Chemical Properties of 1-Pentanol (CAS 71-41-0)

InChI

InChI=1S/C5H12O/c1-2-3-4-5-6/h6H,2-5H2,1H3

InChI Key

AMQJEAYHLZJPGS-UHFFFAOYSA-N

Formula

C5H12O

SMILES

CCCCCO

Molecular Weight¹

88.15

CAS

71-41-0

Other Names

• 1-Pentol
• 1-Pentyl alcohol
• Alcool amylique
• Amyl alcohol
• Amyl alcohol, n-
• Amyl alcohol, normal
• Amylol
• Butyl carbinol
• N-AMYL ALCOHOL
• N-PENTYL ALCOHOL
• NSC 5707
• Pentan-1-ol
• Pentanol
• Pentanol-1
• Pentasol
• Pentyl alcohol
• Primary amyl alcohol
• Primary-N-amyl alcohol
• UN 1105
• n-Amylalkohol
• n-Butylcarbinol
• n-C5H11OH
• n-Pentan-1-ol
• n-Pentanol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,oc : Flash Point (Open 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_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• 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.
• NFPA Health : NFPA Health 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.
• I : 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_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.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

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

Physical Properties

Property	Value	Unit	Source
ω	0.5790		KDB
PAff	795.00	kJ/mol	NIST
Tig	633.15	K	KDB
ΔcH°liquid	[-3330.91; -3324.00]	kJ/mol
ΔcH°liquid	-3330.91 ± 0.28	kJ/mol	NIST
ΔcH°liquid	-3329.90 ± 0.67	kJ/mol	NIST
ΔcH°liquid	-3329.96 ± 0.64	kJ/mol	NIST
ΔcH°liquid	-3324.60 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-3324.00	kJ/mol	NIST
Cp,liquid	206.67	J/mol×K	THERMOD...
μ	1.70	debye	KDB
LFL	1.10	% in Air	KDB
UFL	7.50	% in Air	KDB
Tflash,oc	298.15	K	KDB
ΔfG°	-146.10	kJ/mol	KDB
ΔfH°gas	[-301.00; -294.70]	kJ/mol
ΔfH°gas	-298.90	kJ/mol	KDB
ΔfH°gas	-294.70	kJ/mol	NIST
ΔfH°gas	-294.70 ± 0.30	kJ/mol	NIST
ΔfH°gas	-295.70 ± 0.70	kJ/mol	NIST
ΔfH°gas	-295.63 ± 0.74	kJ/mol	NIST
ΔfH°gas	-301.00	kJ/mol	NIST
ΔfH°gas	-301.00 ± 0.50	kJ/mol	NIST
ΔfH°gas	-300.60 ± 2.00	kJ/mol	NIST
ΔfH°liquid	[-358.40; -351.62]	kJ/mol
ΔfH°liquid	-351.62 ± 0.28	kJ/mol	NIST
ΔfH°liquid	-352.60 ± 0.70	kJ/mol	NIST
ΔfH°liquid	-352.57 ± 0.72	kJ/mol	NIST
ΔfH°liquid	-357.90 ± 0.50	kJ/mol	NIST
ΔfH°liquid	-358.40 ± 1.70	kJ/mol	NIST
ΔfusH°	10.51	kJ/mol	Heat Ca...
ΔvapH°	[54.23; 57.80]	kJ/mol
ΔvapH°	57.04	kJ/mol	NIST
ΔvapH°	Outlier 54.23	kJ/mol	NIST
ΔvapH°	55.18	kJ/mol	NIST
ΔvapH°	55.40	kJ/mol	NIST
ΔvapH°	55.40	kJ/mol	NIST
ΔvapH°	57.80	kJ/mol	NIST
ΔvapH°	57.40	kJ/mol	NIST
ΔvapH°	56.94 ± 0.17	kJ/mol	NIST
ΔvapH°	56.90	kJ/mol	NIST
ΔvapH°	56.90 ± 0.20	kJ/mol	NIST
ΔvapH°	56.90 ± 0.20	kJ/mol	NIST
ΔvapH°	57.70 ± 1.10	kJ/mol	NIST
ΔvapH°	57.70 ± 1.00	kJ/mol	NIST
ΔvapH°	57.80	kJ/mol	NIST
IE	[10.00; 10.42]	eV
IE	10.00	eV	NIST
IE	10.38	eV	NIST
IE	10.42 ± 0.03	eV	NIST
log10WS	[-0.60; -0.60]
log10WS	-0.60		Aq. Sol...
log10WS	-0.60		Estimat...
logPoct/wat	1.169		Crippen Calculated Property
McVol	87.180	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[3868.00; 3920.00]	kPa
Pc	3897.00	kPa	KDB
Pc	3900.00 ± 20.00	kPa	NIST
Pc	3920.00 ± 40.00	kPa	NIST
Pc	3868.00 ± 20.00	kPa	NIST
Pc	3868.00 ± 20.00	kPa	NIST
Pc	3909.00	kPa	NIST
Pc	3909.00	kPa	NIST
ρc	[269.73; 273.26]	kg/m3
ρc	269.73 ± 1.76	kg/m3	NIST
ρc	269.73	kg/m3	NIST
ρc	273.26 ± 17.63	kg/m3	NIST
Inp	[722.00; 801.00]
Inp	Outlier 791.40		NIST
Inp	Outlier 793.10		NIST
Inp	775.50		NIST
Inp	771.90		NIST
Inp	766.50		NIST
Inp	762.30		NIST
Inp	757.90		NIST
Inp	757.18		NIST
Inp	754.60		NIST
Inp	753.50		NIST
Inp	752.70		NIST
Inp	752.20		NIST
Inp	766.00		NIST
Inp	763.40		NIST
Inp	761.50		NIST
Inp	754.60		NIST
Inp	753.50		NIST
Inp	752.70		NIST
Inp	752.20		NIST
Inp	766.00		NIST
Inp	763.40		NIST
Inp	761.50		NIST
Inp	Outlier 730.20		NIST
Inp	Outlier 734.70		NIST
Inp	754.00		NIST
Inp	748.00		NIST
Inp	768.00		NIST
Inp	760.00		NIST
Inp	749.00		NIST
Inp	754.00		NIST
Inp	Outlier 789.00		NIST
Inp	746.40		NIST
Inp	742.00		NIST
Inp	Outlier 728.00		NIST
Inp	Outlier 731.00		NIST
Inp	Outlier 730.00		NIST
Inp	751.00		NIST
Inp	747.00		NIST
Inp	746.00		NIST
Inp	736.00		NIST
Inp	746.00		NIST
Inp	Outlier 730.00		NIST
Inp	Outlier 722.00		NIST
Inp	752.00		NIST
Inp	758.00		NIST
Inp	763.00		NIST
Inp	775.00		NIST
Inp	747.00		NIST
Inp	750.00		NIST
Inp	773.00		NIST
Inp	774.00		NIST
Inp	752.00		NIST
Inp	755.00		NIST
Inp	759.00		NIST
Inp	764.00		NIST
Inp	764.00		NIST
Inp	765.00		NIST
Inp	766.00		NIST
Inp	760.00		NIST
Inp	760.00		NIST
Inp	756.00		NIST
Inp	766.00		NIST
Inp	768.00		NIST
Inp	768.00		NIST
Inp	765.00		NIST
Inp	764.00		NIST
Inp	763.00		NIST
Inp	779.00		NIST
Inp	766.00		NIST
Inp	767.00		NIST
Inp	744.10		NIST
Inp	760.40		NIST
Inp	783.00		NIST
Inp	769.00		NIST
Inp	735.00		NIST
Inp	735.00		NIST
Inp	772.00		NIST
Inp	759.00		NIST
Inp	754.00		NIST
Inp	754.00		NIST
Inp	753.00		NIST
Inp	749.00		NIST
Inp	748.30		NIST
Inp	752.00		NIST
Inp	760.00		NIST
Inp	768.00		NIST
Inp	751.90		NIST
Inp	751.90		NIST
Inp	764.00		NIST
Inp	765.00		NIST
Inp	764.00		NIST
Inp	753.00		NIST
Inp	758.00		NIST
Inp	765.00		NIST
Inp	771.00		NIST
Inp	780.00		NIST
Inp	764.00		NIST
Inp	765.00		NIST
Inp	766.00		NIST
Inp	764.00		NIST
Inp	766.00		NIST
Inp	767.00		NIST
Inp	746.00		NIST
Inp	756.00		NIST
Inp	770.00		NIST
Inp	763.00		NIST
Inp	762.00		NIST
Inp	781.00		NIST
Inp	772.00		NIST
Inp	778.00		NIST
Inp	761.00		NIST
Inp	760.00		NIST
Inp	770.00		NIST
Inp	776.00		NIST
Inp	775.00		NIST
Inp	760.00		NIST
Inp	763.00		NIST
Inp	768.00		NIST
Inp	758.00		NIST
Inp	768.00		NIST
Inp	Outlier 800.00		NIST
Inp	762.00		NIST
Inp	761.00		NIST
Inp	767.00		NIST
Inp	767.00		NIST
Inp	744.00		NIST
Inp	749.00		NIST
Inp	747.00		NIST
Inp	745.00		NIST
Inp	744.00		NIST
Inp	744.00		NIST
Inp	747.00		NIST
Inp	774.00		NIST
Inp	Outlier 801.00		NIST
Inp	754.00		NIST
Inp	765.00		NIST
Inp	768.00		NIST
Inp	773.00		NIST
Inp	762.00		NIST
Inp	762.00		NIST
Inp	762.00		NIST
Inp	763.00		NIST
Inp	762.00		NIST
Inp	771.00		NIST
Inp	749.00		NIST
Inp	776.00		NIST
Inp	779.00		NIST
Inp	772.00		NIST
Inp	749.00		NIST
Inp	765.00		NIST
Inp	768.00		NIST
Inp	768.00		NIST
Inp	759.00		NIST
Inp	764.00		NIST
Inp	766.00		NIST
Inp	780.00		NIST
Inp	765.00		NIST
Inp	760.00		NIST
Inp	760.00		NIST
Inp	763.00		NIST
Inp	744.00		NIST
Inp	747.00		NIST
Inp	766.00		NIST
Inp	775.00		NIST
Inp	771.00		NIST
Inp	776.00		NIST
Inp	768.00		NIST
Inp	748.00		NIST
Inp	747.00		NIST
Inp	745.00		NIST
Inp	767.00		NIST
Inp	768.00		NIST
Inp	766.00		NIST
Inp	744.00		NIST
Inp	759.00		NIST
Inp	764.00		NIST
Inp	752.00		NIST
Inp	763.00		NIST
Inp	766.00		NIST
Inp	747.00		NIST
Inp	752.00		NIST
Inp	763.00		NIST
Inp	752.00		NIST
Inp	759.00		NIST
Inp	764.00		NIST
Inp	766.00		NIST
Inp	772.00		NIST
Inp	740.00		NIST
Inp	766.00		NIST
Inp	781.00		NIST
Inp	772.00		NIST
Inp	771.00		NIST
Inp	756.00		NIST
Inp	744.00		NIST
Inp	744.00		NIST
Inp	744.00		NIST
Inp	756.00		NIST
Inp	766.00		NIST
Inp	742.00		NIST
Inp	740.00		NIST
Inp	742.00		NIST
Inp	743.00		NIST
Inp	744.00		NIST
Inp	746.00		NIST
Inp	761.00		NIST
Inp	764.00		NIST
Inp	754.00		NIST
Inp	747.00		NIST
Inp	746.00		NIST
Inp	767.00		NIST
Inp	756.00		NIST
Inp	756.00		NIST
Inp	754.00		NIST
Inp	762.00		NIST
Inp	751.00		NIST
Inp	769.00		NIST
Inp	769.00		NIST
Inp	759.00		NIST
Inp	762.00		NIST
Inp	767.00		NIST
Inp	769.00		NIST
Inp	771.00		NIST
Inp	765.00		NIST
Inp	759.00		NIST
Inp	760.00		NIST
Inp	764.00		NIST
Inp	744.00		NIST
Inp	768.00		NIST
Inp	751.00		NIST
Inp	750.00		NIST
Inp	767.00		NIST
Inp	767.00		NIST
Inp	760.00		NIST
Inp	763.00		NIST
Inp	764.00		NIST
Inp	764.00		NIST
Inp	765.00		NIST
Inp	765.00		NIST
Inp	751.00		NIST
Inp	742.00		NIST
Inp	740.00		NIST
Inp	764.00		NIST
Inp	764.00		NIST
Inp	761.00		NIST
Inp	744.00		NIST
Inp	751.00		NIST
Inp	770.00		NIST
Inp	770.00		NIST
Inp	755.00		NIST
Inp	749.00		NIST
Inp	756.00		NIST
Inp	761.00		NIST
Inp	766.00		NIST
Inp	750.00		NIST
Inp	757.00		NIST
Inp	760.00		NIST
Inp	766.00		NIST
Inp	763.00		NIST
Inp	764.00		NIST
Inp	Outlier 787.00		NIST
Inp	Outlier 730.00		NIST
Inp	757.00		NIST
Inp	750.00		NIST
Inp	Outlier 723.00		NIST
