed of sound, m/s (1)

Molar heat capacity at constant pressure, J/K/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
323.15	100.00	386.32
328.15	100.00	389.56
333.15	100.00	392.79
338.15	100.00	395.86
343.15	100.00	399.09
348.15	100.00	402.33
353.15	100.00	405.57
358.15	100.00	408.80
363.15	100.00	412.04
368.15	100.00	415.28
373.15	100.00	418.85
378.15	100.00	422.09
383.15	100.00	425.50
388.15	100.00	428.73
393.15	100.00	432.31
398.15	100.00	435.38
403.15	100.00	438.78
408.15	100.00	442.53
413.15	100.00	445.77
418.15	100.00	449.34
423.15	100.00	452.92
428.15	100.00	456.50
433.15	100.00	460.59
438.15	100.00	465.35
323.15	10180.00	385.13
328.15	10180.00	388.02
333.15	10180.00	391.26
338.15	10180.00	394.33
343.15	10180.00	397.39
348.15	10180.00	400.46
353.15	10180.00	403.52
358.15	10180.00	406.93
363.15	10180.00	410.00
368.15	10180.00	413.23
373.15	10180.00	416.13
378.15	10180.00	419.36
383.15	10180.00	422.60
388.15	10180.00	426.01
393.15	10180.00	429.07
398.15	10180.00	433.16
403.15	10180.00	435.89
408.15	10180.00	438.78
413.15	10180.00	441.68
418.15	10180.00	444.06
423.15	10180.00	447.64
428.15	10180.00	450.88
433.15	10180.00	454.28
438.15	10180.00	458.20
443.15	10180.00	462.12
448.15	10180.00	465.70
453.15	10180.00	469.95
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	100.00	0.0015
293.15	1000.00	0.0015
293.15	5000.00	0.0016
293.15	10000.00	0.0017
293.15	20000.00	0.0019
293.15	30000.00	0.0021
293.15	40000.00	0.0023
293.15	50000.00	0.0026
293.15	60000.00	0.0028
293.15	70000.00	0.0031
293.15	80000.00	0.0034
293.15	100000.00	0.0041
293.15	120000.00	0.0050
293.15	140000.00	0.0058
313.15	100.00	0.0011
313.15	1000.00	0.0011
313.15	5000.00	0.0011
313.15	10000.00	0.0012
313.15	20000.00	0.0013
313.15	30000.00	0.0015
313.15	40000.00	0.0016
313.15	50000.00	0.0018
313.15	60000.00	0.0019
313.15	70000.00	0.0021
313.15	80000.00	0.0023
313.15	100000.00	0.0028
313.15	120000.00	0.0032
313.15	140000.00	0.0038
333.15	100.00	0.0008
333.15	1000.00	0.0008
333.15	5000.00	0.0009
333.15	10000.00	0.0009
333.15	20000.00	0.0010
333.15	30000.00	0.0011
333.15	40000.00	0.0012
333.15	50000.00	0.0013
333.15	60000.00	0.0014
333.15	70000.00	0.0016
333.15	80000.00	0.0017
333.15	100000.00	0.0020
333.15	120000.00	0.0023
333.15	140000.00	0.0027
353.15	100.00	0.0006
353.15	1000.00	0.0006
353.15	5000.00	0.0007
353.15	10000.00	0.0007
353.15	20000.00	0.0008
353.15	30000.00	0.0009
353.15	40000.00	0.0010
353.15	50000.00	0.0010
353.15	60000.00	0.0011
353.15	70000.00	0.0012
353.15	80000.00	0.0013
353.15	100000.00	0.0015
353.15	120000.00	0.0018
353.15	140000.00	0.0020
373.15	100.00	0.0005
373.15	1000.00	0.0005
373.15	5000.00	0.0005
373.15	10000.00	0.0006
373.15	20000.00	0.0006
373.15	30000.00	0.0007
373.15	40000.00	0.0008
373.15	50000.00	0.0008
373.15	60000.00	0.0009
373.15	70000.00	0.0010
373.15	80000.00	0.0011
373.15	100000.00	0.0012
373.15	120000.00	0.0014
373.15	140000.00	0.0016
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.20	6020.00	0.0015
298.20	8050.00	0.0015
298.20	10020.00	0.0015
304.90	6020.00	0.0013
303.40	8050.00	0.0014
303.30	10020.00	0.0014
314.50	5990.00	0.0011
313.40	8000.00	0.0012
313.30	10020.00	0.0012
323.40	6050.00	0.0010
323.10	8010.00	0.0010
323.40	10000.00	0.0010
334.10	6010.00	0.0009
333.30	8030.00	0.0009
333.40	10000.00	0.0009
343.30	5990.00	0.0008
343.20	8070.00	0.0008
343.30	10010.00	0.0008
353.40	6080.00	0.0007
353.60	8020.00	0.0007
353.40	9980.00	0.0007
364.00	6040.00	0.0006
363.70	8020.00	0.0006
363.30	10050.00	0.0006
374.00	6000.00	0.0005
373.90	8020.00	0.0006
373.10	10070.00	0.0006
383.00	6010.00	0.0005
383.40	8050.00	0.0005
383.20	10000.00	0.0005
393.10	6080.00	0.0005
393.60	8030.00	0.0005
393.00	10020.00	0.0005
403.00	6040.00	0.0004
404.10	8020.00	0.0004
403.10	10040.00	0.0004
413.20	6080.00	0.0004
413.70	7990.00	0.0004
412.90	10010.00	0.0004
423.00	6080.00	0.0004
423.90	8050.00	0.0004
423.40	10000.00	0.0004
433.20	6010.00	0.0003
433.30	8000.00	0.0003
432.90	10020.00	0.0004
443.50	6020.00	0.0003
443.50	8010.00	0.0003
443.20	10050.00	0.0003
453.30	6020.00	0.0003
454.00	8040.00	0.0003
453.30	9950.00	0.0003
463.40	6040.00	0.0003
464.10	8020.00	0.0003
463.30	10010.00	0.0003
473.40	6040.00	0.0003
473.50	8010.00	0.0003
473.30	10050.00	0.0003
483.40	6050.00	0.0002
