Isopropyl Alcohol (CAS 67-63-0)

InChI

InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3

InChI Key

KFZMGEQAYNKOFK-UHFFFAOYSA-N

Formula

C3H8O

SMILES

CC(C)O

Molecular Weight¹

60.09

CAS

67-63-0

Other Names

1-Methylethyl Alcohol
1-methylethanol
2-Hydroxypropane
2-PROPANOL
2-Propyl alcohol
Alcojel
Alcolo
Alcool isopropilico
Alcool isopropylique
Alcosolve
Alcosolve 2
Alkolave
Arquad DMCB
Avantin
Avantine
Combi-Schutz
Dimethylcarbinol
Hartosol
IPA
IPS 1
Imsol A
Isohol
Isopropanol
Isopropyl alcohol, rubbing
Lavacol
Lutosol
PRO
Petrohol
Propan-2-ol
Propane, 2-hydroxy-
Propanol-2
Propol
SEC-PROPYL ALCOHOL
Spectrar
Sterisol hand disinfectant
Takineocol
UN 1219
Virahol
Visco 1152
i-Propanol
i-Propylalkohol
iso-C3H7OH
iso-Propylalkohol
n-Propan-2-ol
sec-Propanol

ω : Acentric Factor.
PAff : Proton affinity (kJ/mol).
T_ig : Autoignition Temperature (K).
BasG : Gas basicity (kJ/mol).
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).
σ_cond : Electrical conductivity (S/m).
LFL : Lower Flammability Limit (% in Air).
UFL : Upper Flammability Limit (% in Air).
T_flash,cc : Flash Point (Closed Cup Method) (K).
T_flash,oc : Flash Point (Open Cup Method) (K).
Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
R_g : Radius of Gyration.
Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
IE : Ionization energy (eV).
log₁₀WS : Log10 of Water solubility in mol/l.
logP_oct/wat : Octanol/Water partition coefficient.
McVol : McGowan's characteristic volume (ml/mol).
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.
Δ_fusS : Entropy of fusion at a given temperature (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_boil : Boiling point at given 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).
V_m : Molar Volume (m³/mol).
Z_c : Critical Compressibility.
Z_ra : Rackett Parameter.
¹: Molecular weight from the IUPAC atomic weights tables.

Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Please note that you need to enable javascript to get access to all the properties. Here is how to do it for Internet Explorer and for Firefox.

Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources

Physical Properties

Property	Value	Unit	Source
ω	0.6650		KDB
PAff	[793.00; 796.00]	kJ/mol
PAff	793.00	kJ/mol	NIST
PAff	796.00 ± 6.00	kJ/mol	NIST
T_ig	672.04	K	KDB
BasG	762.60	kJ/mol	NIST
Δ_cH°_liquid	[-2006.90; -2005.10]	kJ/mol
Δ_cH°_liquid	-2006.90 ± 0.20	kJ/mol	NIST
Δ_cH°_liquid	-2005.80 ± 0.40	kJ/mol	NIST
Δ_cH°_liquid	-2005.10	kJ/mol	NIST
μ	1.70	debye	KDB
η	[0.0020443; 0.0020980]	Pa×s
η	0.0020980	Pa×s	Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
η	0.0020630	Pa×s	Thermodynamic properties of binary liquid mixtures of diethylenetriamine with alcohols at different temperatures
η	0.0020443	Pa×s	Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
LFL	2.30	% in Air	KDB
UFL	12.70	% in Air	KDB
T_flash,cc	291.48	K	KDB
T_flash,oc	284.82	K	KDB
Δ_fG°	-173.50	kJ/mol	KDB
R_g	2.7260		KDB
Δ_fH°_gas	[-272.80; -271.10]	kJ/mol
Δ_fH°_gas	-272.60	kJ/mol	KDB
Δ_fH°_gas	-272.80	kJ/mol	NIST
Δ_fH°_gas	-271.10	kJ/mol	NIST
Δ_fH°_gas	-272.30 ± 0.92	kJ/mol	NIST
Δ_fH°_gas	-272.80	kJ/mol	NIST
Δ_fH°_liquid	[-318.70; -317.00]	kJ/mol
Δ_fH°_liquid	-317.00 ± 0.30	kJ/mol	NIST
Δ_fH°_liquid	-318.20 ± 0.71	kJ/mol	NIST
Δ_fH°_liquid	-318.70	kJ/mol	NIST
Δ_fusH°	4.09	kJ/mol	Joback Calculated Property
Δ_vapH°	[40.00; 45.90]	kJ/mol
Δ_vapH°	45.48	kJ/mol	NIST
Δ_vapH°	44.00	kJ/mol	NIST
Δ_vapH°	45.34 ± 0.02	kJ/mol	NIST
Δ_vapH°	45.34 ± 0.02	kJ/mol	NIST
Δ_vapH°	45.20 ± 0.10	kJ/mol	NIST
Δ_vapH°	45.20 ± 0.10	kJ/mol	NIST
Δ_vapH°	45.51	kJ/mol	NIST
Δ_vapH°	44.00	kJ/mol	NIST
Δ_vapH°	45.90 ± 0.20	kJ/mol	NIST
Δ_vapH°	44.40	kJ/mol	NIST
Δ_vapH°	Outlier 40.00 ± 0.04	kJ/mol	NIST
IE	[10.10; 10.49]	eV
IE	10.17 ± 0.02	eV	NIST
IE	10.15 ± 0.07	eV	NIST
IE	10.10 ± 0.02	eV	NIST
IE	10.29 ± 0.02	eV	NIST
IE	10.18	eV	NIST
IE	10.12 ± 0.03	eV	NIST
IE	10.15 ± 0.05	eV	NIST
IE	10.44	eV	NIST
IE	10.49 ± 0.03	eV	NIST
IE	10.42	eV	NIST
IE	10.36	eV	NIST
IE	10.42	eV	NIST
log₁₀WS	[0.43; 0.43]
log₁₀WS	0.43		Aq. Solubility Prediction
log₁₀WS	0.43		Estimated Solubility
logP_oct/wat	0.387		Crippen Calculated Property
McVol	59.000	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
P_c	[4716.00; 5380.00]	kPa
P_c	4764.00	kPa	KDB
P_c	4755.00	kPa	Isothermal Vapor-Liquid Equilibria for the 2-Propanol + n-Heptane System near the Critical Region
P_c	4760.00 ± 20.00	kPa	NIST
P_c	4770.00	kPa	NIST
P_c	4761.00 ± 20.00	kPa	NIST
P_c	4761.00 ± 20.00	kPa	NIST
P_c	4762.00	kPa	NIST
P_c	4716.00 ± 8.00	kPa	NIST
P_c	4762.00 ± 4.75	kPa	NIST
P_c	4764.00	kPa	NIST
P_c	Outlier 5370.23 ± 101.32	kPa	NIST
P_c	Outlier 5380.00	kPa	NIST
ρ_c	[271.03; 272.83]	kg/m³
ρ_c	271.03 ± 1.20	kg/m³	NIST
ρ_c	272.83	kg/m³	NIST
ρ_c	272.71	kg/m³	NIST
I_np	[444.00; 530.00]
I_np	508.00		NIST
I_np	491.00		NIST
I_np	453.00		NIST
I_np	508.00		NIST
I_np	491.00		NIST
I_np	453.00		NIST
I_np	508.00		NIST
I_np	491.00		NIST
I_np	453.00		NIST
I_np	480.00		NIST
I_np	458.00		NIST
I_np	447.00		NIST
I_np	450.00		NIST
I_np	444.00		NIST
I_np	450.00		NIST
I_np	446.00		NIST
I_np	477.00		NIST
I_np	456.00		NIST
I_np	460.00		NIST
I_np	476.00		NIST
I_np	490.00		NIST
I_np	486.00		NIST
I_np	463.00		NIST
I_np	450.00		NIST
I_np	524.00		NIST
I_np	494.00		NIST
I_np	524.00		NIST
I_np	524.00		NIST
I_np	495.40		NIST
I_np	500.00		NIST
I_np	481.00		NIST
I_np	515.80		NIST
I_np	515.00		NIST
I_np	510.00		NIST
I_np	510.00		NIST
I_np	483.00		NIST
I_np	480.00		NIST
I_np	472.00		NIST
I_np	474.00		NIST
I_np	456.00		NIST
I_np	530.00		NIST
I_np	496.00		NIST
I_np	493.00		NIST
I_np	506.00		NIST
I_np	483.40		NIST
I_np	514.00		NIST
I_np	500.00		NIST
I_np	488.00		NIST
I_np	500.00		NIST
I_np	502.00		NIST
I_np	516.00		NIST
I_np	516.00		NIST
I_np	477.00		NIST
I_np	477.00		NIST
I_np	498.00		NIST
I_np	499.00		NIST
I_np	477.00		NIST
I_np	500.00		NIST
I_np	511.00		NIST
I_np	486.00		NIST
I_np	486.00		NIST
I_np	474.00		NIST
I_np	486.00		NIST
I_np	474.00		NIST
I_np	530.00		NIST
I_np	475.00		NIST
I_np	491.00		NIST
I_np	481.00		NIST
I_np	503.00		NIST
I_np	475.00		NIST
I_np	500.00		NIST
I_np	516.00		NIST
I_np	477.00		NIST
I_np	474.00		NIST
I_np	491.00		NIST
I_np	530.00		NIST
I_np	514.00		NIST
I_np	508.00		NIST
I_np	453.00		NIST
I_np	458.00		NIST
I_np	446.00		NIST
I_np	490.00		NIST
I	[884.00; 975.00]
I	935.00		NIST
I	949.00		NIST
I	957.00		NIST
I	949.00		NIST
I	957.00		NIST
I	962.00		NIST
I	885.00		NIST
I	963.00		NIST
I	935.00		NIST
I	928.00		NIST
I	922.00		NIST
I	912.00		NIST
I	932.00		NIST
I	920.00		NIST
I	910.00		NIST
I	940.00		NIST
I	903.00		NIST
I	927.00		NIST
I	891.00		NIST
I	884.00		NIST
I	920.00		NIST
I	935.00		NIST
I	941.40		NIST
I	950.00		NIST
I	921.00		NIST
I	912.00		NIST
I	884.00		NIST
I	888.00		NIST
I	932.00		NIST
I	938.00		NIST
I	909.00		NIST
I	Outlier 975.00		NIST
I	970.00		NIST
I	935.00		NIST
I	924.00		NIST
I	917.00		NIST
I	928.00		NIST
I	922.00		NIST
I	948.00		NIST
I	923.00		NIST
I	884.00		NIST
I	925.00		NIST
I	926.00		NIST
I	884.00		NIST
I	917.00		NIST
I	885.00		NIST
I	921.00		NIST
I	912.00		NIST
I	925.00		NIST
I	938.00		NIST
I	947.00		NIST
I	970.00		NIST
I	Outlier 975.00		NIST
I	910.00		NIST
I	933.00		NIST
I	884.00		NIST
I	906.00		NIST
I	931.00		NIST
I	931.00		NIST
I	942.00		NIST
I	921.00		NIST
I	884.00		NIST
I	962.00		NIST
I	908.00		NIST
I	927.00		NIST
I	923.00		NIST
I	917.00		NIST
I	935.00		NIST
I	962.00		NIST
I	922.00		NIST
I	940.00		NIST
S°_liquid	[179.90; 192.90]	J/mol×K
S°_liquid	180.58	J/mol×K	NIST
S°_liquid	179.90	J/mol×K	NIST
S°_liquid	192.90	J/mol×K	NIST
S°_liquid	190.80	J/mol×K	NIST
T_boil	[3.50; 385.20]	K
T_boil	355.40	K	KDB
T_boil	355.37	K	Physical properties and phase equilibria of the system isopropyl acetate + isopropanol + 1-octyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide
T_boil	355.15	K	Multiphase equilibria for mixtures containing water, isopropanol, propionic acid, and isopropyl propionate
T_boil	355.53	K	Isobaric VLE at 0.6 MPa for binary systems isobutyl acetate + ethanol, + 1-propanol or + 2-propanol
T_boil	355.35	K	Isobaric vapor-liquid equilibrium data for the binary system methyl acetate + isopropyl acetate and the quaternary system methyl acetate + methanol + isopropanol + isopropyl acetate at 101.3 kPa
T_boil	355.60	K	Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
T_boil	355.40	K	Experimental studies and thermodynamic analysis of isobaric vapor-liquid-liquid equilibria of 2-propanol + water system using n-propyl acetate and isopropyl acetate as entrainers
T_boil	355.61	K	VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa
T_boil	355.45	K	Isobaric (vapour + liquid) equilibrium for (2-propanol + water + ammonium thiocyanate): Fitting the data by an empirical equation
T_boil	355.25	K	Isobaric (vapour + liquid + liquid) equilibrium data for (di-n-propyl ether + n-propyl alcohol + water) and (diisopropyl ether + isopropyl alcohol + water) systems at 100 kPa
T_boil	355.27	K	Vapour-liquid equilibrium and extractive distillation for separation of azeotrope isopropyl alcohol and diisopropyl ether
T_boil	355.33	K	Separation of the mixture (isopropyl alcohol + diisopropyl ether + n-propanol): Entrainer selection, interaction exploration and vapour-liquid equilibrium measurements
T_boil	355.71	K	A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
T_boil	355.33	K	Vapor Liquid Equilibria for Ternary Mixtures of Isopropyl Alcohol, Isopropyl Acetate, and DMSO at 101.3 kPa
T_boil	355.60	K	Acetonitrile Dehydration via Extractive Distillation Using Low Transition Temperature Mixtures as Entrainers
T_boil	355.37	K	Vapor Liquid Equilibria for Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene at 101 kPa
T_boil	355.35	K	Measurement and Correlation of Excess Molar Enthalpies for Ethylene Glycol + Alkanol Systems at the Temperatures (298.15, 308.15, and 323.15) K
T_boil	355.15	K	Vapor-Liquid Equilibria for the Binary Systems of Dimethoxymethane with Some Fuel Oxygenates
T_boil	355.41	K	Vapor-Liquid Equilibrium Behavior of Tolan in Alcohol
T_boil	355.39	K	Vapor-Liquid Equilibrium Behaviors of Coumarin and Vanillin in Ethanol, 1-Propanol, and 2-Propanol
T_boil	355.35	K	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
T_boil	355.40	K	Vapor-Liquid Equilibrium Behaviors of 3-Ethoxy-4-hydroxybenzaldehyde in Alcohol
T_boil	355.40	K	Vapor Liquid Equilibrium Behaviors of 5-Methyl-2-(1-methylethyl)phenol in Alcohol
T_boil	355.65	K	Isobaric Vapor-Liquid Equilibrium for (Propan-2-ol + Water + 1-Butyl-3-methylimidazolium Tetrafluoroborate)
T_boil	355.42 ± 0.20	K	NIST
T_boil	355.42 ± 0.30	K	NIST
T_boil	355.42 ± 0.07	K	NIST
T_boil	355.65 ± 0.20	K	NIST
T_boil	355.65 ± 0.30	K	NIST
T_boil	355.42 ± 0.20	K	NIST
T_boil	355.60	K	NIST
T_boil	385.20 ± 0.20	K	NIST
T_boil	355.60 ± 0.10	K	NIST
T_boil	355.40	K	NIST
T_boil	355.45 ± 0.40	K	NIST
T_boil	355.45 ± 0.40	K	NIST
T_boil	355.45 ± 0.30	K	NIST
T_boil	355.06 ± 0.25	K	NIST
T_boil	355.45 ± 0.10	K	NIST
T_boil	354.85 ± 0.30	K	NIST
T_boil	355.45 ± 0.30	K	NIST
T_boil	355.00 ± 0.30	K	NIST
T_boil	355.55 ± 0.30	K	NIST
T_boil	355.20 ± 0.60	K	NIST
T_boil	355.70 ± 0.30	K	NIST
T_boil	355.50 ± 0.40	K	NIST
T_boil	355.39 ± 0.30	K	NIST
T_boil	355.50 ± 0.50	K	NIST
T_boil	353.60 ± 0.50	K	NIST
T_boil	355.45 ± 0.25	K	NIST
T_boil	355.45	K	NIST
T_boil	353.60 ± 0.30	K	NIST
T_boil	355.45 ± 0.40	K	NIST
T_boil	355.45 ± 0.30	K	NIST
T_boil	355.45 ± 0.08	K	NIST
T_boil	355.55 ± 0.15	K	NIST
T_boil	355.54 ± 0.20	K	NIST
T_boil	355.37 ± 0.30	K	NIST
T_boil	355.16 ± 0.20	K	NIST
T_boil	355.48 ± 0.30	K	NIST
T_boil	355.35 ± 0.50	K	NIST
T_boil	355.45	K	NIST
T_boil	355.35 ± 0.50	K	NIST
T_boil	355.55 ± 0.30	K	NIST
T_boil	355.65 ± 1.00	K	NIST
T_boil	355.55 ± 0.50	K	NIST
T_boil	Outlier 3.50 ± 2.00	K	NIST
T_boil	354.70 ± 1.00	K	NIST
T_boil	355.55 ± 0.50	K	NIST
T_boil	355.45 ± 0.10	K	NIST
T_boil	355.55 ± 0.50	K	NIST
T_boil	355.60 ± 0.25	K	NIST
T_boil	355.30 ± 0.50	K	NIST
T_boil	355.25 ± 0.50	K	NIST
T_boil	355.15 ± 1.00	K	NIST
T_boil	355.48 ± 0.33	K	NIST
T_boil	355.35 ± 0.30	K	NIST
T_boil	354.65 ± 1.00	K	NIST
T_boil	357.65 ± 1.00	K	NIST
T_boil	355.48 ± 0.44	K	NIST
T_boil	355.45 ± 0.20	K	NIST
T_boil	353.90 ± 2.00	K	NIST
T_boil	355.40 ± 0.10	K	NIST
T_boil	355.55 ± 0.50	K	NIST
T_boil	364.85 ± 0.50	K	NIST
T_boil	355.65 ± 0.50	K	NIST
T_boil	355.15 ± 1.30	K	NIST
T_boil	355.55 ± 0.50	K	NIST
T_boil	355.65 ± 1.00	K	NIST
T_boil	355.85 ± 0.50	K	NIST
T_boil	355.35 ± 0.30	K	NIST
T_boil	355.45 ± 0.50	K	NIST
T_boil	355.60 ± 0.40	K	NIST
T_boil	355.39 ± 0.20	K	NIST
T_boil	355.57 ± 0.10	K	NIST
T_boil	355.55 ± 0.30	K	NIST
T_boil	355.25 ± 0.30	K	NIST
T_boil	354.87 ± 0.30	K	NIST
T_boil	355.55 ± 0.50	K	NIST
T_boil	355.90 ± 0.40	K	NIST
T_boil	355.15 ± 2.00	K	NIST
T_boil	355.51 ± 0.10	K	NIST
T_boil	355.45 ± 0.30	K	NIST
T_boil	354.95 ± 0.50	K	NIST
T_boil	354.55 ± 0.50	K	NIST
T_boil	355.45 ± 0.50	K	NIST
T_boil	355.54 ± 0.10	K	NIST
T_boil	355.44 ± 0.10	K	NIST
T_boil	355.55 ± 0.10	K	NIST
T_boil	355.46 ± 0.20	K	NIST
T_boil	355.50 ± 0.20	K	NIST
T_boil	355.55 ± 0.50	K	NIST
T_boil	355.45 ± 1.00	K	NIST
T_boil	355.95 ± 1.00	K	NIST
T_boil	355.60 ± 0.50	K	NIST
T_boil	355.60 ± 0.50	K	NIST
T_boil	355.60 ± 0.50	K	NIST
T_boil	355.15 ± 0.20	K	NIST
T_boil	355.60 ± 0.20	K	NIST
T_boil	Outlier 82.21 ± 0.20	K	NIST
T_boil	353.85 ± 0.50	K	NIST
T_boil	355.55 ± 0.30	K	NIST
T_boil	355.50 ± 0.30	K	NIST
T_boil	355.15 ± 0.20	K	NIST
T_boil	355.40 ± 0.05	K	NIST
T_boil	355.55 ± 0.50	K	NIST
T_boil	355.41 ± 0.05	K	NIST
T_boil	355.40 ± 0.05	K	NIST
T_boil	355.43 ± 0.05	K	NIST
T_boil	355.41 ± 0.05	K	NIST
T_boil	355.55 ± 0.20	K	NIST
T_boil	351.65 ± 3.00	K	NIST
T_boil	355.75 ± 0.30	K	NIST
T_boil	354.65 ± 1.50	K	NIST
T_boil	354.20 ± 0.50	K	NIST
T_boil	355.65 ± 1.00	K	NIST
T_boil	355.15 ± 1.50	K	NIST
T_boil	355.59 ± 0.20	K	NIST
T_boil	355.19 ± 0.20	K	NIST
T_boil	356.15 ± 1.00	K	NIST
T_boil	356.00 ± 0.50	K	NIST
T_boil	355.65 ± 1.50	K	NIST
T_boil	356.00 ± 0.50	K	NIST
T_c	[507.36; 516.60]	K
T_c	508.30	K	KDB
T_c	508.72	K	One- and two-phase isochoric heat capacities and saturated densities of 2-propanol in the critical and supercritical regions
T_c	508.30 ± 0.30	K	NIST
T_c	508.60	K	NIST
T_c	508.00 ± 0.60	K	NIST
T_c	508.00 ± 0.60	K	NIST
T_c	508.00	K	NIST
T_c	507.36 ± 0.20	K	NIST
T_c	508.30	K	NIST
T_c	508.30 ± 0.05	K	NIST
T_c	508.30 ± 1.00	K	NIST
T_c	508.30 ± 0.20	K	NIST
T_c	508.30 ± 0.30	K	NIST
T_c	508.30 ± 0.30	K	NIST
T_c	508.26	K	NIST
T_c	511.50	K	NIST
T_c	508.15 ± 0.50	K	NIST
T_c	508.40 ± 0.30	K	NIST
T_c	508.80	K	NIST
T_c	Outlier 516.60	K	NIST
T_c	511.20 ± 3.00	K	NIST
T_c	507.80	K	NIST
T_fus	[183.60; 185.75]	K
T_fus	183.60	K	KDB
T_fus	183.90	K	Aq. Solubility Prediction
T_fus	184.65	K	NIST
T_fus	185.75 ± 0.50	K	NIST
T_fus	185.35	K	NIST
T_triple	[184.60; 185.26]	K
T_triple	185.26 ± 0.05	K	NIST
T_triple	185.25 ± 0.06	K	NIST
T_triple	185.20 ± 0.05	K	NIST
T_triple	184.67 ± 0.10	K	NIST
T_triple	184.60 ± 0.30	K	NIST
T_triple	184.60 ± 0.15	K	NIST
V_c	[0.222; 0.223]	m³/kmol
V_c	0.222	m³/kmol	KDB
V_c	0.222	m³/kmol	NIST
V_c	0.223 ± 0.003	m³/kmol	NIST
Z_c	0.2502460		KDB
Z_ra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[103.06; 148.10]	J/mol×K	[358.72; 597.25]