Inp	753.00		NIST
Inp	760.00		NIST
Inp	758.00		NIST
Inp	758.00		NIST
Inp	753.00		NIST
Inp	763.00		NIST
Inp	744.00		NIST
Inp	744.00		NIST
Inp	764.00		NIST
Inp	756.00		NIST
Inp	746.00		NIST
Inp	766.00		NIST
Inp	772.00		NIST
Inp	764.00		NIST
Inp	756.00		NIST
Inp	744.10		NIST
Inp	735.00		NIST
Inp	753.00		NIST
Inp	768.00		NIST
Inp	780.00		NIST
Inp	766.00		NIST
Inp	763.00		NIST
Inp	754.00		NIST
Inp	762.00		NIST
Inp	749.00		NIST
Inp	765.00		NIST
Inp	771.00		NIST
Inp	745.00		NIST
Inp	759.00		NIST
Inp	747.00		NIST
Inp	781.00		NIST
Inp	744.00		NIST
Inp	740.00		NIST
Inp	761.00		NIST
Inp	767.00		NIST
Inp	758.00		NIST
Inp	773.00		NIST
Inp	770.00		NIST
I	[1200.00; 1294.00]
I	1256.00		NIST
I	1238.00		NIST
I	1263.00		NIST
I	Outlier 1288.00		NIST
I	Outlier 1210.00		NIST
I	1241.00		NIST
I	Outlier 1208.00		NIST
I	1226.00		NIST
I	1222.00		NIST
I	1255.00		NIST
I	1250.00		NIST
I	1218.00		NIST
I	1237.00		NIST
I	1245.00		NIST
I	1245.00		NIST
I	1257.00		NIST
I	1250.00		NIST
I	1242.00		NIST
I	1265.00		NIST
I	1217.00		NIST
I	1255.00		NIST
I	1256.00		NIST
I	1230.00		NIST
I	1271.00		NIST
I	1261.00		NIST
I	Outlier 1213.00		NIST
I	Outlier 1214.00		NIST
I	1220.00		NIST
I	1236.00		NIST
I	1230.00		NIST
I	1260.00		NIST
I	1256.00		NIST
I	1258.00		NIST
I	1252.00		NIST
I	1244.00		NIST
I	1258.00		NIST
I	1260.00		NIST
I	1254.00		NIST
I	1255.00		NIST
I	1252.00		NIST
I	1252.00		NIST
I	1255.00		NIST
I	1241.00		NIST
I	1242.00		NIST
I	1220.00		NIST
I	1238.00		NIST
I	1255.00		NIST
I	1262.00		NIST
I	1232.00		NIST
I	1261.00		NIST
I	1239.00		NIST
I	1249.00		NIST
I	1274.00		NIST
I	1274.00		NIST
I	1274.00		NIST
I	1238.00		NIST
I	1274.00		NIST
I	1233.00		NIST
I	1251.00		NIST
I	1238.00		NIST
I	1251.00		NIST
I	1245.00		NIST
I	1250.00		NIST
I	1256.00		NIST
I	1239.00		NIST
I	1250.00		NIST
I	1249.00		NIST
I	1258.00		NIST
I	1250.00		NIST
I	1250.00		NIST
I	1251.00		NIST
I	1250.00		NIST
I	1233.00		NIST
I	1264.00		NIST
I	Outlier 1294.00		NIST
I	1245.00		NIST
I	1241.00		NIST
I	1250.00		NIST
I	1248.00		NIST
I	Outlier 1292.00		NIST
I	1235.00		NIST
I	1249.00		NIST
I	1256.00		NIST
I	1252.00		NIST
I	1252.00		NIST
I	1256.00		NIST
I	1246.00		NIST
I	1236.00		NIST
I	Outlier 1206.00		NIST
I	1249.00		NIST
I	1241.00		NIST
I	1236.00		NIST
I	1250.00		NIST
I	1258.00		NIST
I	1260.00		NIST
I	1251.00		NIST
I	1255.00		NIST
I	1258.00		NIST
I	1236.00		NIST
I	Outlier 1216.00		NIST
I	1228.00		NIST
I	1262.00		NIST
I	1256.00		NIST
I	1253.00		NIST
I	1261.00		NIST
I	1262.00		NIST
I	1265.00		NIST
I	1232.00		NIST
I	1242.00		NIST
I	1240.00		NIST
I	1249.00		NIST
I	1240.00		NIST
I	1260.00		NIST
I	1249.00		NIST
I	1240.00		NIST
I	Outlier 1280.00		NIST
I	1231.00		NIST
I	1230.00		NIST
I	1241.00		NIST
I	1240.00		NIST
I	1253.00		NIST
I	1237.00		NIST
I	1260.00		NIST
I	Outlier 1206.00		NIST
I	1233.00		NIST
I	1244.00		NIST
I	1254.00		NIST
I	1255.00		NIST
I	1255.00		NIST
I	1237.00		NIST
I	1238.00		NIST
I	1259.00		NIST
I	1260.00		NIST
I	1272.00		NIST
I	1256.00		NIST
I	1257.00		NIST
I	1259.00		NIST
I	1259.00		NIST
I	1259.00		NIST
I	1250.00		NIST
I	1268.00		NIST
I	1268.00		NIST
I	1264.00		NIST
I	1255.00		NIST
I	1264.00		NIST
I	1244.00		NIST
I	1241.00		NIST
I	Outlier 1213.00		NIST
I	1255.00		NIST
I	1252.00		NIST
I	1255.00		NIST
I	1262.00		NIST
I	1248.00		NIST
I	1272.00		NIST
I	1238.00		NIST
I	1253.00		NIST
I	1275.00		NIST
I	1250.00		NIST
I	1248.00		NIST
I	1258.00		NIST
I	1253.00		NIST
I	1251.00		NIST
I	1244.00		NIST
I	1259.00		NIST
I	1233.00		NIST
I	Outlier 1285.00		NIST
I	1217.00		NIST
I	1276.00		NIST
I	1250.00		NIST
I	1235.00		NIST
I	1246.00		NIST
I	Outlier 1210.00		NIST
I	1250.00		NIST
I	1246.00		NIST
I	1259.00		NIST
I	1228.00		NIST
I	1246.00		NIST
I	1249.00		NIST
I	1260.00		NIST
I	1230.00		NIST
I	1252.00		NIST
I	1262.00		NIST
I	1244.00		NIST
I	1260.00		NIST
I	1257.00		NIST
I	1244.00		NIST
I	1231.00		NIST
I	1242.00		NIST
I	1243.00		NIST
I	1229.00		NIST
I	1231.00		NIST
I	1249.00		NIST
I	1232.00		NIST
I	1231.00		NIST
I	1238.00		NIST
I	Outlier 1213.00		NIST
I	1247.00		NIST
I	1247.00		NIST
I	1271.00		NIST
I	1245.00		NIST
I	1223.00		NIST
I	1224.00		NIST
I	1256.00		NIST
I	1256.00		NIST
I	1223.00		NIST
I	1224.00		NIST
I	1236.00		NIST
I	1230.00		NIST
I	1252.00		NIST
I	1249.00		NIST
I	1256.00		NIST
I	1256.00		NIST
I	1259.00		NIST
I	1265.00		NIST
I	1256.00		NIST
I	1262.00		NIST
I	1258.00		NIST
I	1231.00		NIST
I	1256.00		NIST
I	1262.00		NIST
I	1244.00		NIST
I	1242.00		NIST
I	1249.00		NIST
I	1255.00		NIST
I	1255.00		NIST
I	1256.00		NIST
I	1261.00		NIST
I	1258.00		NIST
I	1224.00		NIST
I	1253.00		NIST
I	1253.00		NIST
I	1241.00		NIST
I	1255.00		NIST
I	1253.00		NIST
I	1248.00		NIST
I	1239.00		NIST
I	1249.00		NIST
I	1255.00		NIST
I	1253.00		NIST
I	1250.00		NIST
I	1240.00		NIST
I	1253.00		NIST
I	1260.00		NIST
I	1255.00		NIST
I	1260.00		NIST
I	1252.00		NIST
I	1250.00		NIST
I	1248.00		NIST
I	1230.00		NIST
I	1245.00		NIST
I	1266.00		NIST
I	Outlier 1213.00		NIST
I	1243.00		NIST
I	1233.00		NIST
I	1270.00		NIST
I	1252.00		NIST
I	1252.00		NIST
I	1252.00		NIST
I	Outlier 1200.00		NIST
I	1236.00		NIST
I	1250.00		NIST
I	1247.00		NIST
I	Outlier 1213.00		NIST
I	1260.00		NIST
I	1255.00		NIST
I	1259.00		NIST
I	1264.00		NIST
I	Outlier 1213.00		NIST
I	1248.00		NIST
I	1250.00		NIST
I	1244.00		NIST
I	1276.00		NIST
I	1249.00		NIST
I	1242.00		NIST
I	1232.00		NIST
I	1247.00		NIST
I	1256.00		NIST
I	1230.00		NIST
I	1241.00		NIST
I	1257.00		NIST
I	1237.00		NIST
I	1252.00		NIST
I	1274.00		NIST
I	1251.00		NIST
I	Outlier 1206.00		NIST
I	1258.00		NIST
I	1236.00		NIST
S°gas	401.30	J/mol×K	NIST
S°liquid	[254.80; 258.90]	J/mol×K
S°liquid	258.90	J/mol×K	NIST
S°liquid	254.80	J/mol×K	NIST
Tboil	[273.28; 684.20]	K
Tboil	411.13	K	KDB
Tboil	411.15	K	Excess ...
Tboil	410.95	K	Liquid-...
Tboil	411.11	K	Isobari...
Tboil	410.78	K	Vapor-L...
Tboil	410.85	K	Vapor-L...
Tboil	411.10	K	Isobari...
Tboil	Outlier 684.20 ± 0.40	K	NIST
Tboil	410.90 ± 0.30	K	NIST
Tboil	410.20	K	NIST
Tboil	410.15 ± 0.40	K	NIST
Tboil	411.20	K	NIST
Tboil	392.40	K	NIST
Tboil	411.00 ± 0.30	K	NIST
Tboil	411.10 ± 0.08	K	NIST
Tboil	411.00 ± 0.50	K	NIST
Tboil	Outlier 273.28 ± 0.10	K	NIST
Tboil	410.80 ± 0.40	K	NIST
Tboil	411.20 ± 0.50	K	NIST
Tboil	411.20 ± 0.40	K	NIST
Tboil	411.15	K	NIST
Tboil	409.15 ± 3.00	K	NIST
Tboil	411.65 ± 0.50	K	NIST
Tboil	410.65 ± 3.00	K	NIST
Tboil	410.65 ± 0.50	K	NIST
Tboil	411.15 ± 0.50	K	NIST
Tboil	411.00 ± 0.50	K	NIST
Tboil	410.15 ± 0.70	K	NIST
Tboil	408.65 ± 2.00	K	NIST
Tboil	411.07 ± 0.20	K	NIST
Tboil	409.65 ± 1.00	K	NIST
Tboil	406.65 ± 3.00	K	NIST
Tboil	410.65 ± 0.50	K	NIST
Tboil	411.15 ± 0.50	K	NIST
Tboil	411.35 ± 0.50	K	NIST
Tboil	411.05 ± 1.00	K	NIST
Tboil	411.15 ± 0.50	K	NIST
Tboil	410.15 ± 1.00	K	NIST
Tboil	410.15 ± 1.00	K	NIST
Tboil	411.40 ± 0.50	K	NIST
Tboil	411.35 ± 0.50	K	NIST
Tboil	411.15 ± 0.50	K	NIST
Tboil	409.15 ± 3.00	K	NIST
Tboil	410.90 ± 0.50	K	NIST
Tboil	411.15 ± 1.00	K	NIST
Tboil	410.95 ± 0.50	K	NIST
Tboil	411.10 ± 0.50	K	NIST
Tboil	407.15 ± 3.00	K	NIST
Tboil	411.21 ± 0.05	K	NIST
Tboil	410.80 ± 0.20	K	NIST
Tboil	411.10 ± 0.10	K	NIST
Tboil	409.85 ± 0.50	K	NIST
Tboil	410.95 ± 0.30	K	NIST
Tboil	411.40 ± 0.10	K	NIST
Tboil	408.90 ± 1.50	K	NIST
Tboil	410.95 ± 0.30	K	NIST
Tboil	410.95 ± 0.50	K	NIST
Tboil	411.15 ± 0.07	K	NIST
Tboil	410.40 ± 0.30	K	NIST
Tboil	409.15 ± 2.00	K	NIST
Tboil	411.20 ± 0.20	K	NIST
Tboil	411.00 ± 0.50	K	NIST
Tboil	410.65 ± 1.00	K	NIST
Tboil	411.15 ± 1.00	K	NIST
Tboil	411.10 ± 0.20	K	NIST
Tboil	411.10 ± 0.10	K	NIST
Tboil	402.20 ± 0.50	K	NIST
Tboil	404.15 ± 4.00	K	NIST
Tboil	410.00 ± 3.00	K	NIST
Tboil	404.75 ± 3.00	K	NIST
Tboil	411.00 ± 1.00	K	NIST
Tboil	402.90 ± 1.00	K	NIST
Tboil	404.15 ± 3.00	K	NIST
Tboil	404.25 ± 3.00	K	NIST
Tc	[551.60; 588.50]	K
Tc	588.10	K	KDB
Tc	588.10 ± 0.50	K	NIST
Tc	588.00 ± 0.40	K	NIST
Tc	588.20 ± 0.50	K	NIST
Tc	588.50 ± 0.60	K	NIST
Tc	588.50 ± 0.60	K	NIST
Tc	588.00	K	NIST
Tc	587.70 ± 0.20	K	NIST
Tc	588.20	K	NIST
Tc	Outlier 551.60	K	NIST
Tc	588.11	K	NIST
Tfus	[194.20; 194.95]	K