483.40	8080.00	0.0002
483.40	10000.00	0.0002
493.40	6040.00	0.0002
493.40	8010.00	0.0002
493.20	10050.00	0.0002
503.40	6080.00	0.0002
502.70	7960.00	0.0002
503.20	10010.00	0.0002
514.20	6050.00	0.0002
513.00	8040.00	0.0002
513.00	10000.00	0.0002
523.70	5970.00	0.0002
523.00	8000.00	0.0002
523.70	10040.00	0.0002
533.50	6040.00	0.0002
533.30	8040.00	0.0002
533.50	10070.00	0.0002
542.90	6010.00	0.0002
542.90	8060.00	0.0002
542.90	9950.00	0.0002
552.90	6070.00	0.0001
553.20	8010.00	0.0002
552.90	10020.00	0.0002
563.00	6050.00	0.0001
563.00	8020.00	0.0001
563.00	10020.00	0.0002
573.00	6010.00	0.0001
573.00	8020.00	0.0001
573.00	10040.00	0.0001
582.80	6000.00	0.0001
582.90	7960.00	0.0001
582.80	10010.00	0.0001
593.00	6020.00	0.0001
592.90	8070.00	0.0001
593.00	10000.00	0.0001
603.10	6010.00	0.0001
602.90	8020.00	0.0001
603.10	10010.00	0.0001
613.10	6040.00	0.0001
612.90	8020.00	0.0001
613.10	10010.00	0.0001
623.20	6050.00	0.0001
623.00	7990.00	0.0001
623.20	10050.00	0.0001
633.50	6020.00	0.0001
632.80	8040.00	0.0001
633.50	10010.00	0.0001
643.40	6020.00	0.0001
643.00	8050.00	0.0001
643.40	10010.00	0.0001
653.40	6070.00	0.0001
652.90	8020.00	0.0001
653.40	10040.00	0.0001
663.20	6010.00	0.0001
663.10	8010.00	0.0001
663.20	10050.00	0.0001
673.50	6040.00	0.0001
672.90	8010.00	0.0001
673.50	9980.00	0.0001
683.30	6010.00	0.0001
683.20	8050.00	0.0001
683.20	10040.00	0.0001
693.20	6010.00	0.0001
693.20	8020.00	0.0001
693.20	10010.00	0.0001
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
284.60	670.00	0.0018
284.70	2710.00	0.0018
284.70	4240.00	0.0018
350.50	690.00	0.0007
350.50	4250.00	0.0007
350.50	8310.00	0.0007
294.00	8310.00	0.0016
322.30	4240.00	0.0010
284.60	2190.00	0.0018
353.10	8320.00	0.0007
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.09	1022.00	735.79
313.09	2023.00	736.6
313.09	3017.00	737.36
313.09	4026.00	738.14
313.09	5023.00	738.89
313.09	6032.00	739.66
313.09	7011.00	740.38
313.09	8009.00	741.15
313.09	9026.00	741.91
313.09	10008.00	742.66
313.09	11022.00	743.39
313.09	12012.00	744.09
313.09	13019.00	744.82
313.09	14017.00	745.55
313.09	15025.00	746.22
313.09	16025.00	746.91
313.09	17015.00	747.58
313.09	18022.00	748.26
313.09	19025.00	748.93
313.09	20013.00	749.59
313.09	21015.00	750.23
313.09	22011.00	750.9
313.09	23021.00	751.53
313.09	24015.00	752.21
313.09	24354.00	752.42
322.97	1025.00	728.33
322.97	2028.00	729.17
322.97	3026.00	729.97
322.97	4034.00	730.78
322.97	5021.00	731.59
322.97	6017.00	732.37
322.97	7017.00	733.17
322.97	8041.00	733.99
322.97	9015.00	734.73
322.97	10016.00	735.5
322.97	11019.00	736.28
322.97	12011.00	737.01
322.97	13028.00	737.78
322.97	14041.00	738.53
322.97	14994.00	739.22
322.97	16027.00	739.96
322.97	17001.00	740.64
322.97	18015.00	741.35
322.97	19032.00	742.07
322.97	20004.00	742.74
322.97	21009.00	743.43
322.97	22023.00	744.14
322.97	23009.00	744.8
322.97	24013.00	745.5
322.97	24507.00	745.83
332.80	1023.00	721.08
332.80	2019.00	721.96
332.80	3022.00	722.81
332.80	4030.00	723.69
332.80	5026.00	724.53
332.80	6035.00	725.36
332.80	7014.00	726.16
332.80	8025.00	727.03
332.80	9017.00	727.84
332.80	10020.00	728.67
332.80	11023.00	729.46
332.80	12022.00	730.26
332.80	13004.00	731.04
332.80	14008.00	731.81
332.80	15018.00	732.57
332.80	16023.00	733.35
332.80	17014.00	734.08
332.80	18006.00	734.82
332.80	19024.00	735.59
332.80	20023.00	736.32
332.80	21009.00	737.01
332.80	22009.00	737.73
332.80	23018.00	738.45
332.80	24018.00	739.17
332.80	24665.00	739.63
342.69	1019.00	713.8
342.69	2025.00	714.75
342.69	3025.00	715.67
342.69	4014.00	716.58
342.69	5015.00	717.47
342.69	6017.00	718.36
342.69	7021.00	719.25
342.69	8007.00	720.13
342.69	9019.00	721.03
342.69	10018.00	721.86
342.69	11016.00	722.71
342.69	12013.00	723.56
342.69	13021.00	724.39
342.69	14020.00	725.21
342.69	15030.00	726.04
342.69	16024.00	726.83
342.69	17011.00	727.58
342.69	18025.00	728.36
342.69	19023.00	729.15
342.69	20013.00	729.88
342.69	21006.00	730.67
342.69	22021.00	731.41
342.69	23014.00	732.15
342.69	24013.00	732.89
342.69	24725.00	733.44
352.51	1021.00	706.54
352.51	2027.00	707.55
352.51	3013.00	708.48
352.51	4019.00	709.46
352.51	5027.00	710.45
352.51	6014.00	711.35
352.51	7020.00	712.33
352.51	8000.00	713.23
352.51	9024.00	714.18
352.51	10009.00	715.07