C_p,gas	103.06	J/mol×K	358.72	NIST
C_p,gas	105.70 ± 1.60	J/mol×K	365.75	NIST
C_p,gas	105.77	J/mol×K	371.15	NIST
C_p,gas	106.29	J/mol×K	373.15	NIST
C_p,gas	108.10 ± 1.60	J/mol×K	378.85	NIST
C_p,gas	109.20 ± 1.60	J/mol×K	384.95	NIST
C_p,gas	110.08	J/mol×K	391.15	NIST
C_p,gas	110.80 ± 1.60	J/mol×K	393.65	NIST
C_p,gas	111.65	J/mol×K	398.15	NIST
C_p,gas	113.00 ± 1.60	J/mol×K	405.35	NIST
C_p,gas	114.35	J/mol×K	411.15	NIST
C_p,gas	117.02	J/mol×K	423.15	NIST
C_p,gas	118.70	J/mol×K	431.15	NIST
C_p,gas	122.10	J/mol×K	448.15	NIST
C_p,gas	122.80	J/mol×K	451.15	NIST
C_p,gas	121.70 ± 1.60	J/mol×K	453.15	NIST
C_p,gas	124.20 ± 1.60	J/mol×K	466.75	NIST
C_p,gas	127.01	J/mol×K	473.15	NIST
C_p,gas	126.70 ± 1.60	J/mol×K	480.55	NIST
C_p,gas	130.30 ± 1.60	J/mol×K	499.75	NIST
C_p,gas	132.90 ± 1.60	J/mol×K	513.95	NIST
C_p,gas	137.50 ± 1.60	J/mol×K	539.05	NIST
C_p,gas	142.60 ± 1.60	J/mol×K	567.05	NIST
C_p,gas	148.10 ± 1.60	J/mol×K	597.25	NIST
C_p,liquid	[149.75; 218.14]	J/mol×K	[292.84; 600.10]

C_p,liquid	149.75	J/mol×K	292.84	NIST
C_p,liquid	151.00	J/mol×K	293.10	NIST
C_p,liquid	152.30	J/mol×K	293.10	NIST
C_p,liquid	154.00	J/mol×K	298.00	NIST
C_p,liquid	163.60	J/mol×K	298.00	NIST
C_p,liquid	159.99	J/mol×K	298.04	NIST
C_p,liquid	180.30	J/mol×K	298.10	NIST
C_p,liquid	161.20	J/mol×K	298.15	NIST
C_p,liquid	154.75	J/mol×K	298.15	NIST
C_p,liquid	154.43	J/mol×K	298.15	NIST
C_p,liquid	162.80	J/mol×K	298.20	NIST
C_p,liquid	169.90	J/mol×K	303.00	NIST
C_p,liquid	172.40	J/mol×K	303.20	NIST
C_p,liquid	165.60	J/mol×K	311.60	NIST
C_p,liquid	180.30	J/mol×K	324.00	NIST
C_p,liquid	218.14	J/mol×K	508.16	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	208.53	J/mol×K	508.18	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	195.91	J/mol×K	508.28	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	187.80	J/mol×K	508.37	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	185.69	J/mol×K	508.47	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	186.90	J/mol×K	508.57	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	192.91	J/mol×K	508.67	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	186.90	J/mol×K	508.76	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	179.56	J/mol×K	509.35	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	180.16	J/mol×K	509.45	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	178.84	J/mol×K	509.55	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	179.98	J/mol×K	509.64	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	177.46	J/mol×K	509.79	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	177.28	J/mol×K	509.99	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	178.12	J/mol×K	510.14	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	177.94	J/mol×K	510.23	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	176.68	J/mol×K	510.33	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	178.60	J/mol×K	510.48	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	176.74	J/mol×K	516.90	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	176.80	J/mol×K	516.99	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	176.80	J/mol×K	517.08	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	172.17	J/mol×K	517.27	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	173.13	J/mol×K	521.87	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	168.57	J/mol×K	521.96	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	173.19	J/mol×K	522.14	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	168.63	J/mol×K	522.33	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	171.63	J/mol×K	522.42	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	173.85	J/mol×K	522.51	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	175.18	J/mol×K	522.60	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	168.39	J/mol×K	530.01	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	168.27	J/mol×K	532.04	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	168.33	J/mol×K	535.11	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	168.39	J/mol×K	540.06	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	168.63	J/mol×K	545.13	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	169.77	J/mol×K	560.04	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	173.85	J/mol×K	570.09	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	174.22	J/mol×K	580.16	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	176.38	J/mol×K	590.07	Influence of nanofluid instability on thermodynamic properties near the critical point
C_p,liquid	178.60	J/mol×K	600.10	Influence of nanofluid instability on thermodynamic properties near the critical point
η	[0.0006241; 0.0024050]	Pa×s	[293.00; 343.15]