Tfus	194.20	K	KDB
Tfus	194.68	K	Aq. Sol...
Tfus	194.95	K	NIST
Tfus	194.35 ± 0.30	K	NIST
Tfus	194.65 ± 0.50	K	NIST
Tfus	194.65 ± 0.50	K	NIST
Ttriple	[194.20; 195.56]	K
Ttriple	195.56	K	KDB
Ttriple	195.56 ± 0.02	K	NIST
Ttriple	194.20 ± 0.20	K	NIST
Vc	[0.326; 0.326]	m3/kmol
Vc	0.326	m3/kmol	KDB
Vc	0.326	m3/kmol	NIST
Zc	0.2598130		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[167.91; 221.40]	J/mol×K	[403.49; 573.95]
Cp,gas	167.91	J/mol×K	403.49	NIST
Cp,gas	177.70 ± 1.40	J/mol×K	418.95	NIST
Cp,gas	178.20 ± 1.40	J/mol×K	420.75	NIST
Cp,gas	174.58	J/mol×K	423.32	NIST
Cp,gas	179.70 ± 1.40	J/mol×K	426.15	NIST
Cp,gas	181.70 ± 1.40	J/mol×K	433.45	NIST
Cp,gas	179.33	J/mol×K	438.26	NIST
Cp,gas	184.40 ± 1.40	J/mol×K	442.85	NIST
Cp,gas	184.80 ± 1.40	J/mol×K	444.35	NIST
Cp,gas	184.35	J/mol×K	453.45	NIST
Cp,gas	192.90 ± 1.40	J/mol×K	472.85	NIST
Cp,gas	190.44	J/mol×K	473.19	NIST
Cp,gas	195.50 ± 1.40	J/mol×K	482.25	NIST
Cp,gas	209.30 ± 1.40	J/mol×K	531.25	NIST
Cp,gas	215.80 ± 1.40	J/mol×K	554.15	NIST
Cp,gas	221.40 ± 1.40	J/mol×K	573.95	NIST
Cp,liquid	[183.30; 240.60]	J/mol×K	[293.15; 313.20]
Cp,liquid	205.60	J/mol×K	293.15	NIST
Cp,liquid	209.12	J/mol×K	298.00	NIST
Cp,liquid	183.30	J/mol×K	298.00	NIST
Cp,liquid	207.45	J/mol×K	298.15	NIST
Cp,liquid	207.40	J/mol×K	298.15	NIST
Cp,liquid	208.98	J/mol×K	298.15	NIST
Cp,liquid	208.19	J/mol×K	298.15	NIST
Cp,liquid	208.40	J/mol×K	298.15	NIST
Cp,liquid	207.45	J/mol×K	298.15	NIST
Cp,liquid	208.30	J/mol×K	298.15	NIST
Cp,liquid	212.30	J/mol×K	301.26	NIST
Cp,liquid	201.70	J/mol×K	302.40	NIST
Cp,liquid	240.60	J/mol×K	313.20	NIST
η	[0.0006470; 0.0054170]	Pa×s	[283.15; 373.15]
η	0.0054170	Pa×s	283.15	Density...
η	0.0046820	Pa×s	288.15	Densiti...
η	0.0040601	Pa×s	293.15	Densiti...
η	0.0040290	Pa×s	293.15	Densiti...
η	0.0039740	Pa×s	293.15	Density...
η	0.0040300	Pa×s	293.15	Density...
η	0.0040250	Pa×s	293.15	Densiti...
η	0.0041170	Pa×s	293.15	Density...
η	0.0034580	Pa×s	298.15	Densiti...
η	0.0034940	Pa×s	298.15	Densiti...
η	0.0035344	Pa×s	298.15	Densiti...
η	0.0035560	Pa×s	298.15	Density...
η	0.0034970	Pa×s	298.15	Densiti...
η	0.0034800	Pa×s	298.15	Density...
η	0.0034410	Pa×s	298.15	Density...
η	0.0030600	Pa×s	303.15	Density...
η	0.0030582	Pa×s	303.15	Densiti...
η	0.0030200	Pa×s	303.15	Density...
η	0.0030220	Pa×s	303.15	Densiti...
η	0.0030070	Pa×s	303.15	Densiti...
η	0.0029900	Pa×s	303.15	Density...
η	0.0026250	Pa×s	308.15	Densiti...
η	0.0022995	Pa×s	313.15	Densiti...
η	0.0023120	Pa×s	313.15	Densiti...
η	0.0023320	Pa×s	313.15	Density...
η	0.0022630	Pa×s	313.15	Density...
η	0.0023170	Pa×s	313.15	Densiti...
η	0.0023150	Pa×s	313.15	Density...
η	0.0020290	Pa×s	318.15	Densiti...
η	0.0018010	Pa×s	323.15	Density...
η	0.0018220	Pa×s	323.15	Density...
η	0.0017950	Pa×s	323.15	Densiti...
η	0.0014250	Pa×s	333.15	Density...
η	0.0014400	Pa×s	333.15	Density...
η	0.0011460	Pa×s	343.15	Density...
η	0.0011460	Pa×s	343.15	Density...
η	0.0009310	Pa×s	353.15	Density...
η	0.0009350	Pa×s	353.15	Density...
η	0.0007670	Pa×s	363.15	Density...
η	0.0007720	Pa×s	363.15	Density...
η	0.0006470	Pa×s	373.15	Density...
ΔfusH	[9.83; 10.51]	kJ/mol	[194.20; 195.60]
ΔfusH	9.83	kJ/mol	194.20	NIST
ΔfusH	10.50	kJ/mol	195.56	NIST
ΔfusH	10.51	kJ/mol	195.60	NIST
ΔfusH	10.50	kJ/mol	195.60	NIST
ΔfusH	10.50	kJ/mol	195.60	NIST
ΔvapH	[7.10; 56.20]	kJ/mol	[313.00; 586.00]
ΔvapH	55.70 ± 0.20	kJ/mol	313.00	NIST
ΔvapH	54.40 ± 0.20	kJ/mol	328.00	NIST
ΔvapH	53.00 ± 0.20	kJ/mol	343.00	NIST
ΔvapH	51.20 ± 0.20	kJ/mol	358.00	NIST
ΔvapH	56.20	kJ/mol	359.00	NIST
ΔvapH	55.00	kJ/mol	360.50	NIST
ΔvapH	50.50 ± 0.10	kJ/mol	362.00	NIST
ΔvapH	54.30	kJ/mol	368.50	NIST
ΔvapH	51.50	kJ/mol	372.50	NIST
ΔvapH	49.20 ± 0.10	kJ/mol	374.00	NIST
ΔvapH	51.60	kJ/mol	388.00	NIST
ΔvapH	47.00 ± 0.10	kJ/mol	392.00	NIST
ΔvapH	41.40	kJ/mol	392.40	NIST
ΔvapH	47.20	kJ/mol	404.00	NIST
ΔvapH	44.35	kJ/mol	410.90	KDB
ΔvapH	44.40 ± 0.10	kJ/mol	411.00	NIST
ΔvapH	44.40	kJ/mol	411.00	NIST
ΔvapH	44.36	kJ/mol	411.20	NIST
ΔvapH	45.40	kJ/mol	424.50	NIST
ΔvapH	40.10	kJ/mol	448.00	NIST
ΔvapH	36.10	kJ/mol	473.00	NIST
ΔvapH	31.70	kJ/mol	498.00	NIST
ΔvapH	26.40	kJ/mol	523.00	NIST
ΔvapH	22.00	kJ/mol	548.00	NIST
ΔvapH	14.10	kJ/mol	573.00	NIST
ΔvapH	7.10	kJ/mol	586.00	NIST
ν	[0.0000029; 0.0000050]	m2/s	[293.15; 313.15]
ν	0.0000050	m2/s	293.15	Densiti...
ν	0.0000044	m2/s	295.15	Densiti...
ν	0.0000042	m2/s	298.15	Densiti...
ν	0.0000039	m2/s	300.15	Densiti...
ν	0.0000036	m2/s	303.15	Densiti...
ν	0.0000037	m2/s	303.15	Densiti...
ν	0.0000035	m2/s	305.15	Densiti...
ν	0.0000031	m2/s	308.15	Densiti...
ν	0.0000029	m2/s	313.15	Densiti...
Pvap	[0.34; 113.30]	kPa	[298.15; 414.65]
Pvap	0.34	kPa	298.15	Vapor P...
Pvap	0.49	kPa	303.15	Vapor P...
Pvap	0.69	kPa	308.15	Vapor P...
Pvap	0.91	kPa	313.15	Charact...
Pvap	0.97	kPa	313.15	Vapor P...
Pvap	0.90	kPa	313.15	Vapour-...
Pvap	1.36	kPa	318.15	Vapor P...
Pvap	1.87	kPa	323.15	Vapor P...
Pvap	2.53	kPa	328.15	Vapor P...
Pvap	3.38	kPa	333.15	Vapor P...
Pvap	4.47	kPa	338.15	Vapor P...
Pvap	5.87	kPa	343.15	Vapor P...
Pvap	7.63	kPa	348.15	Vapor P...
Pvap	9.83	kPa	353.15	Vapor P...
Pvap	12.52	kPa	358.15	Vapor P...
Pvap	15.81	kPa	363.15	Vapor P...
Pvap	19.86	kPa	368.15	Vapor P...
Pvap	24.68	kPa	373.15	Vapor P...
Pvap	30.47	kPa	378.15	Vapor P...
Pvap	31.30	kPa	379.35	Isobari...
Pvap	35.30	kPa	382.40	Isobari...
Pvap	37.36	kPa	383.15	Vapor P...
Pvap	40.00	kPa	384.45	Low-Pre...
Pvap	40.01	kPa	384.85	Low-Pre...
Pvap	40.00	kPa	385.65	Isobari...
Pvap	45.45	kPa	388.15	Vapor P...
Pvap	49.20	kPa	390.75	Isobari...
Pvap	54.41	kPa	392.76	Low-Pre...
Pvap	54.88	kPa	393.15	Vapor P...
Pvap	56.90	kPa	394.70	Isobari...
Pvap	66.15	kPa	398.11	Low-Pre...
Pvap	65.84	kPa	398.15	Vapor P...
Pvap	69.30	kPa	400.05	Isobari...
Pvap	72.93	kPa	400.95	Low-Pre...
Pvap	78.45	kPa	403.15	Vapor P...
Pvap	82.75	kPa	404.59	Low-Pre...
Pvap	81.30	kPa	404.60	Isobari...
Pvap	90.21	kPa	407.17	Low-Pre...
Pvap	94.50	kPa	409.00	Isobari...
Pvap	101.20	kPa	410.73	Low-Pre...
Pvap	101.90	kPa	411.35	Isobari...
Pvap	113.30	kPa	414.65	Isobari...
n0	[1.39776; 1.41192]		[288.15; 323.15]
n0	1.41192		288.15	Experim...
n0	1.41040		293.00	Quatern...
n0	1.40900		293.10	Viscosi...
n0	1.40980		293.13	Isobari...
n0	1.40980		293.13	Isobari...
n0	1.40980		293.15	Isobari...
n0	1.40995		293.15	Excess ...
n0	1.40980		293.15	Experim...
n0	1.40976		293.15	Densiti...
n0	1.40920		293.15	Measure...
n0	1.40980		293.15	Isobari...
n0	1.40980		293.15	Isobari...
n0	1.40994		293.15	Experim...
n0	1.40995		293.15	Densiti...
n0	1.41000		293.15	Isother...
n0	1.40980		293.15	ERAS mo...
n0	1.40970		293.20	Vapor L...
n0	1.41000		293.20	Liquid-...
n0	1.40970		293.20	Vapor L...
n0	1.40730		298.15	Thermod...
n0	1.40784		298.15	Thermop...
n0	1.40680		298.15	Densiti...
n0	1.40850		298.15	Compara...
n0	1.40770		298.15	Isobari...
n0	1.40780		298.15	Mixing ...
n0	1.40780		298.15	Excess ...
n0	1.40970		298.15	Investi...
n0	1.40941		298.15	Atmosph...
n0	1.40774		298.15	Effect ...
n0	1.40797		298.15	Experim...
n0	1.40710		298.15	Liquid-...
n0	1.40730		298.15	Thermod...
n0	1.40850		298.15	Bubble ...
n0	1.40780		298.15	Excess ...
n0	1.40796		298.15	Experim...
n0	1.40703		298.15	Liquid ...
n0	1.40770		298.15	Isobari...
n0	1.40770		298.15	Density...
n0	1.40860		298.15	Excess ...
n0	1.40880		298.15	Excess ...
n0	1.40780		298.15	Effect ...
n0	1.40770		298.15	Liquid-...
n0	1.40890		298.15	Excess ...
n0	1.40800		298.15	Density...
n0	1.40800		298.15	Vapor l...
n0	1.40764		298.20	Vapor-L...
n0	1.40730		298.20	Tie lin...
n0	1.40592		303.15	Densiti...
n0	1.40690		303.15	Compara...
n0	1.40592		303.15	Densiti...
n0	1.40500		303.15	Thermod...
n0	1.40595		303.15	Experim...
n0	1.40500		303.15	Thermod...
n0	1.40388		308.15	Experim...
n0	1.40590		308.15	Compara...
n0	1.40310		308.15	Densiti...
n0	1.40320		308.15	Thermod...
n0	1.40320		308.15	Thermod...
n0	1.40390		313.15	Compara...
n0	1.40189		313.15	Experim...
n0	1.40178		313.15	Thermop...