352.51	11022.00	715.96
352.51	12012.00	716.84
352.51	13026.00	717.71
352.51	14017.00	718.6
352.51	15021.00	719.45
352.51	16022.00	720.3
352.51	17012.00	721.08
352.51	18027.00	721.95
352.51	19013.00	722.74
352.51	20028.00	723.53
352.51	21021.00	724.33
352.51	22023.00	725.14
352.51	23008.00	725.88
352.51	24020.00	726.65
352.51	24813.00	727.31
362.29	1015.00	699.21
362.29	2020.00	700.31
362.29	3015.00	701.33
362.29	4012.00	702.34
362.29	5029.00	703.4
362.29	6009.00	704.36
362.29	7029.00	705.38
362.29	8013.00	706.3
362.29	9012.00	707.31
362.29	10038.00	708.31
362.29	11027.00	709.22
362.29	12009.00	710.09
362.29	13007.00	711.04
362.29	14015.00	711.96
362.29	15008.00	712.81
362.29	16034.00	713.71
362.29	17030.00	714.59
362.29	18011.00	715.43
362.29	19021.00	716.29
362.29	20007.00	717.15
362.29	21017.00	717.94
362.29	22032.00	718.77
362.29	23002.00	719.6
362.29	24005.00	720.38
362.29	24809.00	721.05
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	745.23
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.00	2100.00	752.3
293.00	3100.00	752.9
293.00	4100.00	753.6
293.00	5000.00	754.2
293.00	10100.00	757.5
293.00	20000.00	763.5
293.00	30000.00	769.0
293.00	40000.00	774.3
293.00	50000.00	779.0
293.00	60000.00	783.8
293.00	69900.00	788.0
293.00	79900.00	792.5
293.00	89900.00	796.7
293.00	99900.00	800.8
293.00	109900.00	804.8
293.00	119900.00	808.7
293.00	129900.00	812.4
293.00	134900.00	814.4
293.00	137400.00	815.2
313.00	2100.00	737.7
313.00	3100.00	738.5
313.00	4100.00	739.2
313.00	5000.00	739.9
313.00	10100.00	743.4
313.00	20000.00	750.1
313.00	30000.00	756.3
313.00	40000.00	761.8
313.00	50000.00	767.1
313.00	60000.00	772.1
313.00	69900.00	777.0
313.00	79900.00	781.6
313.00	89900.00	786.1
313.00	99900.00	790.4
313.00	109900.00	794.6
313.00	119900.00	798.7
313.00	129900.00	802.7
313.00	134900.00	804.6
313.00	137400.00	805.4
333.00	2100.00	722.8
333.00	3100.00	723.6
333.00	4100.00	724.5
333.00	5000.00	725.3
333.00	10100.00	729.4
333.00	20000.00	736.6
333.00	30000.00	743.4
333.00	40000.00	749.6
333.00	50000.00	755.3
333.00	60000.00	760.8
333.00	69900.00	766.0
333.00	79900.00	770.9
333.00	89900.00	775.7
333.00	99900.00	780.1
333.00	109900.00	784.6
333.00	119900.00	788.8
333.00	129900.00	793.2
333.00	134900.00	795.1
333.00	137400.00	796.0
353.00	2100.00	708.1
353.00	3100.00	709.0
353.00	4100.00	710.0
353.00	5000.00	710.9
353.00	10100.00	715.6
353.00	20000.00	723.9
353.00	30000.00	731.3
353.00	40000.00	737.7
353.00	50000.00	744.1
353.00	60000.00	750.1
353.00	69900.00	755.6
353.00	79900.00	760.7
353.00	89900.00	765.7
353.00	99900.00	770.5
353.00	109900.00	775.1
353.00	119900.00	779.6
353.00	129900.00	784.0
353.00	134900.00	786.0
353.00	137400.00	787.0
373.00	2100.00	693.2
373.00	3100.00	694.3
373.00	4100.00	695.3
373.00	5000.00	696.3
373.00	10100.00	701.5
373.00	20000.00	710.8
373.00	30000.00	718.7
373.00	40000.00	726.0
373.00	50000.00	733.1
373.00	60000.00	739.4
373.00	69900.00	745.2
373.00	79900.00	750.7
373.00	89900.00	756.0
373.00	99900.00	761.0
373.00	109900.00	765.9
373.00	119900.00	770.6
373.00	129900.00	775.1
373.00	134900.00	777.4
373.00	137400.00	778.5
393.00	2100.00	678.1
393.00	3100.00	679.2
393.00	4100.00	680.4
393.00	5000.00	681.6
393.00	10100.00	687.5
393.00	20000.00	697.8
393.00	30000.00	706.6
393.00	40000.00	714.7
393.00	50000.00	722.2
393.00	60000.00	728.7
393.00	69900.00	735.1
393.00	79900.00	741.1
393.00	89900.00	746.8
393.00	99900.00	752.2
393.00	109900.00	757.2
393.00	119900.00	762.0
393.00	129900.00	766.8
393.00	134900.00	769.0
393.00	137400.00	770.2
413.00	2100.00	662.8
413.00	3100.00	664.2
413.00	4100.00	665.6
413.00	5000.00	666.9
413.00	10100.00	673.7
413.00	20000.00	685.1
413.00	30000.00	694.9
413.00	40000.00	703.6
413.00	50000.00	711.4
413.00	60000.00	718.7
413.00	69900.00	725.4
413.00	79900.00	731.7
413.00	89900.00	737.3
413.00	99900.00	743.2
413.00	109900.00	748.5
413.00	119900.00	753.7
413.00	129900.00	758.5
413.00	134900.00	760.9
413.00	137400.00	762.0
433.00	2100.00	646.8
433.00	3100.00	648.5
433.00	4100.00	650.0
433.00	5000.00	651.6
433.00	10100.00	659.5
433.00	20000.00	672.0
433.00	30000.00	682.8
433.00	40000.00	692.1
433.00	50000.00	700.6
433.00	60000.00	708.3
433.00	69900.00	715.6
433.00	79900.00	722.1
433.00	89900.00	728.3