η	0.0021000	Pa×s	293.00	Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
η	0.0022256	Pa×s	293.15	Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η	0.0023820	Pa×s	293.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0023820	Pa×s	293.15	Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η	0.0024050	Pa×s	293.15	Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K
η	0.0023621	Pa×s	293.15	Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η	0.0023820	Pa×s	293.15	Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η	0.0023840	Pa×s	293.15	Viscosities and Densities of Binary Mixtures of (N-Acetylmorpholine + Alkanols) from (293.15 to 323.15) K
η	0.0020610	Pa×s	298.15	Studies of mixing properties of binary systems of 2-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K
η	0.0020450	Pa×s	298.15	Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η	0.0019102	Pa×s	298.15	Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η	0.0020690	Pa×s	298.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0020620	Pa×s	298.15	Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K
η	0.0020450	Pa×s	298.15	Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η	0.0020550	Pa×s	298.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0020550	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0014900	Pa×s	303.00	Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
η	0.0017880	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0017370	Pa×s	303.15	Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η	0.0017694	Pa×s	303.15	Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η	0.0017580	Pa×s	303.15	Studies of mixing properties of binary systems of 2-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K
η	0.0017630	Pa×s	303.15	Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η	0.0017919	Pa×s	303.15	Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
η	0.0017430	Pa×s	303.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0017880	Pa×s	303.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0017820	Pa×s	303.15	Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K
η	0.0017520	Pa×s	303.15	Viscosities and Densities of Binary Mixtures of (N-Acetylmorpholine + Alkanols) from (293.15 to 323.15) K
η	0.0017630	Pa×s	303.15	Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η	0.0015630	Pa×s	308.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0015730	Pa×s	308.15	Studies of mixing properties of binary systems of 2-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K
η	0.0015242	Pa×s	308.15	Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η	0.0015529	Pa×s	308.15	Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
η	0.0015630	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0011300	Pa×s	313.00	Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
η	0.0013554	Pa×s	313.15	Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
η	0.0012880	Pa×s	313.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0013297	Pa×s	313.15	Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η	0.0013472	Pa×s	313.15	Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η	0.0013790	Pa×s	313.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0013780	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0013350	Pa×s	313.15	Viscosities and Densities of Binary Mixtures of (N-Acetylmorpholine + Alkanols) from (293.15 to 323.15) K
η	0.0011822	Pa×s	318.15	Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
η	0.0010411	Pa×s	323.15	Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
η	0.0010380	Pa×s	323.15	Viscosities and Densities of Binary Mixtures of (N-Acetylmorpholine + Alkanols) from (293.15 to 323.15) K
η	0.0010145	Pa×s	323.15	Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η	0.0010020	Pa×s	323.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0007890	Pa×s	333.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
η	0.0006241	Pa×s	333.15	Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η	0.0006260	Pa×s	343.15	Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
σ_cond	[5.20e-05; 8.43e-05]	S/m	[298.15; 318.15]

σ_cond	5.20e-05	S/m	298.15	Electrical Conductivity of Caprolactam Tetrabutylammonium Bromide Ionic Liquids in Aqueous and Alcohol Binary Systems
σ_cond	7.00e-05	S/m	303.15	Electrical Conductivity of Caprolactam Tetrabutylammonium Bromide Ionic Liquids in Aqueous and Alcohol Binary Systems
σ_cond	7.50e-05	S/m	308.15	Electrical Conductivity of Caprolactam Tetrabutylammonium Bromide Ionic Liquids in Aqueous and Alcohol Binary Systems
σ_cond	8.08e-05	S/m	313.15	Electrical Conductivity of Caprolactam Tetrabutylammonium Bromide Ionic Liquids in Aqueous and Alcohol Binary Systems
σ_cond	8.43e-05	S/m	318.15	Electrical Conductivity of Caprolactam Tetrabutylammonium Bromide Ionic Liquids in Aqueous and Alcohol Binary Systems
Δ_fusH	[5.30; 5.41]	kJ/mol	[184.60; 185.20]

Δ_fusH	5.30	kJ/mol	184.60	NIST
Δ_fusH	5.30	kJ/mol	184.60	NIST
Δ_fusH	5.37	kJ/mol	184.67	NIST
Δ_fusH	5.37	kJ/mol	184.70	NIST
Δ_fusH	5.41	kJ/mol	185.20	NIST
Δ_fusH	5.41	kJ/mol	185.20	NIST
Δ_fusH	5.41	kJ/mol	185.20	NIST
Δ_vapH	[10.50; 50.30]	kJ/mol	[211.50; 503.00]

Δ_vapH	50.30	kJ/mol	211.50	NIST
Δ_vapH	45.50	kJ/mol	318.00	NIST
Δ_vapH	45.70	kJ/mol	323.50	NIST
Δ_vapH	43.20	kJ/mol	324.00	NIST
Δ_vapH	43.40 ± 0.08	kJ/mol	324.11	NIST
Δ_vapH	44.80	kJ/mol	327.50	NIST
Δ_vapH	42.70 ± 0.10	kJ/mol	330.00	NIST
Δ_vapH	43.20	kJ/mol	338.50	NIST
Δ_vapH	41.70	kJ/mol	339.00	NIST
Δ_vapH	43.10	kJ/mol	343.50	NIST
Δ_vapH	42.80	kJ/mol	346.00	NIST
Δ_vapH	41.00 ± 0.10	kJ/mol	346.00	NIST
Δ_vapH	39.80 ± 0.10	kJ/mol	355.00	NIST
Δ_vapH	39.80	kJ/mol	355.00	NIST
Δ_vapH	39.80	kJ/mol	355.00	NIST
Δ_vapH	39.85	kJ/mol	355.40	NIST
Δ_vapH	39.83	kJ/mol	355.50	KDB
Δ_vapH	42.00	kJ/mol	357.50	NIST
Δ_vapH	38.90 ± 0.10	kJ/mol	363.00	NIST
Δ_vapH	41.30	kJ/mol	366.50	NIST
Δ_vapH	41.10	kJ/mol	387.00	NIST
Δ_vapH	39.20	kJ/mol	420.00	NIST
Δ_vapH	29.70	kJ/mol	423.00	NIST
Δ_vapH	39.10	kJ/mol	451.50	NIST
Δ_vapH	23.70	kJ/mol	453.00	NIST
Δ_vapH	35.30	kJ/mol	480.50	NIST
Δ_vapH	16.50	kJ/mol	483.00	NIST
Δ_vapH	10.50	kJ/mol	503.00	NIST
P_vap	[5.78; 4362.00]	kPa	[297.80; 503.15]