n0	1.39987		318.15	Experim...
n0	1.40030		318.15	Mixing ...
n0	1.39960		318.15	Densiti...
n0	1.39776		323.15	Experim...
ρl	[759.77; 822.42]	kg/m3	[283.15; 363.15]
ρl	821.79	kg/m3	283.15	Excess ...
ρl	822.42	kg/m3	283.15	Volumet...
ρl	821.95	kg/m3	283.15	Densiti...
ρl	821.81	kg/m3	283.15	Excess ...
ρl	821.90	kg/m3	283.15	Densiti...
ρl	818.56	kg/m3	288.15	Densiti...
ρl	819.15	kg/m3	288.15	Excess ...
ρl	818.30	kg/m3	288.15	Tempera...
ρl	818.34	kg/m3	288.15	Thermod...
ρl	818.59	kg/m3	288.15	Densiti...
ρl	818.30	kg/m3	288.15	Densiti...
ρl	818.79	kg/m3	288.15	Volumet...
ρl	818.28	kg/m3	288.15	Influen...
ρl	818.80	kg/m3	288.15	Excess ...
ρl	815.00	kg/m3	293.00	KDB
ρl	814.60	kg/m3	293.00	Fluid-P...
ρl	814.68	kg/m3	293.15	Densiti...
ρl	814.89	kg/m3	293.15	Densiti...
ρl	814.59	kg/m3	293.15	Volumet...
ρl	814.81	kg/m3	293.15	Thermod...
ρl	814.60	kg/m3	293.15	Densiti...
ρl	814.50	kg/m3	293.15	Correla...
ρl	814.63	kg/m3	293.15	Influen...
ρl	815.13	kg/m3	293.15	Volumet...
ρl	814.53	kg/m3	293.15	Osmotic...
ρl	814.80	kg/m3	293.15	Excess ...
ρl	814.92	kg/m3	293.15	Densiti...
ρl	810.90	kg/m3	298.00	Fluid-P...
ρl	811.00	kg/m3	298.00	Compara...
ρl	810.93	kg/m3	298.15	Volumet...
ρl	811.10	kg/m3	298.15	Tempera...
ρl	811.47	kg/m3	298.15	Excess ...
ρl	810.88	kg/m3	298.15	Physica...
ρl	810.88	kg/m3	298.15	Excess ...
ρl	810.84	kg/m3	298.15	Study o...
ρl	811.00	kg/m3	298.15	Volumet...
ρl	811.80	kg/m3	298.15	Excess ...
ρl	810.90	kg/m3	298.15	Dynamic...
ρl	810.93	kg/m3	298.15	Densiti...
ρl	810.82	kg/m3	298.15	FT-IR s...
ρl	811.00	kg/m3	298.15	Thermod...
ρl	811.03	kg/m3	298.15	Densiti...
ρl	810.97	kg/m3	298.15	Influen...
ρl	810.12	kg/m3	298.15	Isobari...
ρl	810.89	kg/m3	298.15	Excess ...
ρl	810.83	kg/m3	298.15	Densiti...
ρl	811.10	kg/m3	298.15	The stu...
ρl	811.10	kg/m3	298.15	Surface...
ρl	811.04	kg/m3	298.15	Densiti...
ρl	811.40	kg/m3	298.15	Thermod...
ρl	811.26	kg/m3	298.15	Densiti...
ρl	811.14	kg/m3	298.15	Thermod...
ρl	810.82	kg/m3	298.15	Excess ...
ρl	810.80	kg/m3	298.15	Correla...
ρl	811.45	kg/m3	298.15	Volumet...
ρl	811.04	kg/m3	298.15	Vapor-l...
ρl	810.88	kg/m3	298.15	Excess ...
ρl	810.90	kg/m3	298.15	Excess ...
ρl	810.90	kg/m3	298.15	Excess ...
ρl	811.23	kg/m3	298.15	Densiti...
ρl	811.29	kg/m3	298.20	Liquid-...
ρl	807.00	kg/m3	303.00	Compara...
ρl	807.30	kg/m3	303.00	Fluid-P...
ρl	807.24	kg/m3	303.15	Volumet...
ρl	807.37	kg/m3	303.15	Densiti...
ρl	807.11	kg/m3	303.15	Volumet...
ρl	807.25	kg/m3	303.15	Densiti...
ρl	807.46	kg/m3	303.15	Thermod...
ρl	807.07	kg/m3	303.15	Excess ...
ρl	807.10	kg/m3	303.15	Correla...
ρl	807.74	kg/m3	303.15	Volumet...
ρl	807.55	kg/m3	303.15	Densiti...
ρl	807.57	kg/m3	303.15	Densiti...
ρl	810.00	kg/m3	303.15	Study o...
ρl	807.10	kg/m3	303.15	FT-IR s...
ρl	807.28	kg/m3	303.15	Influen...
ρl	803.00	kg/m3	308.00	Compara...
ρl	803.67	kg/m3	308.15	Densiti...
ρl	804.01	kg/m3	308.15	Volumet...
ρl	803.52	kg/m3	308.15	Osmotic...
ρl	803.38	kg/m3	308.15	FT-IR s...
ρl	803.68	kg/m3	308.15	Densiti...
ρl	803.70	kg/m3	308.15	Excess ...
ρl	804.10	kg/m3	308.15	Tempera...
ρl	803.70	kg/m3	308.15	The stu...
ρl	803.74	kg/m3	308.15	Thermod...
ρl	803.53	kg/m3	308.15	Volumet...
ρl	803.86	kg/m3	308.15	Densiti...
ρl	803.83	kg/m3	308.15	Densiti...
ρl	803.50	kg/m3	308.15	Physica...
ρl	803.30	kg/m3	308.15	Thermod...
ρl	803.30	kg/m3	308.15	Correla...
ρl	803.56	kg/m3	308.15	Influen...
ρl	800.00	kg/m3	313.00	Compara...
ρl	799.82	kg/m3	313.15	Influen...
ρl	800.57	kg/m3	313.15	Excess ...
ρl	800.08	kg/m3	313.15	Densiti...
ρl	800.11	kg/m3	313.15	Densiti...
ρl	799.79	kg/m3	313.15	Volumet...
ρl	800.26	kg/m3	313.15	Excess ...
ρl	799.71	kg/m3	313.15	Excess ...
ρl	799.60	kg/m3	313.15	Correla...
ρl	799.94	kg/m3	313.15	Densiti...
ρl	799.90	kg/m3	313.15	Densiti...
ρl	799.40	kg/m3	313.15	Excess ...
ρl	799.80	kg/m3	313.15	Excess ...
ρl	800.24	kg/m3	313.15	Volumet...
ρl	799.99	kg/m3	313.15	Thermod...
ρl	796.32	kg/m3	318.15	Densiti...
ρl	796.43	kg/m3	318.15	Volumet...
ρl	796.17	kg/m3	318.15	Densiti...
ρl	796.10	kg/m3	318.15	The stu...
ρl	796.03	kg/m3	318.15	Volumet...
ρl	795.98	kg/m3	318.15	Physica...
ρl	796.29	kg/m3	318.15	Densiti...
ρl	795.80	kg/m3	318.15	Correla...
ρl	792.48	kg/m3	323.15	Densiti...
ρl	792.15	kg/m3	323.15	Osmotic...
ρl	792.46	kg/m3	323.15	Densiti...
ρl	792.14	kg/m3	323.15	Osmotic...
ρl	792.23	kg/m3	323.15	Volumet...
ρl	792.57	kg/m3	323.15	Volumet...
ρl	792.36	kg/m3	323.15	Densiti...
ρl	792.00	kg/m3	323.15	Correla...
ρl	789.01	kg/m3	328.15	Excess ...
ρl	788.50	kg/m3	328.15	Densiti...
ρl	788.74	kg/m3	328.15	Excess ...
ρl	788.61	kg/m3	328.15	Densiti...
ρl	788.67	kg/m3	328.15	Volumet...
ρl	788.82	kg/m3	328.15	Excess ...
ρl	788.40	kg/m3	328.15	The stu...
ρl	788.56	kg/m3	328.15	Densiti...
ρl	784.72	kg/m3	333.15	Volumet...
ρl	784.59	kg/m3	333.15	Densiti...
ρl	784.66	kg/m3	333.15	Densiti...
ρl	780.70	kg/m3	338.15	Densiti...
ρl	781.05	kg/m3	338.15	Excess ...
ρl	780.62	kg/m3	338.15	Densiti...
ρl	776.58	kg/m3	343.15	Densiti...
ρl	772.49	kg/m3	348.15	Densiti...
ρl	772.87	kg/m3	348.15	Excess ...
ρl	768.33	kg/m3	353.15	Densiti...
ρl	764.08	kg/m3	358.15	Densiti...
ρl	759.77	kg/m3	363.15	Densiti...
D*i	[0.00; 0.00]	m2/s	[253.13; 364.73]
D*i	0.00	m2/s	253.13	Viscous...
D*i	0.00	m2/s	253.19	Viscous...
D*i	0.00	m2/s	258.42	Viscous...
D*i	0.00	m2/s	258.47	Viscous...
D*i	0.00	m2/s	263.25	Viscous...
D*i	0.00	m2/s	263.28	Viscous...
D*i	0.00	m2/s	268.65	Viscous...
D*i	0.00	m2/s	268.66	Viscous...
D*i	0.00	m2/s	278.40	Viscous...
D*i	0.00	m2/s	278.43	Viscous...
D*i	0.00	m2/s	288.31	Viscous...
D*i	0.00	m2/s	288.33	Viscous...
D*i	0.00	m2/s	298.16	Viscous...
D*i	0.00	m2/s	298.17	Viscous...
D*i	0.00	m2/s	298.19	Viscous...
D*i	0.00	m2/s	298.21	Viscous...
D*i	0.00	m2/s	298.21	Viscous...
D*i	0.00	m2/s	298.27	Viscous...
D*i	0.00	m2/s	298.27	Viscous...
D*i	0.00	m2/s	308.09	Viscous...
D*i	0.00	m2/s	308.11	Viscous...
D*i	0.00	m2/s	318.08	Viscous...
D*i	0.00	m2/s	318.09	Viscous...
D*i	0.00	m2/s	323.10	Viscous...
D*i	0.00	m2/s	323.10	Viscous...
D*i	0.00	m2/s	323.15	Viscous...
D*i	0.00	m2/s	323.15	Viscous...
D*i	0.00	m2/s	327.86	Viscous...
D*i	0.00	m2/s	327.86	Viscous...
D*i	0.00	m2/s	337.71	Viscous...
D*i	0.00	m2/s	337.74	Viscous...
D*i	0.00	m2/s	347.21	Viscous...
D*i	0.00	m2/s	347.25	Viscous...
D*i	0.00	m2/s	352.35	Viscous...
D*i	0.00	m2/s	352.36	Viscous...
D*i	0.00	m2/s	352.55	Viscous...
D*i	0.00	m2/s	364.52	Viscous...
D*i	0.00	m2/s	364.59	Viscous...
D*i	0.00	m2/s	364.73	Viscous...
ΔfusS	[50.61; 53.70]	J/mol×K	[194.20; 195.56]
ΔfusS	50.61	J/mol×K	194.20	NIST
ΔfusS	53.70	J/mol×K	195.56	NIST
csound,fluid	[1192.80; 1325.90]	m/s	[283.15; 323.15]
csound,fluid	1325.90	m/s	283.15	Excess ...
csound,fluid	1312.50	m/s	288.15	Densiti...
csound,fluid	1292.50	m/s	293.15	Acousti...
csound,fluid	1293.45	m/s	293.15	Densiti...
csound,fluid	1276.01	m/s	298.15	Densiti...
csound,fluid	1274.00	m/s	298.15	Densiti...
csound,fluid	1274.10	m/s	298.15	Excess ...
csound,fluid	1281.20	m/s	298.15	Ultraso...
csound,fluid	1274.32	m/s	298.15	Densiti...
csound,fluid	1258.25	m/s	303.15	Densiti...
csound,fluid	1243.67	m/s	308.15	Densiti...
csound,fluid	1240.00	m/s	308.15	Densiti...
csound,fluid	1242.40	m/s	308.15	Acousti...
csound,fluid	1225.50	m/s	313.15	Excess ...
csound,fluid	1192.80	m/s	323.15	Acousti...
γ	[0.02; 0.03]	N/m	[293.15; 323.15]
γ	0.03	N/m	293.15	Density...
γ	0.03	N/m	293.15	The add...
γ	0.03	N/m	293.15	Surface...
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	298.15	Surface...
γ	0.03	N/m	298.15	Surface...
γ	0.02	N/m	298.15	The add...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.15	The add...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	The add...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	313.15	The add...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	The add...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	323.15	Surface...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	323.20	K	1.70	NIST