433.00	99900.00	734.3
433.00	109900.00	739.8
433.00	119900.00	745.1
433.00	129900.00	750.3
433.00	134900.00	752.7
433.00	137400.00	753.9
448.00	2100.00	634.6
448.00	3100.00	636.7
448.00	4100.00	638.2
448.00	5000.00	640.0
448.00	10100.00	648.5
448.00	20000.00	662.4
448.00	30000.00	674.0
448.00	40000.00	684.0
448.00	50000.00	692.9
448.00	60000.00	701.0
448.00	69900.00	708.3
448.00	79900.00	715.3
448.00	89900.00	721.9
448.00	99900.00	727.9
448.00	109900.00	733.5
448.00	119900.00	739.0
448.00	129900.00	744.2
448.00	134900.00	746.7
448.00	137400.00	747.9
468.00	2100.00	617.8
468.00	3100.00	619.9
468.00	4100.00	622.0
468.00	5000.00	624.1
468.00	10100.00	634.1
468.00	20000.00	649.5
468.00	30000.00	661.8
468.00	40000.00	672.8
468.00	50000.00	682.6
468.00	60000.00	691.0
468.00	69900.00	698.9
468.00	79900.00	706.3
468.00	89900.00	712.9
468.00	99900.00	719.2
468.00	109900.00	725.1
468.00	119900.00	731.0
468.00	129900.00	736.3
468.00	134900.00	738.9
468.00	137400.00	740.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.29	100.00	756.0
283.29	1000.00	757.0
283.29	3000.00	758.0
283.30	5000.00	760.0
283.30	10000.00	763.0
283.31	20000.00	769.0
283.30	30000.00	775.0
283.30	40000.00	780.0
283.30	50000.00	785.0
283.30	60000.00	790.0
283.31	70000.00	795.0
283.32	80000.00	799.0
283.32	90000.00	803.0
293.17	100.00	749.0
293.18	1000.00	750.0
293.19	5000.00	753.0
293.19	10000.00	756.0
293.19	20000.00	763.0
293.19	30000.00	769.0
293.19	40000.00	774.0
293.19	50000.00	780.0
293.20	60000.00	785.0
293.19	70000.00	789.0
293.19	80000.00	794.0
293.19	90000.00	798.0
293.19	100000.00	802.0
303.05	100.00	742.0
303.05	1000.00	743.0
303.05	5000.00	746.0
303.06	10000.00	749.0
303.05	20000.00	756.0
303.04	30000.00	762.0
303.06	40000.00	768.0
303.05	50000.00	774.0
303.05	60000.00	779.0
303.05	70000.00	784.0
303.05	80000.00	789.0
303.05	90000.00	793.0
303.04	100000.00	797.0
312.89	100.00	736.0
312.89	1000.00	737.0
312.90	5000.00	740.0
312.90	10000.00	744.0
312.90	20000.00	751.0
312.90	30000.00	757.0
312.90	40000.00	763.0
312.90	50000.00	769.0
312.90	60000.00	774.0
312.90	70000.00	780.0
312.90	80000.00	784.0
312.90	90000.00	789.0
312.90	100000.00	793.0
322.83	100.00	727.0
322.83	1000.00	728.0
322.83	5000.00	732.0
322.83	10000.00	736.0
322.83	20000.00	743.0
322.83	30000.00	750.0
322.83	40000.00	756.0
322.83	50000.00	762.0
322.83	60000.00	768.0
322.83	70000.00	773.0
322.83	80000.00	778.0
322.83	90000.00	783.0
322.83	100000.00	787.0
332.74	100.00	720.0
332.74	1000.00	721.0
332.74	5000.00	725.0
332.74	10000.00	729.0
332.74	20000.00	737.0
332.74	30000.00	744.0
332.74	40000.00	750.0
332.74	50000.00	757.0
332.74	60000.00	762.0
332.74	70000.00	768.0
332.74	80000.00	773.0
332.74	90000.00	778.0
332.75	100000.00	782.0
342.67	100.00	713.0
342.67	1000.00	714.0
342.67	5000.00	718.0
342.67	10000.00	722.0
342.67	20000.00	731.0
342.67	30000.00	738.0
342.67	40000.00	745.0
342.67	50000.00	751.0
342.67	60000.00	757.0
342.67	69990.00	763.0
342.67	80000.00	768.0
342.67	90000.00	773.0
342.67	100000.00	778.0
352.58	100.00	707.0
352.58	1000.00	708.0
352.58	5000.00	712.0
352.58	10000.00	716.0
352.58	20000.00	725.0
352.58	30000.00	733.0
352.58	40000.00	740.0
352.58	50000.00	747.0
352.58	60000.00	753.0
352.58	70000.00	759.0
352.58	80000.00	764.0
352.58	90000.00	769.0
352.58	100000.00	774.0
362.49	100.00	699.0
362.49	1000.00	700.0
362.48	5000.00	704.0
362.48	10000.00	709.0
362.48	20000.00	718.0
362.48	30000.00	726.0
362.49	40000.00	734.0
362.48	50000.00	741.0
362.49	60000.00	747.0
362.49	70000.00	753.0
362.48	80000.00	759.0
362.48	90000.00	764.0
362.49	100000.00	769.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	759.2
278.15	1000.00	760.5
278.15	5000.00	763.1
278.15	10000.00	766.2
278.15	20000.00	771.9
278.15	30000.00	777.3
278.15	40000.00	782.3
278.15	50000.00	787.1
278.15	60000.00	791.7
298.15	100.00	745.6
298.15	1000.00	746.2
298.15	5000.00	749.0
298.15	10000.00	752.4
298.15	20000.00	758.7
298.15	30000.00	764.7
298.15	40000.00	770.1
298.15	50000.00	775.3
298.15	60000.00	780.2
323.15	100.00	727.2
323.15	1000.00	728.2
323.15	5000.00	731.4
323.15	10000.00	735.3
323.15	20000.00	742.6
323.15	30000.00	749.2
323.15	40000.00	755.2
323.15	50000.00	760.9
323.15	60000.00	766.3
348.15	100.00	708.7
348.15	1000.00	709.6
348.15	5000.00	713.4