P_vap	5.78	kPa	297.80	An experimental investigation and modelling of the thermal and caloric properties of nanofluids isopropyl alcohol - Al2O3 nanoparticles
P_vap	5.80	kPa	298.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	8.00	kPa	303.10	An experimental investigation and modelling of the thermal and caloric properties of nanofluids isopropyl alcohol - Al2O3 nanoparticles
P_vap	7.93	kPa	303.15	Solubility of Carbonyl Sulfide in Aqueous Solutions of Ethylene Glycol at Temperatures from (308.15 K to 323.15) K
P_vap	7.86	kPa	303.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	10.72	kPa	308.15	Solubility of Carbonyl Sulfide in Aqueous Solutions of Ethylene Glycol at Temperatures from (308.15 K to 323.15) K
P_vap	10.52	kPa	308.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	13.77	kPa	313.11	Vapour liquid equilibrium for the 2-methylpropane + methanol, +ethanol, +2-propanol, +2-butanol and +2-methyl-2-propanol systems at 313.15K
P_vap	13.94	kPa	313.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	16.22	kPa	315.80	An experimental investigation and modelling of the thermal and caloric properties of nanofluids isopropyl alcohol - Al2O3 nanoparticles
P_vap	17.46	kPa	317.07	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	17.98	kPa	317.65	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	18.39	kPa	318.10	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	18.24	kPa	318.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	19.01	kPa	318.73	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	19.48	kPa	319.19	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	20.03	kPa	319.72	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	20.52	kPa	320.19	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	21.00	kPa	320.65	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	21.49	kPa	321.11	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	22.03	kPa	321.58	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	22.55	kPa	322.07	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	23.03	kPa	322.47	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	23.52	kPa	322.91	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	23.64	kPa	323.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	23.47	kPa	323.16	Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
P_vap	23.60	kPa	323.19	Vapor Liquid Equilibrium for Butane + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-Propanol (TBA) at 323 K
P_vap	24.02	kPa	323.32	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	24.51	kPa	323.71	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	25.03	kPa	324.13	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	25.48	kPa	324.49	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	26.04	kPa	324.94	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	26.52	kPa	325.30	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	27.08	kPa	325.72	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	27.69	kPa	326.18	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	28.19	kPa	326.53	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	28.83	kPa	326.99	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	29.45	kPa	327.46	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	30.08	kPa	327.86	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	30.35	kPa	328.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	30.96	kPa	328.47	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	31.86	kPa	329.06	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	32.76	kPa	329.64	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	33.77	kPa	330.26	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	34.52	kPa	330.73	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	35.48	kPa	331.32	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	36.37	kPa	331.83	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	36.47	kPa	332.03	Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
P_vap	36.06	kPa	332.10	An experimental investigation and modelling of the thermal and caloric properties of nanofluids isopropyl alcohol - Al2O3 nanoparticles
P_vap	37.45	kPa	332.44	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	38.41	kPa	332.99	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	38.59	kPa	333.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	39.33	kPa	333.50	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	39.54	kPa	333.72	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	40.00	kPa	333.94	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
P_vap	40.41	kPa	334.10	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	41.44	kPa	334.60	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	42.44	kPa	335.12	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	43.46	kPa	335.64	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	44.38	kPa	336.11	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	45.32	kPa	336.55	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	46.34	kPa	337.07	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	47.28	kPa	337.50	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	48.35	kPa	337.98	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	48.66	kPa	338.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	49.34	kPa	338.45	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	50.25	kPa	338.86	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	51.26	kPa	339.30	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	52.33	kPa	339.72	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	53.01	kPa	340.04	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	53.33	kPa	340.18	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
P_vap	53.94	kPa	340.43	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	55.03	kPa	340.89	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	55.03	kPa	340.98	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	55.92	kPa	341.25	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	56.96	kPa	341.69	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	58.05	kPa	342.09	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	59.04	kPa	342.48	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	59.93	kPa	342.82	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	60.00	kPa	342.87	Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
P_vap	60.66	kPa	343.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	60.66	kPa	343.19	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	60.91	kPa	343.20	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	61.30	kPa	343.44	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	61.94	kPa	343.59	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	62.98	kPa	343.96	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	63.92	kPa	344.32	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	64.96	kPa	344.68	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	63.92	kPa	344.70	An experimental investigation and modelling of the thermal and caloric properties of nanofluids isopropyl alcohol - Al2O3 nanoparticles
P_vap	65.23	kPa	344.86	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	65.97	kPa	345.05	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	66.66	kPa	345.25	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
P_vap	66.84	kPa	345.35	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	68.03	kPa	345.75	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	69.14	kPa	346.13	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	69.47	kPa	346.33	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	70.12	kPa	346.46	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	72.04	kPa	347.11	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	74.18	kPa	347.79	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	75.22	kPa	348.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	75.27	kPa	348.21	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	75.96	kPa	348.37	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	77.81	kPa	348.95	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	79.34	kPa	349.48	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	79.99	kPa	349.55	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
P_vap	80.00	kPa	349.60	Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
P_vap	79.96	kPa	349.61	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	81.58	kPa	350.08	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	83.94	kPa	350.75	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	85.15	kPa	351.19	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	85.47	kPa	351.21	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	87.17	kPa	351.69	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	88.63	kPa	352.09	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	90.24	kPa	352.54	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	90.34	kPa	352.63	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	92.44	kPa	353.15	Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
P_vap	92.57	kPa	353.16	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	93.32	kPa	353.30	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
P_vap	93.80	kPa	353.30	Isothermal vapor liquid equilibrium for binary mixtures containing furfural and its derivatives
P_vap	93.41	kPa	353.46	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	94.46	kPa	353.66	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	96.15	kPa	354.17	Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
P_vap	96.49	kPa	354.20	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	98.05	kPa	354.59	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	98.66	kPa	354.67	Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
P_vap	100.00	kPa	355.06	Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
P_vap	100.03	kPa	355.09	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	100.00	kPa	355.09	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	101.30	kPa	355.15	Multiphase equilibria for mixtures containing water, isopropanol, propionic acid, and isopropyl propionate
P_vap	101.30	kPa	355.33	Vapor Liquid Equilibria for Ternary Mixtures of Isopropyl Alcohol, Isopropyl Acetate, and DMSO at 101.3 kPa
P_vap	101.30	kPa	355.35	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
P_vap	101.28	kPa	355.38	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	101.06	kPa	355.40	Ammonium-Based Ionic Liquid as an Entrainer for the Separation of n-Propanol + Water and Isopropanol + Water Mixtures
P_vap	101.00	kPa	355.40	Experimental studies and thermodynamic analysis of isobaric vapor-liquid-liquid equilibria of 2-propanol + water system using n-propyl acetate and isopropyl acetate as entrainers
P_vap	101.54	kPa	355.41	Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
P_vap	101.07	kPa	355.42	Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
P_vap	101.30	kPa	355.45	Isobaric (vapour + liquid) equilibrium for (2-propanol + water + ammonium thiocyanate): Fitting the data by an empirical equation
P_vap	101.32	kPa	355.60	Acetonitrile Dehydration via Extractive Distillation Using Low Transition Temperature Mixtures as Entrainers
P_vap	101.32	kPa	355.65	Isobaric Vapor-Liquid Equilibrium for (Propan-2-ol + Water + 1-Butyl-3-methylimidazolium Tetrafluoroborate)
P_vap	101.30	kPa	355.71	A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
P_vap	103.44	kPa	355.93	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	105.38	kPa	356.40	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	106.91	kPa	356.76	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	108.63	kPa	357.16	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	110.13	kPa	357.52	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	111.88	kPa	357.93	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	113.79	kPa	358.35	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	115.10	kPa	358.65	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	116.64	kPa	358.98	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	118.64	kPa	359.43	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	120.24	kPa	359.77	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	121.30	kPa	359.95	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
P_vap	122.11	kPa	360.16	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	124.03	kPa	360.57	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	125.62	kPa	360.90	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	127.12	kPa	361.21	Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
P_vap	127.36	kPa	361.26	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	129.08	kPa	361.62	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	130.93	kPa	361.98	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	132.35	kPa	362.26	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	133.65	kPa	362.52	Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
P_vap	144.10	kPa	364.50	Vapour liquid equilibrium for the systems butane + methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K
P_vap	144.50	kPa	364.50	Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
P_vap	144.10	kPa	364.51	Vapor Liquid Equilibrium for the Systems trans-2-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
P_vap	144.20	kPa	364.51	Vapor Liquid Equilibrium for the Systems 2-Methylpropane + Methanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
P_vap	143.90	kPa	364.52	Vapor-Liquid Equilibrium for the cis-2-Butene + Methanol, + 2-Propanol, + 2-Butanol, + 2-Methyl-2-propanol Systems at 364.5 K
P_vap	152.55	kPa	366.10	Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
P_vap	161.30	kPa	367.65	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
P_vap	177.97	kPa	370.40	Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
P_vap	200.10	kPa	373.50	Isothermal vapor liquid equilibrium for binary mixtures containing furfural and its derivatives
P_vap	201.30	kPa	373.65	Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
P_vap	203.40	kPa	374.20	Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
P_vap	228.82	kPa	377.60	Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
P_vap	254.25	kPa	380.80	Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
P_vap	593.80	kPa	408.30	Isothermal vapor liquid equilibrium for binary mixtures containing furfural and its derivatives
P_vap	1610.00	kPa	450.00	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	1640.00	kPa	451.50	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	2040.00	kPa	461.50	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	2030.00	kPa	462.50	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	2460.00	kPa	469.00	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	2420.00	kPa	469.00	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	2780.00	kPa	477.00	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	2740.00	kPa	477.00	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	3060.00	kPa	482.00	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	3090.00	kPa	482.00	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	3081.00	kPa	483.15	Measurement and correlation of vapor-liquid equilibria for the 2-propanol + n-hexane system near the critical
P_vap	3500.00	kPa	489.00	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	3460.00	kPa	489.50	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	3677.00	kPa	493.15	Measurement and correlation of vapor-liquid equilibria for the 2-propanol + n-hexane system near the critical
P_vap	3970.00	kPa	494.50	Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 K
P_vap	4362.00	kPa	503.15	Measurement and correlation of vapor-liquid equilibria for the 2-propanol + n-hexane system near the critical
n₀	[1.35540; 1.38000]		[293.15; 323.15]