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	814.7
293.15	10000.00	821.1
293.15	20000.00	827.3
293.15	30000.00	833.2
293.15	40000.00	838.6
293.15	50000.00	843.6
293.15	60000.00	848.5
293.15	70000.00	853.1
293.15	80000.00	857.4
293.15	90000.00	861.7
293.15	100000.00	865.8
293.15	110000.00	869.6
293.15	120000.00	873.2
293.15	130000.00	876.9
293.15	140000.00	880.3
303.15	100.00	807.3
303.15	10000.00	814.4
303.15	20000.00	820.7
303.15	30000.00	826.7
303.15	40000.00	832.2
303.15	50000.00	837.5
303.15	60000.00	842.4
303.15	70000.00	847.0
303.15	80000.00	851.6
303.15	90000.00	855.8
303.15	100000.00	860.1
303.15	110000.00	864.1
303.15	120000.00	868.0
303.15	130000.00	871.7
303.15	140000.00	875.2
313.15	100.00	799.8
313.15	10000.00	807.4
313.15	20000.00	814.1
313.15	30000.00	820.2
313.15	40000.00	826.0
313.15	50000.00	831.5
313.15	60000.00	836.6
313.15	70000.00	841.4
313.15	80000.00	846.1
313.15	90000.00	850.5
313.15	100000.00	854.8
313.15	110000.00	858.9
313.15	120000.00	862.8
313.15	130000.00	866.6
313.15	140000.00	870.2
323.15	100.00	792.5
323.15	10000.00	800.3
323.15	20000.00	807.3
323.15	30000.00	813.7
323.15	40000.00	819.8
323.15	50000.00	825.4
323.15	60000.00	830.7
323.15	70000.00	835.7
323.15	80000.00	840.4
323.15	90000.00	845.0
323.15	100000.00	849.3
323.15	110000.00	853.6
323.15	120000.00	857.6
323.15	130000.00	861.5
323.15	140000.00	865.3
333.15	100.00	784.4
333.15	10000.00	792.7
333.15	20000.00	800.1
333.15	30000.00	806.8
333.15	40000.00	813.1
333.15	50000.00	818.9
333.15	60000.00	824.4
333.15	70000.00	829.7
333.15	80000.00	834.6
333.15	90000.00	839.2
333.15	100000.00	843.7
333.15	110000.00	848.0
333.15	120000.00	852.1
333.15	130000.00	856.0
333.15	140000.00	860.0
343.15	100.00	776.5
343.15	10000.00	785.2
343.15	20000.00	792.9
343.15	30000.00	799.9
343.15	40000.00	806.6
343.15	50000.00	812.6
343.15	60000.00	818.3
343.15	70000.00	823.7
343.15	80000.00	828.7
343.15	90000.00	833.5
343.15	100000.00	838.2
343.15	110000.00	842.5
343.15	120000.00	846.8
343.15	130000.00	850.9
343.15	140000.00	854.8
353.15	100.00	768.1
353.15	10000.00	777.3
353.15	20000.00	785.6
353.15	30000.00	792.9
353.15	40000.00	799.8
353.15	50000.00	806.1
353.15	60000.00	812.0
353.15	70000.00	817.6
353.15	80000.00	822.8
353.15	90000.00	827.8
353.15	100000.00	832.6
353.15	110000.00	837.2
353.15	120000.00	841.6
353.15	130000.00	845.8
353.15	140000.00	849.7
363.15	100.00	759.4
363.15	10000.00	769.2
363.15	20000.00	777.7
363.15	30000.00	785.6
363.15	40000.00	792.6
363.15	50000.00	799.2
363.15	60000.00	805.5
363.15	70000.00	811.3
363.15	80000.00	816.7
363.15	90000.00	821.8
363.15	100000.00	826.8
363.15	110000.00	831.3
363.15	120000.00	835.8
363.15	130000.00	840.1
363.15	140000.00	844.2
373.15	100.00	750.7
373.15	10000.00	761.2
373.15	20000.00	770.3
373.15	30000.00	778.2
373.15	40000.00	785.7
373.15	50000.00	792.5
373.15	60000.00	798.9
373.15	70000.00	804.9
373.15	80000.00	810.5
373.15	90000.00	815.8
373.15	100000.00	820.9
373.15	110000.00	825.7
373.15	120000.00	830.3
373.15	130000.00	834.7
373.15	140000.00	839.0
383.15	100.00	741.5
383.15	10000.00	752.3
383.15	20000.00	761.9
383.15	30000.00	770.7
383.15	40000.00	778.5
383.15	50000.00	785.7
383.15	60000.00	792.3
383.15	70000.00	798.5
383.15	80000.00	804.3
383.15	90000.00	809.7
383.15	100000.00	815.0
383.15	110000.00	819.9
383.15	120000.00	824.7
383.15	130000.00	829.2
383.15	140000.00	833.5
393.15	100.00	731.7
393.15	10000.00	743.4
393.15	20000.00	753.7
393.15	30000.00	762.8
393.15	40000.00	771.0
393.15	50000.00	778.6
393.15	60000.00	785.6
393.15	70000.00	792.0
393.15	80000.00	798.1
393.15	90000.00	803.7
393.15	100000.00	809.1
393.15	110000.00	814.2
393.15	120000.00	819.1
393.15	130000.00	823.7
393.15	140000.00	828.1
403.15	100.00	721.7
403.15	10000.00	734.4
403.15	20000.00	745.3
403.15	30000.00	754.9
403.15	40000.00	763.4
403.15	50000.00	771.3
403.15	60000.00	778.4
403.15	70000.00	785.1
403.15	80000.00	791.3
403.15	90000.00	797.2
403.15	100000.00	802.8
403.15	110000.00	808.0
403.15	120000.00	813.0
403.15	130000.00	817.8
403.15	140000.00	822.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	810.8
Reference