348.15	10000.00	717.8
348.15	20000.00	726.1
348.15	30000.00	733.5
348.15	40000.00	740.2
348.15	50000.00	746.4
348.15	60000.00	752.3
373.15	1000.00	690.8
373.15	5000.00	695.2
373.15	10000.00	700.4
373.15	20000.00	709.8
373.15	30000.00	718.1
373.15	40000.00	725.6
373.15	50000.00	732.5
373.15	60000.00	738.9
423.15	1000.00	652.6
423.15	5000.00	658.7
423.15	10000.00	665.6
423.15	20000.00	677.6
423.15	30000.00	688.0
423.15	40000.00	697.0
423.15	50000.00	705.3
423.15	60000.00	712.8
463.15	5000.00	627.9
463.15	10000.00	636.9
463.15	20000.00	651.8
463.15	30000.00	664.2
463.15	40000.00	674.8
463.15	50000.00	684.1
463.15	60000.00	692.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.21	2007.00	750.58
293.21	3977.00	752.18
293.21	5979.00	753.71
293.21	7982.00	755.06
293.22	9987.00	756.38
293.21	12987.00	758.27
293.22	15986.00	760.07
293.22	18994.00	761.82
293.22	21995.00	763.63
293.22	24987.00	765.5
293.22	27987.00	767.37
293.21	29985.00	768.5
313.10	1990.00	736.16
313.10	4017.00	737.72
313.10	6016.00	739.14
313.10	8014.00	740.64
313.10	10011.00	742.11
313.10	13007.00	744.26
313.10	16011.00	746.36
313.10	19017.00	748.61
313.10	22017.00	750.69
313.10	25019.00	752.63
313.10	28017.00	754.52
313.10	30020.00	755.75
333.01	2024.00	721.82
333.00	3976.00	723.61
333.01	5981.00	725.32
333.01	7987.00	726.99
333.01	10019.00	728.35
333.01	13016.00	730.73
333.01	16014.00	733.04
333.01	19018.00	735.29
333.01	22015.00	737.46
333.01	25018.00	739.58
333.01	28015.00	741.65
333.01	30024.00	742.99
353.12	2000.00	706.86
353.12	3991.00	708.83
353.12	5996.00	710.75
353.12	8009.00	712.81
353.12	10014.00	714.63
353.12	13006.00	717.28
353.12	16007.00	719.83
353.12	19003.00	722.16
353.12	22006.00	724.55
353.12	25008.00	726.87
353.12	28011.00	729.13
353.12	30007.00	730.59
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	745.29
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.53	8012.00	740.43
313.50	9962.00	741.88
313.50	12011.00	743.35
313.52	13987.00	744.76
313.48	16030.00	746.15
313.48	17972.00	747.51
323.46	7994.00	733.56
323.48	9968.00	735.18
323.57	11960.00	736.57
323.52	13993.00	738.13
323.49	16021.00	739.64
323.49	18018.00	741.06
333.55	8003.00	726.32
333.51	9996.00	727.99
333.55	11980.00	729.56
333.56	13998.00	731.15
333.53	15975.00	732.68
333.52	17973.00	734.22
343.50	7959.00	719.25
343.50	10036.00	721.04
343.48	11000.00	721.9
343.48	11993.00	722.72
343.47	12998.00	723.59
343.52	13977.00	724.32
343.54	14989.00	725.15
343.55	15979.00	725.97
343.56	16970.00	726.72
343.56	18004.00	727.54
353.57	8022.00	712.16
353.57	10035.00	713.95
353.58	11021.00	714.86
353.58	12000.00	715.73
353.56	13021.00	716.67
353.56	13976.00	717.47
353.52	15037.00	718.45
353.55	15991.00	719.22
353.59	17027.00	720.07
353.53	17993.00	720.9
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	756.0
100.00	288.15	752.4
100.00	293.15	748.8
100.00	298.15	745.3
100.00	303.15	741.7
100.00	308.15	738.1
100.00	313.15	734.4
100.00	318.15	730.8
100.00	323.15	727.1
10000.00	283.15	762.4
10000.00	288.15	758.9
10000.00	293.15	755.5
10000.00	298.15	752.1
10000.00	303.15	748.7
10000.00	308.15	745.3
10000.00	313.15	741.8
10000.00	318.15	738.4
10000.00	323.15	734.9
20000.00	283.15	768.3
20000.00	288.15	765.1
20000.00	293.15	761.7
20000.00	298.15	758.5
20000.00	303.15	755.2
20000.00	308.15	752.0
20000.00	313.15	748.7
20000.00	318.15	745.4
20000.00	323.15	742.0
30000.00	283.15	773.9
30000.00	288.15	770.7
30000.00	293.15	767.6
30000.00	298.15	764.4
30000.00	303.15	761.3
30000.00	308.15	758.2
30000.00	313.15	755.0
30000.00	318.15	751.9
30000.00	323.15	748.6
40000.00	283.15	779.2
40000.00	288.15	776.1
40000.00	293.15	773.1
40000.00	298.15	770.0
40000.00	303.15	767.0
40000.00	308.15	764.0
40000.00	313.15	760.9
40000.00	318.15	757.9
40000.00	323.15	754.8
50000.00	283.15	784.1
50000.00	288.15	781.2
50000.00	293.15	778.2
50000.00	298.15	775.3
50000.00	303.15	772.4
50000.00	308.15	769.4
50000.00	313.15	766.4
50000.00	318.15	763.5
50000.00	323.15	760.5
60000.00	283.15	788.6
60000.00	288.15	786.0
60000.00	293.15	783.2
60000.00	298.15	780.3
60000.00	303.15	777.5
60000.00	308.15	774.6
60000.00	313.15	771.7
60000.00	318.15	768.8
60000.00	323.15	765.9
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 3 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