n₀	1.37660		293.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n₀	1.37707		293.15	Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
n₀	1.37740		293.15	Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
n₀	1.37740		293.15	Vapor liquid equilibria and excess volumes of the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate at 101.325 kPa
n₀	1.37740		293.15	Excess Properties and Phase Equilibria for the Potential Biofuel System of Propan-2-ol and 2-Methyl-propan-1-ol at 333.15, 343.15, and 353.15 K
n₀	1.37718		293.15	Vapor Liquid Equilibrium for Methyl Isobutyl Ketone (MIBK) + (1-Propanol or 2-Propanol) Binary Mixtures
n₀	1.37709		293.15	Liquid Liquid Equilibria of Methanol, Ethanol, and Propan-2-ol with Water and Dodecane
n₀	1.37800		293.15	Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
n₀	1.37707		293.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n₀	1.37740		293.15	Vapour-liquid equilibrium of carboxylic acid alcohol binary systems:2-Propanol + butyric acid, 2-butanol + butyric acid and 2-methyl-1-propanol + butyric acid
n₀	1.37710		293.20	Isobaric Vapor Liquid Equilibria for Binary Mixtures of .gamma.-Valerolactone + Methanol, Ethanol, and 2-Propanol
n₀	1.37710		293.20	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
n₀	1.37880		295.15	Isobaric Vapor Liquid Equilibrium Data for Binary Mixtures of 1-Phenylethanone with a Few Alcohols at 95.2 kPa
n₀	1.37580		298.00	Determination of Physicochemical Parameters of Sodium Dodecyl Sulfate in Aqueous Micellar Solutions Containing Short-Chain Alcohols
n₀	1.37450		298.15	Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n₀	1.37495		298.15	Physical Properties of Binary Mixtures of the Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate with Several Alcohols at T = (298.15, 313.15, and 328.15) K and Atmospheric Pressure
n₀	1.37540		298.15	sobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Diisopropyl Ether, 2-Propyl Alcohol, and n-Butyl Propionate at 101.3 kPa
n₀	1.37520		298.15	(Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
n₀	1.37450		298.15	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
n₀	1.37540		298.15	Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol and 2-Propanol with 2-Butanone and Butyl Propionate at 101.3 kPa
n₀	1.37450		298.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
n₀	1.37650		298.15	Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
n₀	1.37496		298.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n₀	1.37540		298.15	Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Diisopropyl Ether, 2-Propyl Alcohol, and 3-Methyl-1-Butanol
n₀	1.37510		298.15	(Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
n₀	1.37496		298.15	Ternary (liquid + liquid) equilibria of the azeotrope (ethyl acetate + 2-propanol) with different ionic liquids at T = 298.15 K
n₀	1.37500		298.15	Isobaric (vapour + liquid) equilibrium for N-methyl-2-pyrrolidone with branched alcohols
n₀	1.37410		298.15	Application of the ERAS model to volumetric properties of binary mixtures of banana oil with primary and secondary alcohols (C1- C4) at different temperatures
n₀	1.37500		298.15	Effect of the temperature on the physical properties of pure 1-propyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and characterization of its binary mixtures with alcohols
n₀	1.37504		298.15	Isothermal (vapour + liquid) equilibria in the binary and ternary systems composed of 2-propanol, 2,2,4-trimethylpentane, and 2,4-dimethyl-3-pentanone
n₀	1.37518		298.15	(Vapour + liquid) equilibria for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane at P = 101.3 kPa
n₀	1.37500		298.15	Density and Viscosity Experimental Data of the Ternary Mixtures 1-Propanol or 2-Propanol + Water + 1-Ethyl-3-methylimidazolium Ethylsulfate. Correlation and Prediction of Physical Properties of the Ternary Systems
n₀	1.37527		298.15	Densities, speeds of sound, and refractive indices for binary mixtures of 1-butyl-3-methylimidazolium methyl sulphate ionic liquid with alcohols at T = (298.15, 303.15, 308.15, and 313.15) K
n₀	1.37520		298.15	Vapor-Liquid Equilibrium and Excess Gibbs Energies of Hexane + N,N-Dimethyl Formamide, 2-Methylpropan-2-ol + 2-Aminophenol, N,N-Dimethyl Formamide, and 2-Propanol + Diisopropyl Amine at 94.4 kPa
n₀	1.37496		298.15	Ternary Liquid-Liquid Equilibria Ethanol + 2-Butanone + 1-Butyl-3-methylimidazolium Hexafluorophosphate, 2-Propanol + 2-Butanone + 1-Butyl-3-methylimidazolium Hexafluorophosphate, and 2-Butanone + 2-Propanol + 1,3-Dimethylimidazolium Methyl Sulfate at 298.15 K
n₀	1.37509		298.15	Vapor-Liquid Equilibria for Binary and Ternary Mixtures of 1,3-Dioxolane, 2-Propanol, and 2,2,4-Trimethylpentane at 101.3 kPa
n₀	1.37523		298.15	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
n₀	1.37560		298.15	Ternary (liquid + liquid) equilibria for the extraction of ethanol, or 2-propanol from aqueous solutions with 1,1'-oxybis(butane) at different temperatures
n₀	1.37480		298.15	Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
n₀	1.37450		298.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n₀	1.35540		298.15	Vapor Liquid Equilibrium for Ternary and Binary Mixtures of 2-Isopropoxypropane, 2-Propanol, and N,N-Dimethylacetamide at 101.3 kPa
n₀	1.37760		298.15	Investigation on vapor liquid equilibrium for 2-propanol + 1-butanol + 1-pentanol at 101.3 kPa
n₀	1.37502		298.15	Isobaric vapour liquid equilibria and physical properties for isopropyl acetate + isopropanol + 1-butyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide mixtures
n₀	1.37530		298.15	Molar excess enthalpies and molar excess volumes of formamide + 1-propanol or 2-propanol and thermodynamic modeling by Prigogine-Flory-Patterson theory and Treszczanowicz-Benson association model
n₀	1.37497		298.15	Isobaric vapour liquid equilibria for binary systems of 2-butanone with ethanol, 1-propanol, and 2-propanol at 20 and 101.3 kPa
n₀	1.37500		298.15	Densities, Excess Molar Volumes, and Refractive Properties of the Binary Mixtures of the Amino Acid Ionic Liquid [bmim][Gly] with 1-Butanol or Isopropanol at T = (298.15 to 313.15) K
n₀	1.37504		298.15	Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, 3-methyl-2-butanone and 2,2,4-trimethylpentane
n₀	1.37540		298.15	Effect of pressure and the capability of 2-methoxyethanol as a solvent in the behaviour of a diisopropyl ether isopropyl alcohol azeotropic mixture
n₀	1.37500		298.15	Excess volumes and excess enthalpies of N-methyl-2-pyrrolidone with branched alcohols
n₀	1.37520		298.15	Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
n₀	1.38000		298.15	Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
n₀	1.37500		298.15	Vapor-Liquid Equilibria Data for Methanol + 2-Propanol+ 2-Methyl-2-butanol and Constituent Binary Systems at 101.3 kPa
n₀	1.37520		298.15	Effect of anion fluorination in 1-ethyl-3-methylimidazolium as solvent for the liquid extraction of ethanol from ethyl tert-butyl ether
n₀	1.37496		298.15	Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
n₀	1.37510		298.15	Physical Properties of Binary and Ternary Mixtures of 2-Propanol, Water, and 1-Butyl-3-methylimidazolium Tetrafluoroborate Ionic Liquid
n₀	1.37510		298.20	Isobaric Vapor Liquid Equilibria for Binary Mixtures of .gamma.-Valerolactone + Methanol, Ethanol, and 2-Propanol
n₀	1.37210		303.15	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
n₀	1.37314		303.15	Densities, speeds of sound, and refractive indices for binary mixtures of 1-butyl-3-methylimidazolium methyl sulphate ionic liquid with alcohols at T = (298.15, 303.15, 308.15, and 313.15) K
n₀	1.37410		303.15	Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
n₀	1.37400		303.15	Densities, Excess Molar Volumes, and Refractive Properties of the Binary Mixtures of the Amino Acid Ionic Liquid [bmim][Gly] with 1-Butanol or Isopropanol at T = (298.15 to 313.15) K
n₀	1.37278		303.15	Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
n₀	1.37278		303.15	Mixing properties of binary mixtures presenting azeotropes at several temperatures
n₀	1.37360		303.15	Solute-Solvent and Solvent-Solvent Interactions of Menthol in Isopropyl Alcohol and its Binary Mixtures with Methyl Salicylate by Volumetric, Viscometric, Interferometric and Refractive Index Techniques.
n₀	1.37410		303.15	Experimental study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
n₀	1.37240		303.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n₀	1.37210		303.15	Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n₀	1.37300		308.15	Densities, Excess Molar Volumes, and Refractive Properties of the Binary Mixtures of the Amino Acid Ionic Liquid [bmim][Gly] with 1-Butanol or Isopropanol at T = (298.15 to 313.15) K
n₀	1.37093		308.15	Densities, speeds of sound, and refractive indices for binary mixtures of 1-butyl-3-methylimidazolium methyl sulphate ionic liquid with alcohols at T = (298.15, 303.15, 308.15, and 313.15) K
n₀	1.37030		308.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n₀	1.37063		308.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Ternary Mixtures of 2-Propanol + Benzyl Alcohol + 2-Phenylethanol at T = 308.15 K
n₀	1.37160		308.15	Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
n₀	1.37020		308.15	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
n₀	1.37020		308.15	Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n₀	1.36870		313.15	Densities, speeds of sound, and refractive indices for binary mixtures of 1-butyl-3-methylimidazolium methyl sulphate ionic liquid with alcohols at T = (298.15, 303.15, 308.15, and 313.15) K
n₀	1.37200		313.15	Densities, Excess Molar Volumes, and Refractive Properties of the Binary Mixtures of the Amino Acid Ionic Liquid [bmim][Gly] with 1-Butanol or Isopropanol at T = (298.15 to 313.15) K
n₀	1.36040		323.15	Physical Properties of Binary and Ternary Mixtures of 2-Propanol, Water, and 1-Butyl-3-methylimidazolium Tetrafluoroborate Ionic Liquid
ρ_l	[738.91; 810.90]	kg/m³	[263.10; 343.30]