Fixed		Measured
Temperature, K - Fluid (supercritical or subcritical phases)	Pressure, kPa - Fluid (supercritical or subcritical phases)	Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
312.96	512.00	799.65
312.96	1022.00	800.04
312.96	1998.00	800.77
312.96	3005.00	801.53
312.96	4003.00	802.28
312.96	5002.00	803.02
312.96	6018.00	803.76
312.96	6994.00	804.49
312.96	8008.00	805.21
312.96	9005.00	805.93
312.96	10008.00	806.66
312.96	11008.00	807.37
312.96	12000.00	808.07
312.96	13024.00	808.78
312.96	13987.00	809.45
312.96	15014.00	810.14
312.96	15991.00	810.8
312.96	17019.00	811.48
312.96	17991.00	812.12
312.96	19007.00	812.79
312.96	19992.00	813.44
312.96	21031.00	814.1
312.96	22041.00	814.76
312.96	23014.00	815.41
312.96	24003.00	816.04
312.96	25037.00	816.73
322.89	520.00	792.06
322.89	1010.00	792.47
322.89	2005.00	793.27
322.89	3007.00	794.07
322.89	4005.00	794.86
322.89	5018.00	795.63
322.89	6001.00	796.42
322.89	7016.00	797.2
322.89	8020.00	797.97
322.89	8997.00	798.71
322.89	10001.00	799.47
322.89	11005.00	800.21
322.89	11996.00	800.95
322.89	13002.00	801.68
322.89	14013.00	802.4
322.89	15005.00	803.11
322.89	16014.00	803.82
322.89	17001.00	804.51
322.89	18016.00	805.21
322.89	19012.00	805.89
322.89	19992.00	806.56
322.89	21036.00	807.26
322.89	22003.00	807.92
322.89	23024.00	808.61
322.89	23994.00	809.26
322.89	25023.00	810.0
332.79	493.00	784.29
332.79	1014.00	784.76
332.79	2006.00	785.61
332.79	3025.00	786.48
332.79	4011.00	787.28
332.79	5020.00	788.11
332.79	6003.00	788.91
332.79	6997.00	789.73
332.79	8009.00	790.54
332.79	8995.00	791.31
332.79	9996.00	792.12
332.79	11018.00	792.9
332.79	11995.00	793.66
332.79	13023.00	794.45
332.79	13999.00	795.19
332.79	15010.00	795.95
332.79	16028.00	796.68
332.79	17003.00	797.41
332.79	18040.00	798.14
332.79	19004.00	798.84
332.79	20035.00	799.59
332.79	21024.00	800.29
332.79	21993.00	800.97
332.79	23039.00	801.71
332.79	24015.00	802.4
332.79	25022.00	803.12
342.76	505.00	776.31
342.76	997.00	776.77
342.76	1995.00	777.69
342.76	3011.00	778.59
342.76	4012.00	779.47
342.76	5011.00	780.34
342.76	6011.00	781.22
342.76	7003.00	782.03
342.76	8015.00	782.91
342.76	9000.00	783.73
342.76	10019.00	784.58
342.76	11020.00	785.4
342.76	12002.00	786.2
342.76	13016.00	787.02
342.76	14024.00	787.81
342.76	15002.00	788.59
342.76	16007.00	789.36
342.76	17037.00	790.15
342.76	17988.00	790.87
342.76	19037.00	791.66
342.76	20003.00	792.38
342.76	21015.00	793.14
342.76	22019.00	793.88
342.76	23039.00	794.62
342.76	24027.00	795.36
342.76	25028.00	796.1
352.71	508.00	768.15
352.71	1011.00	768.66
352.71	1995.00	769.61
352.71	3014.00	770.57
352.71	3998.00	771.49
352.71	5022.00	772.45
352.71	6012.00	773.35
352.71	7006.00	774.26
352.71	8024.00	775.17
352.71	9005.00	776.05
352.71	10016.00	776.94
352.71	11026.00	777.81
352.71	12001.00	778.65
352.71	13002.00	779.5
352.71	14026.00	780.35
352.71	15000.00	781.18
352.71	16005.00	781.98
352.71	17023.00	782.81
352.71	18003.00	783.59
352.71	19049.00	784.43
352.71	20035.00	785.2
352.71	21002.00	785.96
352.71	21995.00	786.73
352.71	23020.00	787.52
352.71	24045.00	788.32
352.71	25009.00	789.05
362.59	517.00	759.7
362.59	1023.00	760.25
362.59	2005.00	761.26
362.59	3010.00	762.29
362.59	3998.00	763.28
362.59	5006.00	764.25
362.59	6013.00	765.23
362.59	7014.00	766.21
362.59	8007.00	767.16
362.59	9020.00	768.1
362.59	10006.00	769.02
362.59	10991.00	769.93
362.59	12025.00	770.87
362.59	13008.00	771.76
362.59	13998.00	772.62
362.59	15017.00	773.51
362.59	16000.00	774.37
362.59	17013.00	775.24
362.59	18032.00	776.11
362.59	19003.00	776.9
362.59	20030.00	777.77
362.59	20987.00	778.55
362.59	22033.00	779.4
362.59	23000.00	780.2
362.59	24031.00	781.02
362.59	25026.00	781.82
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	825.2
278.15	1000.00	825.8
278.15	5000.00	828.5
278.15	10000.00	831.6
278.15	15000.00	834.7
278.15	20000.00	837.6
278.15	25000.00	840.4
278.15	30000.00	843.2
278.15	35000.00	845.9
278.15	40000.00	848.6
278.15	45000.00	851.1
278.15	50000.00	853.6
278.15	55000.00	856.1
278.15	60000.00	858.4
288.15	100.00	818.0
288.15	1000.00	818.7
288.15	5000.00	821.5
288.15	10000.00	824.8
288.15	15000.00	828.0
288.15	20000.00	831.1
288.15	25000.00	834.0
288.15	30000.00	836.9
288.15	35000.00	839.7
288.15	40000.00	842.4
288.15	45000.00	845.0
288.15	50000.00	847.6
288.15	55000.00	850.1
288.15	60000.00	852.5
298.15	100.00	810.7
298.15	1000.00	811.3
298.15	5000.00	814.2
298.15	10000.00	817.7
298.15	15000.00	821.0
298.15	20000.00	824.3
298.15	25000.00	827.3
298.15	30000.00	830.3
298.15	35000.00	833.2
298.15	40000.00	836.0
298.15	45000.00	838.7
298.15	50000.00	841.4
298.15	55000.00	844.0
298.15	60000.00	846.4
308.15	100.00	803.3
308.15	1000.00	804.0
308.15	5000.00	807.0
308.15	10000.00	810.7
308.15	15000.00	814.0
308.15	20000.00	817.5
308.15	25000.00	820.7
308.15	30000.00	823.8
308.15	35000.00	826.8
308.15	40000.00	829.7
308.15	45000.00	832.5
308.15	50000.00	835.3
308.15	55000.00	838.0
308.15	60000.00	840.4
318.15	100.00	795.8
318.15	1000.00	796.6
318.15	5000.00	799.8
318.15	10000.00	803.6
318.15	15000.00	807.2
318.15	20000.00	810.7
318.15	25000.00	814.0
318.15	30000.00	817.3
318.15	35000.00	820.4
318.15	40000.00	823.4
318.15	45000.00	826.3
318.15	50000.00	829.1
318.15	55000.00	831.9
318.15	60000.00	834.6
328.15	100.00	788.2
328.15	1000.00	789.0
328.15	5000.00	792.3
328.15	10000.00	796.3
328.15	15000.00	800.1
328.15	20000.00	803.8
328.15	25000.00	807.2
328.15	30000.00	810.6
328.15	35000.00	813.8
328.15	40000.00	817.0
328.15	45000.00	820.0
328.15	50000.00	822.9
328.15	55000.00	825.8
328.15	60000.00	828.4
338.15	100.00	780.3
338.15	1000.00	781.2
338.15	5000.00	784.8
338.15	10000.00	788.9
338.15	15000.00	792.9
338.15	20000.00	796.7
338.15	25000.00	800.3
338.15	30000.00	803.8
338.15	35000.00	807.2
338.15	40000.00	810.5
338.15	45000.00	813.6
338.15	50000.00	816.6
338.15	55000.00	819.6
338.15	60000.00	822.5
348.15	100.00	772.3
348.15	1000.00	773.1
348.15	5000.00	776.9
348.15	10000.00	781.2
348.15	15000.00	785.5
348.15	20000.00	789.5
348.15	25000.00	793.3
348.15	30000.00	796.9
348.15	35000.00	800.4
348.15	40000.00	803.8
348.15	45000.00	807.1
348.15	50000.00	810.3
348.15	55000.00	813.3
348.15	60000.00	816.2
358.15	100.00	763.8
358.15	1000.00	764.8
358.15	5000.00	768.8
358.15	10000.00	773.5
358.15	15000.00	777.9
358.15	20000.00	782.1
358.15	25000.00	786.1
358.15	30000.00	789.9
358.15	35000.00	793.6
358.15	40000.00	797.1
358.15	45000.00	800.5
358.15	50000.00	803.8
358.15	55000.00	807.0
358.15	60000.00	810.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	2003.00	811.93
298.15	3999.00	813.3
298.15	6003.00	814.64
298.15	8005.00	815.96
298.15	10001.00	817.26
298.15	13000.00	819.15
298.15	16004.00	821.0
298.15	19006.00	822.8
298.15	22000.00	824.56
298.15	24998.00	826.27
323.15	1999.00	794.19
323.15	4001.00	795.77
323.15	6001.00	797.32
323.15	8000.00	798.83
323.15	9998.00	800.31
323.15	12999.00	802.47
323.15	16001.00	804.56
323.15	19002.00	806.59
323.15	22001.00	808.56
323.15	25002.00	810.48
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	2000.00	813.0
298.15	4000.00	814.4
298.15	6000.00	815.8
298.15	8010.00	817.1
298.15	10000.00	818.5
298.15	13000.00	820.4
298.15	16000.00	822.3
298.15	19010.00	824.1
298.15	22000.00	825.9
298.15	25000.00	827.6
298.15	27990.00	829.4
298.15	29980.00	830.4
303.16	1980.00	808.8
303.16	3980.00	810.2
303.16	6010.00	811.7
303.16	8020.00	813.0
303.16	10030.00	814.4
303.16	12990.00	816.4
303.16	15980.00	818.4
303.15	19000.00	820.3
303.16	22010.00	822.1
303.16	25000.00	823.9
303.15	27980.00	825.6
303.16	29990.00	826.7
313.15	1990.00	800.6
313.15	4000.00	802.2
313.15	5980.00	803.7
313.15	7980.00	805.1
313.15	10020.00	806.6
313.15	13010.00	808.7
313.16	15980.00	810.8
313.15	19020.00	812.8
313.15	21980.00	814.7
313.16	24990.00	816.6
313.16	28000.00	818.4
313.15	30020.00	819.6
323.15	2000.00	793.5
323.15	4000.00	795.0
323.15	6000.00	796.7
323.15	8000.00	798.2
323.15	10000.00	799.6
323.15	13000.00	801.9
323.15	16000.00	804.0
323.15	19000.00	806.1
323.15	22000.00	808.2
323.15	25000.00	810.2
323.15	27990.00	812.1
323.15	29990.00	813.4
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	815.25
293.15	5000.00	818.83
293.15	10000.00	822.19
293.15	15000.00	825.37
293.15	20000.00	828.41
293.15	25000.00	831.36
293.15	30000.00	834.24
293.15	35000.00	837.11
303.15	100.00	808.05
303.15	5000.00	811.93
303.15	10000.00	815.5
303.15	15000.00	818.82
303.15	20000.00	821.92
303.15	25000.00	824.88
303.15	30000.00	827.74
303.15	35000.00	830.55
313.15	100.00	800.67
313.15	5000.00	804.61
313.15	10000.00	808.28
313.15	15000.00	811.75
313.15	20000.00	815.06
313.15	25000.00	818.26
313.15	30000.00	821.41
313.15	35000.00	824.56
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	810.8
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[317.91; 433.96]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.45991e+01
Coefficient B			-3.07041e+03
Coefficient C			-1.03369e+02
Temperature range, min.			317.91
Temperature range, max.			433.96
Pvap	1.33	kPa	317.91	Calculated Property
Pvap	3.00	kPa	330.80	Calculated Property
Pvap	6.19	kPa	343.70	Calculated Property
Pvap	11.87	kPa	356.59	Calculated Property
Pvap	21.36	kPa	369.49	Calculated Property
Pvap	36.40	kPa	382.38	Calculated Property
Pvap	59.19	kPa	395.28	Calculated Property
Pvap	92.36	kPa	408.17	Calculated Property
Pvap	139.01	kPa	421.07	Calculated Property
Pvap	202.66	kPa	433.96	Calculated Property
Pvap	[3.32e-07; 3863.36]	kPa	[195.56; 588.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.49346e+02
Coefficient B			-1.21964e+04
Coefficient C			-1.93819e+01
Coefficient D			9.39571e-06
Temperature range, min.			195.56
Temperature range, max.			588.00
Pvap	3.32e-07	kPa	195.56	Calculated Property
Pvap	6.96e-04	kPa	239.16	Calculated Property
Pvap	0.09	kPa	282.77	Calculated Property
Pvap	2.21	kPa	326.37	Calculated Property
Pvap	21.18	kPa	369.98	Calculated Property
Pvap	108.89	kPa	413.58	Calculated Property
Pvap	371.28	kPa	457.19	Calculated Property
Pvap	959.68	kPa	500.79	Calculated Property
Pvap	2053.63	kPa	544.40	Calculated Property
Pvap	3863.36	kPa	588.00	Calculated Property