10000.00	303.15	1318.5
20000.00	303.15	1372.4
30000.00	303.15	1421.4
40000.00	303.15	1468.5
50000.00	303.15	1512.3
60000.00	303.15	1553.7
70000.00	303.15	1593.3
10000.00	313.15	1281.7
20000.00	313.15	1337.9
30000.00	313.15	1389.6
40000.00	313.15	1436.8
50000.00	313.15	1481.5
60000.00	313.15	1524.2
70000.00	313.15	1564.6
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[6.62e-04; 1746.95]	kPa	[263.57; 658.20]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.12723e+02
Coefficient B			-1.12005e+04
Coefficient C			-1.39838e+01
Coefficient D			5.78857e-06
Temperature range, min.			263.57
Temperature range, max.			658.20
Pvap	6.62e-04	kPa	263.57	Calculated Property
Pvap	0.04	kPa	307.42	Calculated Property
Pvap	0.66	kPa	351.27	Calculated Property
Pvap	5.30	kPa	395.11	Calculated Property
Pvap	25.51	kPa	438.96	Calculated Property
Pvap	86.39	kPa	482.81	Calculated Property
Pvap	228.37	kPa	526.66	Calculated Property
Pvap	505.56	kPa	570.50	Calculated Property
Pvap	984.52	kPa	614.35	Calculated Property
Pvap	1746.95	kPa	658.20	Calculated Property

Similar Compounds

Find more compounds similar to Dodecane.

Mixtures

• Dodecane + Ethyl Acetate
• Dodecane + Isopropyl acetate
• Dodecane + 2-Pyrrolidinone, 1-methyl-
• Dodecane + 2-Pyrrolidinone, 1-methyl- + Benzene, propyl-
• Dodecane + Formamide, N,N-dimethyl-
• Dodecane + Formamide, N,N-dimethyl- + Benzene, (1-methylpropyl)-
• Dodecane + o-Toluidine
• Benzo[b]thiophene + Dodecane
• 1-Propanol + Dodecane
• Dodecane + Tributyl phosphate
• 1-Octanamine, N,N-dioctyl- + Dodecane
• Dodecane + Benzaldehyde
• Carbon dioxide + Dodecane
• Acetonitrile + Dodecane + Acetic acid
• Acetonitrile + Dodecane + Propanoic acid
• Acetonitrile + Dodecane + Butanoic acid
• Acetonitrile + Dodecane + Propanoic acid, 2-methyl-
• Acetonitrile + Dodecane + Pentanoic acid
• Acetonitrile + Dodecane + Butanoic acid, 3-methyl-
• Dodecane + Acetophenone

Find more mixtures with Dodecane.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Crippen Method
• Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
• Liquid liquid equilibria for n-alkanes (C12, C14, C17) + propylbenzene +NMP mixtures at temperatures between 298 and 328K
• Phase equilibria for the extraction of sec-butylbenzene from dodecane with N,N-dimethylformamide
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
• High-pressure vapor liquid equilibria for CO2 + alkanol systems and densities of n-dodecane and n-tridecane
• Solution thermodynamics near the liquid liquid critical point I. First-order excess derivatives
• Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
• Ionic liquids on desulfurization of fuel oils
• Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
• Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
• P-x data for binary systems using a novel static total pressure apparatus
• Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
• Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
• Liquid-liquid equilibria for ternary systems acetic acid + n-butylacetate + hydrocarbons at 293.15 K
• Interfacial tension of binary mixtures exhibiting azeotropic behavior: Measurement and modeling with PCP-SAFT combined with Density Gradient Theory
• Liquid-liquid equilibria for benzaldehyde + n-alkane mixtures andcharacterization of benzaldehyde + hydrocarbon systems in terms of DISQUAC
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• High-pressure densities and interfacial tensions of binary systems containing carbon dioxide + n-alkanes: (n-Dodecane, n-tridecane, n-tetradecane)
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Liquid liquid equilibria measurements of ternary systems (acetonitrile + a carboxylic acid + dodecane) at 303.15 K
• Liquid liquid equilibria for acetophenone + n-alkane mixtures and characterization of acetophenone systems using DISQUAC
• Speed of sound and thermodynamic properties of ternary liquid mixture octane + dodecane + hexadecane
• High pressure phase behaviour of the CO2 + 1-decanol + n-dodecane system
• Liquid-liquid-liquid equilibria for water + [P6 6 6 14][DCA] + dodecane ternary system
• Study of the suitability of two ammonium-based ionic liquids for the extraction of benzene from its mixtures with aliphatic hydrocarbons.
• Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
• An experimental investigation on the solubility of methane in 1-octanol and n-dodecane at ambient temperatures
• Determination of solubility parameters from density measurements for non-polar hydrocarbons at temperatures from (298 to 433) K and pressures up to 137 MPa
• Compressed liquid densities of binary mixtures of n-decane + n-dodecane at temperatures from 283 K to 363 K and pressures up to 100 MPa
• High temperature and pressure water/oil interfacial tension benchmark data for the Ninth Industrial Fluid Properties Simulation Challenge
• Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
• Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
• Liquid--liquid equilibria for mixtures of {methyl acetate + methanol + n-alkane (C10--C12)} at several temperatures and 1 atm
• Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
• Ternary (liquid + liquid) equilibria for mixtures of 1-hexyl-3-methylimidazolium (tetrafluoroborate or hexafluorophosphate) + benzene + an alkane at T = 298.2 K and p = 0.1 MPa
• Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether +2-methylpentane + (n-decane or n-dodecane) at the temperature 298.15 K
• Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
• Excess molar enthalpies of the ternary mixtures: {tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-dodecane} at the temperature 298.15 K
• Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
• (Liquid + liquid) equilibria for ternary mixtures of (methanol or ethanol + toluene or m-xylene + n-dodecane)
• Ternary (liquid + liquid) equilibria for mixtures of (methanol + aniline + n-octane or n-dodecane) at T = 298.15 K
• (Liquid + liquid) equilibria of [C8mim][NTf2] ionic liquid with a sulfur-component and hydrocarbons
• Excess properties and vapour pressure of (3-diethylaminopropylamine + n-alkanes)
• Solvent extraction of thiophene from n-alkanes (C7, C12, and C16) using the ionic liquid [C8mim][BF4]
• Thermodynamic and acoustic properties of (heptane + dodecane) mixtures under elevated pressures
• Partition behaviour of benzoic acid in (water + n-dodecane) solutions at T = (293.15 and 298.15) K
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• Excess molar enthalpies of binary mixtures containing 2-decanone or dipentyl ether with long-chain n-alkanes at T = 298.15 K
• Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
• Extraction of propylbenzene or butylbenzene from dodecane using 4-methyl-N-butylpyridinium tetrafluoroborate, [mebupy][BF4], as an ionic liquid at different temperatures
• (Liquid + liquid) equilibria for the ternary system (water + dodecane + propylene glycol n-propyl ether)
• Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester + alkane and ester + ester binary systems and the ternary dodecane + ethyl pentanoate + ethyl ethanoate
• Evaluation of [bmim][PF6] as an ionic solvent for the extraction of propylbenzene from aliphatic compounds
• Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
• Physical properties of phosphonium ionic liquid and its mixtures with dodecane and water
• Water/oil/[P6,6,6,14][NTf2] phase equilibria
• (Liquid + liquid) equilibria for mixtures of dodecane and ethanol with alkylsulfate-based ionic liquids
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• 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
• Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques
• Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
• Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
• Heat capacity and Joule-Thomson coefficient of selected n-alkanes at 0.1 and 10 MPa in broad temperature ranges
• Phase equilibrium measurements and thermodynamic modeling of binary mixtures containing a diesel compound n-dodecane + biodiesel compounds: Ethyl dodecanoate and ethyl octanoate
• Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
• Thermophysical properties of fatty acid methyl and ethyl esters
• Excess molar enthalpies of the ternary mixtures: methyl tert-butyl ether + 3-methylpentane + (n-decane or n-dodecane) at 298.15K
• Determination of vapor pressure and thermal decomposition using thermogravimetrical analysis
• Viscous Calibration Liquids for Self-diffusion Measurements
• Prediction and Experimental Measurement of Refractive Index in Ternary Hydrocarbon Mixtures
• Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
• Experimental and Computational Study on Liquid Liquid Equilibrium in Ternary Systems of -Valerolactone, Toluene, and Hydrocarbons
• Densities of the binary systems n-hexane + n-decane and nhexane + n-hexadecane up to 60 MPa and 463 K
• Thermal and Mutual Diffusivity of Binary Mixtures of n-Dodecane and n-Tetracontane with Carbon Monoxide, Hydrogen, and Water from Dynamic Light Scattering (DLS)
• Liquid Liquid Equilibria of Binary and Ternary Systems Methanol/Water + n-Hexane, + n-Octane, + n-Dodecane, and + n-Hexadecane in the Temperature Range between T = 283.15 K and T = 333.15 K
• Equilibrium Study on the Extraction of Levulinic Acid from Aqueous Solution with Aliquat 336 Dissolved in Different Diluents: Solvent s Polarity Effect and Column Design
• Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester
• Viscosity Measurement of Endothermic Fuels at Temperatures from 303 K to 673 K and Pressures up to 5.00 MPa
• Liquid Liquid Equilibria for the Ternary Systems Dodecane + Toluene or Thiophene or Pyridine + 1-Ethyl-3-methylimidazolium Methyl Sulfate
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylbenzene + Linear Alkanes (n-Decane, n-Dodecane, n-Tetradecane, n-Hexadecane, or n-Heptadecane) at 0.1 MPa
• Density, Viscosity, and Freezing Point for Four Binary Systems of n-Dodecane or Methylcyclohexane Mixed with 1-Heptanol or Cyclohexylmethanol
• Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
• Liquid Liquid Equilibria for Systems Containing 4-Phenylbutan-2-one or Benzyl Ethanoate and Selected Alkanes
• Solvent Polarity Effect when Amberlite-LA2 Is Used in the Extraction of Picric Acid
• Density, Viscosity, and Structure of Equilibrium Solvent Phases in Butyric Acid Extraction by Phosphonium Ionic Liquid
• Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
• 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
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Liquid Viscosity and Surface Tension of n-Dodecane, n-Octacosane, Their Mixtures, and a Wax between 323 and 573 K by Surface Light Scattering
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
• Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
• Simultaneous Measurement of Dynamic Viscosity and Density of n-Alkanes at High Pressures
• Density and Compressibility of Multicomponent n-Alkane Mixtures up to 463 K and 140 MPa
• Viscosity Measurements of n-Dodecane at Temperatures between 303 K and 693 K and Pressures up to 10 MPa
• Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
• Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
• Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
• Liquid-Liquid Equilibria of Formic Acid and Furfural in a Biphasic Aqueous-Organic System: Optimization of Solvent and Amine Extractant
• Densities and Viscosities of Ternary System n-Dodecane (1) + Bicyclohexyl (2) + n-Butanol (3) and Corresponding Binaries at T = (293.15 to 333.15) K
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Liquid-Liquid Equilibria of Lactic Acid/Water Solutions in Tri-iso-octylamine/Dodecane/1-Dodecanol at 306.1, 310.1, and 316.1 K. Experimental Data and Prediction
• Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
• Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Quaternary Mixtures of n-Dodecane (1), n-Butylcyclohexane (2), n-Butylbenzene (3), and 2,2,4,4,6,8,8-Heptamethylnonane (4) at 0.1 MPa as Potential Surrogate Mixtures for Military Jet Fuel, JP-5
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
• Phase Equilibrium and Liquid Viscosity of CO2 + n-Dodecane Mixtures between 283 and 353 K
• Liquid-Liquid Equilibrium for Ternary Systems of N-Methylformamide + Pyrrole/Indole + Alkanes at 298.15 K: Phase Equilibrium Measurement and Correlation
• Density, Speed of Sound, Compressibility, and Excess Properties of Carbon Dioxide + n-Dodecane Binary Mixtures from 10 to 70 MPa
• Experimental Investigation of the Thermophysical Properties of the Bio-Aviation Fuel Surrogates: Binary and Ternary Mixtures of n-Dodecane, Methyl Butyrate, and Methyl Decanoate
• Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
• Liquid-Liquid Equilibria for Mixtures of (Furfural + a Chlorinated Aromatic Compound + an Alkane) at T = 298.15 K
• Excess molar volumes and enthalpies of mixing for the ternary system (butyl butyrate + 1-octanol + dodecane) at the temperature 308.15 K.
• Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
• Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
• Solubility of Benzophenone in Binary Alkane + Carbon Tetrachloride Solvent Mixtures
• Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
• Dynamic Viscosities of 2-Pentanol with Alkanes (Octane, Decane, and Dodecane) at Three Temperatures T ) (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO Interaction Parameters
• Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
• Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Measurement and Correlation of Phase Equilibria for Dodecane + sec-Butylbenzene + N-Methyl-2-pyrrolidone
• Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Densities and Viscosities of Binary Mixtures of Tributyl Phosphate with Hexane and Dodecane from (298.15 to 328.15) K
• 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 Equilibria for {1-Ethyl-3-methylimidazolium Diethylphosphate or 1-Ethyl-3-methylimidazolium Ethylsulfate} + 4,6-Dimethyldibenzothiophene + Dodecane Systems at 298.2 K and 313.2 K
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Vapor-Liquid Equilibrium Data for the Nitrogen + Dodecane System at Temperatures from (344 to 593) K and at Pressures up to 60 MPa
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Liquid Liquid Equilibria of Alkane (C10 C14) + sec-Butylbenzene + Sulfolane
• Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
• Vapor Liquid Equilibria of Binary and Ternary Systems Containing Carbon Dioxide, Alkane, and Benzothiophene
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Liquid Liquid Equilibria of Methanol, Ethanol, and Propan-2-ol with Water and Dodecane
• Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
• Liquid Liquid Equilibrium in N-Methyl-2-hydroxyethylammonium Acetate, Butanoate, or Hexanoate Ionic Liquids + Dibenzothiophene + n-Dodecane Systems at 298.2 K and Atmospheric Pressure
• Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
• Isothermal Vapor Liquid Equilibrium Data for the Propan-1-ol + Dodecane System at (323.0, 343.4, 353.2, 363.1, and 369.2) K
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
• Thermodynamics of Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
• Extraction of Butylbenzene from Dodecane Using Hexafluorophosphate-Based Ionic Liquids: Effect of Cation Change
• Liquid Liquid Equilibria for the Ternary System Water + Dodecane + 1-(1-Methyl-2-propoxyethoxy)-2-propanol
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
• Density, Viscosity, and Interfacial Tension of Binary Mixture of Tri-iso-amyl Phosphate (TiAP) and n-Dodecane: Effect of Compositions and Gamma Absorbed Doses
• Solid Liquid Equilibria, Excess Molar Volumes, and Deviations in the Molar Refractivity for the Binary Systems of Alamine 304-1 + Decane, Dodecane, or Dodecanol
• Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
• Liquid Liquid Equilibria for the Ternary Systems of 4-Methyl-1,3-dioxolan-2-one + 1,4-Dimethylbenzene + Octane, Decane, or Dodecane and the Ternary Systems of Acetonitrile + Morpholine + Octane, Decane, or Dodecane at 313.15 K or 298.15 K
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Dodecane with 2,2,4,6,6-Pentamethylheptane or 2,2,4,4,6,8,8-Heptamethylnonane
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Vapor Liquid Equilibrium Data for Binary Systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa
• Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
• Measurement and Modeling of the Densities for CO2 + Dodecane System from 313.55 K to 353.55 K and Pressures up to 18 MPa
• Binary Liquid Liquid Equilibria of ?-Valerolactone with Some Hydrocarbons
• Liquid-Liquid Equilibria of Alkane (C10-C14) + Hexylbenzene + Sulfolane
• Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
• Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
• Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
• Comparison between Experimental and Theoretical Estimations of the Thermal Expansion, Concentration Expansion Coefficients, and Viscosity for Binary Mixtures under Pressures up to 20 MPa
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Excess Molar Enthalpies of Binary Systems of 2-Octanone or 3-Octanone with Dodecane, Tetradecane, or Hexadecane at 298.15 K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Excess Molar Enthalpies of Binary Systems of n-Valeric Anhydride or n-Hexanoic Anhydride with n-Dodecane, n-Tetradecane, or n-Hexadecane at 298.15 K
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Miscibility of Trihexyl(tetradecyl)phosphonium Chloride with Alkanes
• Joback Method
• KDB
• McGowan Method
• NIST Webbook

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