ρ_l	810.90	kg/m³	263.10	Effect of Al2O3 Nanoparticles Additives on the Density, Saturated Vapor Pressure, Surface Tension and Viscosity of Isopropyl Alcohol
ρ_l	797.50	kg/m³	278.15	Thermophysical properties of binary mixtures of 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate ionic liquid with alcohols at several temperatures
ρ_l	795.30	kg/m³	283.10	Effect of Al2O3 Nanoparticles Additives on the Density, Saturated Vapor Pressure, Surface Tension and Viscosity of Isopropyl Alcohol
ρ_l	794.00	kg/m³	283.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρ_l	793.31	kg/m³	283.15	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
ρ_l	793.67	kg/m³	283.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	789.68	kg/m³	288.15	Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρ_l	789.22	kg/m³	288.15	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
ρ_l	789.18	kg/m³	288.15	Mass density, sound velocity, mixing enthalpy, 1H NMR, Ab initio calculations and intermolecular interactions in binary mixtures of N-methylimidazole + water, +methanol, +ethanol, +1-propanol, +2-propanol
ρ_l	789.34	kg/m³	288.15	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
ρ_l	789.34	kg/m³	288.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρ_l	789.18	kg/m³	288.15	Thermophysical Characterization of the Mixtures of the Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate with 1-Propanol or 2-Propanol
ρ_l	789.40	kg/m³	288.15	Thermophysical properties of binary mixtures of 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate ionic liquid with alcohols at several temperatures
ρ_l	789.58	kg/m³	288.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	789.41	kg/m³	288.15	Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols
ρ_l	789.22	kg/m³	288.15	The excess molar volume and the molar surface Gibbs energy of the binary of the ether-functionalized ionic liquids [C22O1IM][TfO] with ethanol and isomeric propanols at T = (288.15-318.15) K
ρ_l	786.00	kg/m³	293.00	KDB
ρ_l	785.25	kg/m³	293.15	Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
ρ_l	785.40	kg/m³	293.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρ_l	785.40	kg/m³	293.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρ_l	784.96	kg/m³	293.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρ_l	785.09	kg/m³	293.15	The excess molar volume and the molar surface Gibbs energy of the binary of the ether-functionalized ionic liquids [C22O1IM][TfO] with ethanol and isomeric propanols at T = (288.15-318.15) K
ρ_l	785.29	kg/m³	293.15	Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols
ρ_l	785.40	kg/m³	293.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρ_l	785.10	kg/m³	293.15	Volumetric Properties of Binary and Ternary Liquid Mixtures of 1-Propanol (1) + 2-Propanol (2) + Water (3) at Different Temperatures and Ambient Pressure (81.5 kPa)
ρ_l	785.30	kg/m³	293.15	Densities and Viscosities of Binary Mixtures Containing 1,3-Dimethylimidazolium Dimethylphosphate and Alcohols
ρ_l	785.24	kg/m³	293.15	Measurement and Correlation of the Excess Properties of Ternary Mixture of {x1[Hmim][BF4] + x21-Propanol + x32-Propanol} at Different Temperatures
ρ_l	785.00	kg/m³	293.15	Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
ρ_l	785.90	kg/m³	293.15	Measurement and correlation of liquid liquid equilibrium data for 2-methyl-1-propanol + 2-propanol + water at several temperatures
ρ_l	785.20	kg/m³	293.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρ_l	785.81	kg/m³	293.15	Investigation on molecular interactions of antibiotics in alcohols using volumetric and acoustic studies at different temperatures
ρ_l	785.40	kg/m³	293.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρ_l	785.08	kg/m³	293.15	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
ρ_l	785.40	kg/m³	293.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρ_l	785.10	kg/m³	293.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρ_l	785.74	kg/m³	293.15	Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
ρ_l	786.00	kg/m³	293.15	Effect of imidazolium-based ionic liquid on vapor-liquid equilibria of 2-propanol + acetonitrile binary system at 101.3 kPa
ρ_l	786.00	kg/m³	293.15	Composition and Temperature Dependence of Density, Surface Tension, and Viscosity of EMIM DEP/MMIM DMP + Water + 1-Propanol/2-Propanol Ternary Mixtures and Their Mathematical Representation Using the Jouyban Acree Model
ρ_l	785.76	kg/m³	293.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρ_l	784.90	kg/m³	293.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρ_l	785.10	kg/m³	293.15	Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
ρ_l	785.10	kg/m³	293.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρ_l	785.35	kg/m³	293.15	Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρ_l	791.50	kg/m³	293.15	Liquid Densities and Speed of Sound for Ionic Liquid (2-HEAA and 2-HDEAA) + Alcohol (1-Propanol and 2-Propanol) Mixtures at T = (293.15-323.15 K) and Atmospheric Pressure
ρ_l	785.18	kg/m³	293.15	Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
ρ_l	785.44	kg/m³	293.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	786.91	kg/m³	293.15	Experimental vapour - liquid equilibrium data of the quaternary system Methanol (1) + Isopropyl Alcohol (2) + Water (3) + Glycerol (4) along with Isopropyl Alcohol (2) + Glycerol (4) and Isopropyl Alcohol (2) + Water (3) binary data at atmospheric and sub-atmospheric pressures.
ρ_l	784.30	kg/m³	295.30	Effect of Al2O3 Nanoparticles Additives on the Density, Saturated Vapor Pressure, Surface Tension and Viscosity of Isopropyl Alcohol
ρ_l	781.18	kg/m³	298.15	Isobaric vapor-liquid equilibria for the binary and ternary mixtures of 2-propanol, water, and 1,3-propanediol at p = 101.3 kPa: Effect of the 1,3-propanediol addition
ρ_l	780.84	kg/m³	298.15	Thermophysical Characterization of the Mixtures of the Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate with 1-Propanol or 2-Propanol
ρ_l	781.30	kg/m³	298.15	Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
ρ_l	782.45	kg/m³	298.15	Experimental vapour - liquid equilibrium data of the quaternary system Methanol (1) + Isopropyl Alcohol (2) + Water (3) + Glycerol (4) along with Isopropyl Alcohol (2) + Glycerol (4) and Isopropyl Alcohol (2) + Water (3) binary data at atmospheric and sub-atmospheric pressures.
ρ_l	781.23	kg/m³	298.15	ACSExcess Molar Enthalpies of Mixtures of (+-)-Linalool with Several Alkanols
ρ_l	781.05	kg/m³	298.15	Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Ethylenediamine with Alcohols at T = (293.15 to 313.15) K
ρ_l	780.99	kg/m³	298.15	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
ρ_l	780.80	kg/m³	298.15	Determination and prediction of solubilities of active pharmaceutical ingredients in selected organic solvents
ρ_l	780.60	kg/m³	298.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρ_l	780.80	kg/m³	298.15	Density and speed of sound of lithium bromide with organic solvents: Measurement and correlation
ρ_l	782.45	kg/m³	298.15	Isobaric ternary vapour-liquid equilibrium of methanol(1) + diisopropyl ether(2) + isopropyl alcohol(3) along with methanol + isopropyl alcohol binary data at atmospheric and sub-atmospheric pressures
ρ_l	781.31	kg/m³	298.15	Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
ρ_l	780.90	kg/m³	298.15	Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
ρ_l	781.60	kg/m³	298.15	Thermophysical Properties of the Pure Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide and Its Binary Mixtures with Alcohols
ρ_l	780.70	kg/m³	298.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρ_l	781.40	kg/m³	298.15	Phase diagrams of (hexane + methanol + 2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation
ρ_l	781.18	kg/m³	298.15	Densities, surface tensions, and isobaric vapor-liquid equilibria for the mixtures of 2-propanol, water, and 1,2-propanediol
ρ_l	782.45	kg/m³	298.15	Experimental isobaric vapor-liquid equilibrium at atmospheric and sub-atmospheric pressures, excess molar volumes and deviations in molar refractivity from 293.15 K to 318.15 K of diisopropyl ether with methanol and isopropyl alcohol.
ρ_l	781.40	kg/m³	298.15	Determination and Correlation of Liquid-Liquid Equilibria Data for Ternary System Isopropyl Acetate + Isopropanol + Water at Different Temperatures
ρ_l	781.10	kg/m³	298.15	Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρ_l	780.95	kg/m³	298.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρ_l	781.08	kg/m³	298.15	Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρ_l	781.00	kg/m³	298.15	Composition and Temperature Dependence of Density, Surface Tension, and Viscosity of EMIM DEP/MMIM DMP + Water + 1-Propanol/2-Propanol Ternary Mixtures and Their Mathematical Representation Using the Jouyban Acree Model
ρ_l	781.10	kg/m³	298.15	Isobaric Vapor-Liquid Phase Equilibrium Measurements, Correlation, and Prediction for Separation of the Mixtures of Cyclohexanone and Alcohols
ρ_l	779.36	kg/m³	298.15	Vapor Liquid Equilibrium of Mixtures Containing the Following Higher Alcohols: 2-Propanol, 2-Methyl-1-propanol, and 3-Methyl-1-butanol
ρ_l	781.59	kg/m³	298.15	Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
ρ_l	781.10	kg/m³	298.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρ_l	782.00	kg/m³	298.15	Isobaric Vapor-Liquid Equilibrium for the Binary Systems of Sec-butyl Acetate and Ethanol, 1-Propanol, or 2-Propanol at 101.3 kPa
ρ_l	781.10	kg/m³	298.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρ_l	780.90	kg/m³	298.15	A combined experimental and computational investigation of excess molar enthalpies of (nitrobenzene + alkanol) mixtures
ρ_l	780.90	kg/m³	298.15	(Liquid + liquid) equilibria for mixtures of dodecane and ethanol with alkylsulfate-based ionic liquids
ρ_l	780.80	kg/m³	298.15	Measurements and modeling of LLE and HE for (methanol + 2,4,4-trimethyl-1-pentene), and LLE for (water + methanol + 2,4,4-trimethyl-1-pentene)
ρ_l	780.60	kg/m³	298.15	Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
ρ_l	781.08	kg/m³	298.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	781.10	kg/m³	298.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρ_l	780.95	kg/m³	298.15	Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
ρ_l	781.10	kg/m³	298.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρ_l	782.70	kg/m³	298.15	Solubility of androstenedione in lower alcohols
ρ_l	781.18	kg/m³	298.15	Liquid Liquid Equilibria, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
ρ_l	780.79	kg/m³	298.15	Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
ρ_l	781.20	kg/m³	298.15	Excess molar enthalpies of R-fenchone + propan-1-ol or +propan-2-ol. Modeling with COSMO-RS and UNIFAC
ρ_l	781.10	kg/m³	298.15	Solubility and solution thermodynamics of thymol in six pure organic solvents
ρ_l	781.20	kg/m³	298.15	Measurement and correlation of solubility and solution thermodynamics of 1,3-dimethylurea in different solvents from T = (288.15 to 328.15) K
ρ_l	781.11	kg/m³	298.15	Experimental study on the calorimetric data of 2-butoxyethanol with aliphatic alcohols (C1-C4) and correlation with the Wilson, NRTL and UNIQUAC models at T = 298 K
ρ_l	782.70	kg/m³	298.15	Liquid liquid equilibria of 4-methyl-2-pentanone + 1-propanol or 2-propanol + water ternary systems: Measurements and correlation at different temperatures
ρ_l	781.34	kg/m³	298.15	Investigation on molecular interactions of antibiotics in alcohols using volumetric and acoustic studies at different temperatures
ρ_l	781.59	kg/m³	298.15	Thermodynamic and spectral investigations of binary liquid mixturesof 2-butoxy ethanol with alcohols at temperature range of 293.15-313.15 K