Similar Compounds

Find more compounds similar to 1-Pentanol.

Mixtures

• 2-Butanone + Benzene, 1,3-dichloro- + 1-Pentanol
• Di-n-propyl ether + 1-Pentanol
• 1-Propanol + 1-Pentanol
• 1-Propanol + Di-n-propyl ether + 1-Pentanol
• Benzene, chloro- + 1-Pentanol
• 1-Pentanol + Acetylacetone
• 1-Pentanol + Diethylene glycol hexyl ether
• 1-Pentanol + 2-Heptanone
• 1-Pentanol + Simvastatin
• Cholesterol + 1-Pentanol
• Cholesterol + 1-Pentanol + Cyclohexane
• Diethyl malonate + 1-Pentanol
• 1-Pentanol + Cyclohexene, 1-methyl-4-(1-methylethenyl)-, (S)-
• Pentane, 2,2,4-trimethyl- + 1-Pentanol
• Isopropyl Alcohol + 1-Pentanol
• 1-Butanol + 1-Pentanol
• Isopropyl Alcohol + 1-Butanol + 1-Pentanol
• 1-Propanol, 2-methyl- + 1-Pentanol + Water
• Formic acid + 1-Pentanol + Water
• Lactic acid + 1-Pentanol + Water

Find more mixtures with 1-Pentanol.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Determination of excess molar enthalpies of the ternary system methyl tert-butyl ether + 1-pentanol + nonane at 298.15K Analysis and comparison with predicted values of the UNIFAC model and some empirical methods
• Measurement of infinite dilution activity coefficients of 1-alkanols (C1 C5) in water as a function of temperature (273 373 K)
• The co-solubility of 2-ethylhexanoic acid and some liquid alcohols in supercritical carbon dioxide
• Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
• Vapor liquid equilibria in the ternary system dipropyl ether + 1-propanol + 1-pentanol and the binary systems dipropyl ether + 1-pentanol, 1-propanol + 1-pentanol at 101.3 kPa
• Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
• Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
• Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
• Determination and correlation of molar excess enthalpies of binary systems 2,4-pentanedione + (1-butanol, + 2-methyl-1-propanol, + 1-pentanol, + 1-heptane, + ethyl acetate, and + water)
• Salting effect on the liquid liquid equilibria for the ternary system water +N-methyl-2-pyrrolidone + 1-pentanol
• Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• Liquid density of 1-pentanol at pressures up to 140MPa and from 293.15 to 403.15K
• Solubility and limiting activity coefficient of simvastatin in different organic solvents
• Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
• Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
• Liquid-liquid equilibrium of (water + 1-propanol + 1-pentanol) system at 298.15 and 323.15 K
• Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
• Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
• The influence of cation, anion and temperature on the liquid-liquid equilibrium of some pentanols-water system
• Experimental measurement and thermodynamic modeling of liquid-liquid equilibrium for 1-pentanol + water + NaNO3 at 298.15 and 308.15 K
• Study of the influence of the structure of the alcohol on vapor pressures and osmotic coefficients of binary mixtures alcohol + 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at T = 323.15 K
• Thermodynamic characterization of second generation biofuels: Vapour-liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol and cyclohexane or toluene
• Solubility of triclosan and iodopropynyl butylcarbamate in pure alkanols at several temperatures
• Solubility of lansoprazole in different solvents
• Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
• Vapour liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol with 2,2,4-trimethylpentane or n-heptane
• Investigation on vapor liquid equilibrium for 2-propanol + 1-butanol + 1-pentanol at 101.3 kPa
• Liquid-liquid equilibrium data for ternary aqueous mixtures containing 1-pentanol and 2-methyl-1-propanol at (298.15, 323.15, and 348.15) K
• Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
• Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
• Vapor-liquid equilibria of binary systems composed of polyoxyethylene 4-octylphenyl ether and alcohols: Experimental measurements and correlation
• Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
• Measurement and correlation of solid-liquid equilibrium for abietic acid + alcohol systems at atmospheric pressure
• Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
• Solubility of N-Ethylcarbazole in different organic solvent at 279.15 - 319.15 K
• Liquid-liquid phase equilibria of ionic liquid solutions in the critical region: 1-Methyl-3-octylimidazolium tetrafluoroborate with1-pentanol or 1-hexanol
• Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
• Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
• Vapour-liquid equilibria of the ternary mixture (1-pentanol + 2,2,4-trimethylpentane + heptane) and the binary mixture (2,2,4-trimethylpentane + heptane) at T = 313.15 K for the characterization of second generation biofuels.
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• An improved static-analytic apparatus for vapor-liquid equilibrium (PTxy) measurement using modified in-situ samplers
• Characterizing second generation biofuels: Excess enthalpies and vapour-liquid equilibria of the binary mixtures containing 1-pentanol or 2-pentanol and n-hexane
• Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
• Determination and correlation of solubility of N-methyl-3,4,5- trinitropyrazole (MTNP) in ten pure solvents from 283.15 K to 323.15 K
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Vapor-liquid equilibria and excess enthalpies of the binary systems 1- pentanol or 2-pentanol and 1-hexene or 1,2,4-trimethylbenzene for the development of biofuels
• Solubility, liquid-liquid equilibrium and critical states for quaternary system acetic acid - n-amyl alcohol - n-amyl acetate - water at 303.15 K and atmospheric pressure
• Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
• Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
• Measurement of the thermal conductivity of biofuel mixtures: Methyl caprate components of biodiesel and alcohols
• Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-pentanol and 3-pentanol
• Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
• Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
• Excess molar enthalpies of ethylformate and (1-propanol, 2-propanol, 1-butanol, 2-butanol, and 1-pentanol) at T = (298.15 and 308.15) K and p = (5 and 10) MPa
• Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
• Excess molar enthalpies of dimethyl carbonate and (butanol isomers and 1-pentanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
• Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
• Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
• Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
• Compressed liquid densities and excess molar volumes for (CO2 + 1-pentanol) binary system at temperatures from 313 to 363 K and pressures up to 25 MPa
• Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of dipropylene glycol dimethyl ether with 1-alkanols at 298.15 K
• Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
• Mixing thermodynamic properties of 1-butyl-4-methylpyridinium tetrafluoroborate [b4mpy][BF4] with water and with an alkan-1ol (methanol to pentanol)
• 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
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
• Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure
• Measurement and modeling of high-pressure (vapour + liquid) equilibria of (CO2 + alcohol) binary systems
• Vapour pressures, osmotic and activity coefficients for binary mixtures containing (1-ethylpyridinium ethylsulfate + several alcohols) at T = 323.15 K
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
• Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Cloud point measurements of 1-butyl-2,3-dimethylimidazolium tetrafluoroborate with alcohols
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Measurement and modeling of osmotic coefficients of binary mixtures (alcohol + 1,3-dimethylpyridinium methylsulfate) at T = 323.15 K
• Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
• (Liquid + liquid) equilibria in {water + acrylic acid + (1-butanol, or 2-butanol, or 1-pentanol)} systems at T = 293.2 K, T = 303.2 K, and T = 313.2 K and atmospheric pressure
• Application of the extended real associated solution (ERAS) theory to excess molar enthalpies of benzaldehyde + 1-alkanols (C1 to C5) at T = 298.15 K
• PrhoT measurements and derived properties of liquid 1-alkanols
• Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
• Determination and correlation of the solubility for diosgenin in alcohols solvents
• Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
• Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
• Solubility of salicylic acid in pure alcohols at different temperatures
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• On the solubility of nicotinic acid and isonicotinic acid in water and organic solvents
• Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Vapour pressures and osmotic coefficients of binary mixtures containing alcohol and pyrrolidinium-based ionic liquids
• FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
• Study of molecular interactions in the mixtures of some primary alcohols with equimolar mixture of 1-propanol and alkylbenzoates at T = 303.15 K
• Osmotic coefficients and apparent molar volumes of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid in alcohols
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Tie line data for the (water + butyric acid + n-butyl alcohol or amyl alcohol) at T = (298.2, 308.2, and 318.2) K and (water + butyric acid + isoamyl alcohol) at T = 298.2 K
• Osmotic coefficients of alcoholic mixtures containing BMpyrDCA: Experimental determination and correlation
• Contribution to study of the thermodynamics properties of mixtures containing 2-methoxy-2-methylpropane, alkanol, alkane
• Effect of the temperature on the physical properties of the pure ionic liquid 1-ethyl-3-methylimidazolium methylsulfate and characterization of its binary mixtures with alcohols
• Solubility of climbazole in various alcohols at different temperatures
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
• Thermodynamic models for determination of the solubility of (-)-shikimic acid in different pure solvents and in (H2O + ethanol) binary solvent mixtures
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• (Vapor + liquid) equilibria of alcohol + 1-methyl-1-propylpiperidinium triflate ionic liquid: VPO measurements and modeling
• Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
• Experimental measurement and correlation of the solubility of aloe-emodin in seven pure solvents
• The study of molecular interactions in 1-ethyl-3-methylimidazolium trifluoromethanesulfonate + 1-pentanol from density, speed of sound and refractive index measurements
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Thermodynamic and spectroscopic properties of binary mixtures of n-butylammonium butanoate ionic liquid with alcohols at T = (293.15-313.15) K
• Determination and modelling of troxerutin solubility in eleven mono-solvents and (1,4-dioxane + 2-propanol) binary solvents at temperatures from 288.15 K to 323.15 K
• Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
• Solubility and thermodynamic properties of vanillyl alcohol in some pure solvents
• Comparative study of physical properties of binary mixtures of halogen free ionic liquids with alcohols
• Solubility of commercial octacosanol in organic solvents and their correlation by thermodynamic models at different temperatures
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Mutual diffusion coefficients of n-butanol + n-heptane and n-pentanol + n-heptane from 288.15 K to 318.15 K
• Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Excess molar enthalpies of R-fenchone + butan-1-ol or + pentan-1-ol. Modeling with COSMO-RS and UNIFAC
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
• Thermodynamic properties of paracetamol impurities 4-nitrophenol and 4'-chloroacetanilide and the impact of such impurities on the crystallisation of paracetamol from solution
• Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
• Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
• Experimental studies on the thermal conductivity of methyl laurate component of biodiesel with three alcohols
• Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
• Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
• Excess molar enthalpies of methylformate + (1-propanol, 2-propanol, 1-butanol, 2-butanol and 1-pentanol) at T = 298.15 K, p = (5.0, 10.0)MPa, and methylformate + 1-propanol at T = 333.15 K, p = 10.0MPa
• ERAS modeling of the excess molar enthalpies of binary liquid mixtures of 1-pentanol and 1-hexanol with acetonitrile at atmospheric pressure and 288, 298, 313 and 323K
• Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
• Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
• Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
• Measurement and Correlation for Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
• THERMODYNAMICS OF MIXTURES CONTAINING AMINES. XIV. CpEm OF BENZYLAMINE WITH HEPTANE AT 293.15 K OR WITH METHANOL, 1-PROPANOL OR 1-PENTANOL AT (293.15-308.15) K
• Measurement and correlation of solubility of carbendazim in lower alcohols
• Capillary Viscometer and Vibrating Tube Densimeter for Simultaneous Measurements up to 70 MPa and 423 K
• Viscous Calibration Liquids for Self-diffusion Measurements
• Thermodynamics of 1,3-dimethylurea in eight alcohols
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
• Measurement and Correlation of Solubility on Reactive Crystallization of Methyl D-(-)-4-Hydroxy-phenylglycinate
• Physical Properties of the Pure Deep Eutectic Solvent, [ChCl]:[Lev] (1:2) DES, and Its Binary Mixtures with Alcohols
• Solubility Correlation and Thermodynamic Analysis of Sorafenib Free Base and Sorafenib Tosylate in Monosolvents and Binary Solvent Mixtures
• Solubility and Thermodynamic Behavior of Veramoss in Different Pure Solvents and {Ethanol + Water} Mixtures from T = 283.15 to 333.15 K
• Measurement and Correlation of Solubility of Loratadine in Different Pure Solvents and Binary Mixtures
• Measurement and Correlation of Solubility of Amorphous Cefmetazole Sodium in Pure Solvents and Binary Solvent Mixtures
• Determination and Correlation of Solubility of Phenylbutazone in Monosolvents and Binary Solvent Mixtures
• Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
• Pressurized-Synthetic Methodology for Solubility Determination at Elevated Temperatures with Application to Paracetamol in Pure Solvents
• Studying the Liquid-Liquid Equilibrium of Systems Water +2-Hydroxyethylammonium Propanoate or 2-Hydroxyethylammonium Butanoate or 2-Hydroxyethylammonium Pentanoate +1-Pentanol at 293.15, 313.15, and 333.15 K: Experimental Determination and Thermodynamic Modeling
• Liquid-Liquid Equilibria Determination and Prediction for Ternary Systems of Water + 1,6-Hexanediamine + (1-Butanol or 1-Pentanol) at 298.2, 308.2, and 318.2 K
• Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
• Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
• Isothermal Vapor-Liquid Equilibrium Measurements of Butan-2-one + 2-Methyl-propan-1-ol/Pentan-1-ol
• Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
• Synergistic Extraction of Hydroquinone from Aqueous Solution with Solvent Mixture of 2-Pentanone and n-Pentanol: Liquid-Liquid Equilibria and Data Correlation
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Viscosity and Density of n-Alcohols at Temperatures between (298.15 and 323.15) K and Pressures up to 30 MPa
• Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
• Effect of the Alkyl Chain on the Physical Properties of Imidazolium-Based Ionic Liquids with 1-Propanol, 1-Butanol, and 1-Pentanol Binary Mixtures
• Density and Derived Properties of Binary Mixtures Containing {2-(Dimethylamino)ethyl Methacrylate + Alcohols} at Temperatures from T = (293.15 to 313.15) K and Pressures of up to 35 MPa
• Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
• Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
• Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
• Measurement and Correlation of Solubility of Hydrochlorothiazide in Monosolvents and Binary Solvent Mixtures from 283.15 to 323.15 K
• Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
• Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
• Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
• Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
• Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
• Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
• Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
• Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 3. Liquid-Liquid Equilibria of Binary Mixtures of 1-Ethyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide with Propan-1-ol, Butan-1-ol, and Pentan-1-ol
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Acetonitrile Mixtures at 298.2 K
• Density, Refractive Index, and Speed of Sound at 298.15 K and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + 1-Pentanol and Ethanol + 2-Methyl-1-propanol
• Measurement and Correlation of Mutual Solubilities for High Viscosity Binary Systems: Aniline + Methylcyclohexane, Phenol + Heptane, Phenol + Octane, and Glycerol + 1-Pentanol
• Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
• Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
• Vapor-Liquid Equilibria of the Binary System 1-Pentanol + Anisole and the Quaternary System Benzene+Cyclohexane+1-Pentanol+Anisole at 101.32 kPa
• Thermodynamic Properties of Mixtures Containing Ionic Liquids.4.LLE of Binary Mixtures of [C2MIM][NTf2] with Propan-1-ol, Butan-1-ol, and Pentan-1-ol and [C4MIM][NTf2] with Cyclohexanol and 1,2-Hexanediol Including Studies of the Influence of Small Amounts of Water
• Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
• Experimental and Predicted Excess Molar Enthalpies of the Ternary System tert-Butyl Methyl Ether + 1-Pentanol + Decane at 298.15 K
• Quaternary Liquid-Liquid Equilibrium of Water + Acetic Acid + Propionic Acid + Solvent (Amyl Alcohol, Cyclohexyl Acetate, or Toluene) Systems
• Solubility and Density of 2,6-Dimethylnaphthalene in C1-C7 1-Alkanols
• Heat Capacities and Derived Thermodynamic Functions of 1-Propanol between 10 K and 350 K and of 1-Pentanol between 85 K and 370 K
• Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
• Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
• 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
• Excess Molar Enthalpies of Methyl Acetate and (1-Propanol, 2-Propanol, 1-Butanol, 2-Butanol, and 1-Pentanol) at T = (298.15 and 308.15) K and P = (5.0 and 10.0) MPa
• Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Nonane
• 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
• Solubility of Organic Systems Containing 1,4-Dioxan-2-one
• 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, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
• Density and Surface Tension of Binary Mixtures of Acetonitrile + 1-Alkanol at 293.15 K
• Liquid-Liquid Equilibrium Diagrams of Ethanol + Water + (Ethyl Acetate or 1-Pentanol) at Several Temperatures
• Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
• Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
• Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
• Excess Molar Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1- or 2-Pentanol at (283.15, 298.15, and 313.15) K
• Isobaric Vapor-Liquid Equilibria of the Ternary System Dibutyl Ether + 1-Pentanol + Nonane
• Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures Containing 2-Methyl-1-propanol + 2-Methyl-1-butanol, 2-Methyl-1-propanol + 3-Methyl-1-butanol, and 2-Methyl-1-propanol + 1-Pentanol
• Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Fluid-Phase Behavior of {1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide, [C6mim][NTf2], + C2-C8 n-Alcohol} Mixtures: Liquid-Liquid Equilibrium and Excess Volumes
• Solubility of Xylitol in Ethanol, Acetone, N,N-Dimethylformamide, 1-Butanol, 1-Pentanol, Toluene, 2-Propanol, and Water
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
• Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K
• Solubilities of Ibuprofen in Different Pure Solvents
• Thermodynamic Parameters of Anionic Surfactant-Additive Systems at the Cloud Point
• Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
• Excess Molar Enthalpies of 2-Methyl-2-butanol (1) + 1-Alkanols (C1-C5) (2) at 298.15 K
• Liquid-Liquid Equilibria of Water + Pentan-1-ol + 2,6,6-Trimethylbicyclo[3.1.1]hep-2-ene or 6,6-Dimethyl-2-methylenebicyclo[3.1.1]heptane at (293.15, 303.15, 313.15, and 323.15) K
• Solubilities of Phloretin in 12 Solvents at Different Temperatures
• Measurement and Study on the Liquid Liquid Equilibrium of Ionic Liquids with Aliphatic Alcohols
• Isobaric Vapor-Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane
• Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
• Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
• Measurement and Correlation of Solubility of Clopidogrel Hydrogen Sulfate (Metastable Form) in Lower Alcohols
• Isobaric Vapor Liquid Equilibrium of 3-Methyl-1-butanol + Ethyl Lactate and 1-Pentanol + Ethyl Lactate at (13.0 and 101.3) kPa
• Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
• Extraction of n-Alcohols from n-Heptane Using Ionic Liquids.
• Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
• Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
• Measurements and Modeling of High-Pressure Phase Behavior of the Carbon Dioxide + Pentan-1-ol Binary System
• Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
• Vapor Liquid Equilibrium Data for Binary Systems of 1H-Pyrrole with Butan-1-ol, Propan-1-ol, or Pentan-1-ol
• Isobaric Vapor Liquid Equilibria of Tertiary Amine and n-Alkane/Alkanol Binary Mixtures: Experimental Measurements and Modeling with GC-PPC-SAFT
• Densities and Viscosities for Binary Liquid Mixtures of Ethanol + 1-Propanol, 1-Butanol, and 1-Pentanol from (293.15 to 328.15) K at 0.1 MPa
• Liquid Liquid Phase Equilibria of the Binary Ionic Liquid Systems [Cn MIM][NTf2] + n-Butanol, + n-Pentanol, + H2O Using UV Spectroscopic and Densimetric Analytical Methods
• Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
• Liquid Liquid Phase Behavior of Solutions of 1,3-Dimethylimidazolium- and 1-Methyl-3-propylimidazolium Bis((trifluoromethyl)sulphonyl)amide (C1,3mimNTf2) in n-Alkyl Alcohols
• Liquid Liquid Equilibrium for the Ternary System 2-Methyl-2-propanol + 1-Pentanol + Water at T = (303.15, 328.15, and 353.15) K
• Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
• 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
• Excess Molar Enthalpies of Binary Mixtures Containing 1-Methyl-3-octyl-imidazolium Tetrafluoroborate and Alcohols at T = 298.15 K
• Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + n-Pentanol), (Propyl Acetate + 1-Methyl-1-butanol), and (Propyl Acetate + 3-Methyl-1-butanol) at 101.3 kPa
• Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of Cefixime Trihydrate in Seven Pure Solvents
• Determination and Correlation of Solubilities of Lauric Acid in Eight Alcohols
• Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• Experimental Liquid-Liquid Equilibria of 1-Alkyl-3-methylimidazolium Hexafluorophosphate with 1-Alcohols
• Solubility of Phenacetinum in Methanol, Ethanol, 1-Propanol, 1-Butanol, 1-Pentanol, Tetrahydrofuran, Ethyl Acetate, and Benzene between 282.65 K and 333.70 K
• Isobaric Vapor-Liquid Equilibrium for the Binary Systems 1-Pentanol + Cyclohexane and 1-Pentanol + n-Hexane at Low Alcohol Compositions
• Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
• Isobaric Vapor Liquid Equilibria of the Ternary System 1-Pentanol + Nonane Anisole
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
• Solubility of Losartan Potassium in Different Pure Solvents from (293.15 to 343.15) K
• Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
• Determination and Correlation of Excess Molar Enthalpies of Eight Binary Systems Containing Acetophenone at Different Temperatures
• Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
• Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
• Solubility of Alcohols and Aromatic Compounds in Imidazolium-Based Ionic Liquids
• Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
• Solubility of D(-)-p-Hydroxyphenylglycine Dane Salt in Eight Alcohols between (293 and 343) K
• Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
• Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Excess Molar Enthalpies of Five Binary Systems Containing Ethyl Acetoacetate at Different Temperatures
• Thermodynamic Properties of Micellization of Sodium Dodecylbenzene Sulfonate in the Aqueous-Rich Region of 1-Pentanol and 1-Hexanol
• Study of the Effects of Temperature and Pressure on the Thermodynamic and Acoustic Properties of Pentan-1-ol, 2-Methyl-2-butanol, and Cyclopentanol in the Pressure Range from (0.1 to 100) MPa and Temperature from (293 to 318) K
• Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Anisole
• Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 2-Ethyl-1-hexanol with 1-Pentanol, 1-Heptanol, or 1-Nonanol at the Temperature 298.15 K
• Densities and Viscosities of exo-Tetrahydrodicyclopentadiene + n-Butanol and exo-Tetrahydrodicyclopentadiene + n-Pentanol at Temperatures of (293.15 to 313.15) K
• Measurement and Correlation of Solubilities of Decanedioic Acid in C4-C6 Alcohol Solvents
• Studies of Monohydric Alcohols in Aqueous Sodium Dodecyl Sulfate Solutions at T = (298.15 and 308.15) K
• Isobaric Vapor-Liquid Equilibria of Heptane + 1-Butanol and Heptane + 1-Pentanol Systems at (53.3 and 91.3) kPa
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubilities of (?,Z)-2-Amino-?-(methoxyimino)-4-thiazole-ethanethioic Acid S-2-Benzothiazolyl Ester in Pure Solvents and a Mixture of Acetonitrile and Dichloromethane
• Isobaric Vapor-Liquid Equilibrium for Binary Mixtures of 3-Methyl-1-butanol + 3-Methyl-1-butyl Ethanoate and 1-Pentanol + Pentyl Ethanoate at 101.3 kPa
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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