ρ_l	798.00	kg/m³	298.15	Liquid Liquid Equilibrium data for the ternary systems of Water, Isopropyl alcohol, and selected entrainers
ρ_l	781.05	kg/m³	298.15	Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
ρ_l	780.91	kg/m³	298.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρ_l	781.05	kg/m³	298.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρ_l	781.21	kg/m³	298.15	Liquid liquid equilibria for the binary system of di-isopropyl ether (DIPE) +water in between 288.15 and 323.15K and the ternary systems of DIPE +water + C1 C4 alcohols at 298.15K
ρ_l	781.21	kg/m³	298.15	Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
ρ_l	780.89	kg/m³	298.15	The excess molar volume and the molar surface Gibbs energy of the binary of the ether-functionalized ionic liquids [C22O1IM][TfO] with ethanol and isomeric propanols at T = (288.15-318.15) K
ρ_l	781.09	kg/m³	298.15	Densities and Viscosities of Binary Mixtures Containing 1,3-Dimethylimidazolium Dimethylphosphate and Alcohols
ρ_l	781.10	kg/m³	298.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρ_l	781.08	kg/m³	298.15	Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols
ρ_l	781.32	kg/m³	298.15	Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
ρ_l	781.40	kg/m³	298.15	Liquid-Liquid Equilibrium for 2,2,2-Trifluoroethanol + Ethanol + Cyclohexane from (288.15 to 308.15) K
ρ_l	781.10	kg/m³	298.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρ_l	780.87	kg/m³	298.15	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
ρ_l	780.91	kg/m³	298.15	Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, diisopropyl ether and 4-methyl-2-pentanone
ρ_l	781.40	kg/m³	298.15	Liquid-Liquid Equilibrium of (Cyclohexane + 2,2,2-Trifluoroethanol) and (Cyclohexane + Methanol) from (278.15 to 318.15) K
ρ_l	781.00	kg/m³	298.15	Thermophysical properties of binary mixtures of 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate ionic liquid with alcohols at several temperatures
ρ_l	780.99	kg/m³	298.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρ_l	781.40	kg/m³	298.15	Effect of Temperature on Phase Equilibrium of the Mixed-Solvent System of (2,2,2-Trifluoroethanol + Methanol + Cyclohexane)
ρ_l	781.35	kg/m³	298.15	Binary Liquid-Liquid Equilibrium (LLE) for Dibutyl Ether (DBE) + Water from (288.15 to 318.15) K and Ternary LLE for Systems of DBE + C1 !less thanless than C4 Alcohols + Water at 298.15 K
ρ_l	781.34	kg/m³	298.15	Binary Liquid-Liquid Equilibrium (LLE) for Methyl tert-Amyl Ether (TAME) + Water from (288.15 to 313.15) K and Ternary LLE for Systems of TAME + C1-C4 Alcohols + Water at 298.15 K
ρ_l	780.98	kg/m³	298.15	Topological investigations of the molecular species and molecular interactions that characterize pyrrolidin-2-one + lower alkanol mixtures
ρ_l	780.35	kg/m³	298.15	Excess enthalpies of binary mixtures of some propylamines + some propanols at 298.15K
ρ_l	781.24	kg/m³	298.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	781.00	kg/m³	298.15	Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
ρ_l	780.69	kg/m³	298.15	Liquid-liquid equilibria and density data for pseudoternary systems of refined soybean oil + (hexanal, or heptanal, or butyric acid, or valeric acid, or caproic acid, or caprylic acid) + dimethyl sulfoxide at 298.15 K
ρ_l	781.50	kg/m³	298.15	Solubility and Liquid-Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa
ρ_l	780.86	kg/m³	298.15	Mass density, sound velocity, mixing enthalpy, 1H NMR, Ab initio calculations and intermolecular interactions in binary mixtures of N-methylimidazole + water, +methanol, +ethanol, +1-propanol, +2-propanol
ρ_l	780.90	kg/m³	298.15	Apparent Molal Volumes and Viscosity B-Coefficients of Acetyl Salicylic Acid (2-Acetoxy Benzoic Acid) Solutions in Higher Alcohols at Different Temperatures
ρ_l	780.89	kg/m³	298.15	Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Methanol, Ethanol, 1-Propanol, and 2-Propanol at Several Temperatures
ρ_l	780.75	kg/m³	298.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρ_l	781.91	kg/m³	298.15	Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
ρ_l	780.85	kg/m³	298.20	A green process for recovery of 1-propanol/2-propanol from their aqueous solutions: Experimental and MD simulation studies
ρ_l	777.47	kg/m³	303.15	Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
ρ_l	776.86	kg/m³	303.15	Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρ_l	776.54	kg/m³	303.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρ_l	776.62	kg/m³	303.15	The excess molar volume and the molar surface Gibbs energy of the binary of the ether-functionalized ionic liquids [C22O1IM][TfO] with ethanol and isomeric propanols at T = (288.15-318.15) K
ρ_l	776.63	kg/m³	303.15	Volumetric Properties of Binary and Ternary Liquid Mixtures of 1-Propanol (1) + 2-Propanol (2) + Water (3) at Different Temperatures and Ambient Pressure (81.5 kPa)
ρ_l	776.57	kg/m³	303.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρ_l	777.30	kg/m³	303.15	Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
ρ_l	776.60	kg/m³	303.15	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
ρ_l	776.80	kg/m³	303.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρ_l	777.50	kg/m³	303.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρ_l	776.97	kg/m³	303.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	776.80	kg/m³	303.15	Densities and Viscosities of Binary Mixtures Containing 1,3-Dimethylimidazolium Dimethylphosphate and Alcohols
ρ_l	776.76	kg/m³	303.15	Measurement and Correlation of the Excess Properties of Ternary Mixture of {x1[Hmim][BF4] + x21-Propanol + x32-Propanol} at Different Temperatures
ρ_l	776.80	kg/m³	303.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρ_l	776.80	kg/m³	303.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	777.00	kg/m³	303.15	Composition and Temperature Dependence of Density, Surface Tension, and Viscosity of EMIM DEP/MMIM DMP + Water + 1-Propanol/2-Propanol Ternary Mixtures and Their Mathematical Representation Using the Jouyban Acree Model
ρ_l	777.28	kg/m³	303.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρ_l	776.81	kg/m³	303.15	Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols
ρ_l	777.00	kg/m³	303.15	Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
ρ_l	776.63	kg/m³	303.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρ_l	776.60	kg/m³	303.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρ_l	776.66	kg/m³	303.15	Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
ρ_l	776.72	kg/m³	303.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρ_l	777.00	kg/m³	303.15	Liquid Densities and Speed of Sound for Ionic Liquid (2-HEAA and 2-HDEAA) + Alcohol (1-Propanol and 2-Propanol) Mixtures at T = (293.15-323.15 K) and Atmospheric Pressure
ρ_l	776.40	kg/m³	303.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρ_l	776.79	kg/m³	303.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρ_l	776.80	kg/m³	303.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρ_l	776.80	kg/m³	303.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρ_l	776.80	kg/m³	303.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρ_l	776.80	kg/m³	303.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρ_l	777.06	kg/m³	303.15	Investigation on molecular interactions of antibiotics in alcohols using volumetric and acoustic studies at different temperatures
ρ_l	776.78	kg/m³	303.15	Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
ρ_l	777.50	kg/m³	303.60	Effect of Al2O3 Nanoparticles Additives on the Density, Saturated Vapor Pressure, Surface Tension and Viscosity of Isopropyl Alcohol
ρ_l	772.10	kg/m³	308.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρ_l	772.40	kg/m³	308.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρ_l	772.46	kg/m³	308.15	Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols
ρ_l	772.27	kg/m³	308.15	The excess molar volume and the molar surface Gibbs energy of the binary of the ether-functionalized ionic liquids [C22O1IM][TfO] with ethanol and isomeric propanols at T = (288.15-318.15) K
ρ_l	772.32	kg/m³	308.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρ_l	772.25	kg/m³	308.15	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
ρ_l	772.40	kg/m³	308.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρ_l	772.41	kg/m³	308.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρ_l	772.26	kg/m³	308.15	Mass density, sound velocity, mixing enthalpy, 1H NMR, Ab initio calculations and intermolecular interactions in binary mixtures of N-methylimidazole + water, +methanol, +ethanol, +1-propanol, +2-propanol
ρ_l	772.43	kg/m³	308.15	Densities and Viscosities of Binary Mixtures Containing 1,3-Dimethylimidazolium Dimethylphosphate and Alcohols
ρ_l	772.42	kg/m³	308.15	Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
ρ_l	772.62	kg/m³	308.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	772.02	kg/m³	308.15	Investigation on molecular interactions of antibiotics in alcohols using volumetric and acoustic studies at different temperatures
ρ_l	772.40	kg/m³	308.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρ_l	772.45	kg/m³	308.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	772.23	kg/m³	308.15	Thermophysical Characterization of the Mixtures of the Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate with 1-Propanol or 2-Propanol
ρ_l	772.32	kg/m³	308.15	Densities, surface tensions, and isobaric vapor-liquid equilibria for the mixtures of 2-propanol, water, and 1,2-propanediol
ρ_l	772.30	kg/m³	308.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρ_l	772.40	kg/m³	308.15	Thermophysical properties of binary mixtures of 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate ionic liquid with alcohols at several temperatures
ρ_l	772.37	kg/m³	308.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρ_l	772.24	kg/m³	308.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρ_l	772.40	kg/m³	308.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρ_l	772.31	kg/m³	308.15	Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
ρ_l	772.40	kg/m³	308.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρ_l	772.51	kg/m³	308.15	Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρ_l	772.48	kg/m³	308.15	Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρ_l	772.39	kg/m³	308.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρ_l	772.40	kg/m³	308.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρ_l	773.15	kg/m³	308.15	Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
ρ_l	767.96	kg/m³	313.15	Measurement and Correlation of the Excess Properties of Ternary Mixture of {x1[Hmim][BF4] + x21-Propanol + x32-Propanol} at Different Temperatures
ρ_l	767.90	kg/m³	313.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρ_l	768.00	kg/m³	313.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρ_l	767.82	kg/m³	313.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρ_l	767.83	kg/m³	313.15	The excess molar volume and the molar surface Gibbs energy of the binary of the ether-functionalized ionic liquids [C22O1IM][TfO] with ethanol and isomeric propanols at T = (288.15-318.15) K
ρ_l	768.45	kg/m³	313.15	Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
ρ_l	768.00	kg/m³	313.15	Experimental Phase Equilibrium for the Binary System of n-Pentane +2-Propanol Using a New Equilibrium Cell and the Static Total Pressure Method
ρ_l	767.76	kg/m³	313.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρ_l	768.11	kg/m³	313.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρ_l	767.84	kg/m³	313.15	Volumetric Properties of Binary and Ternary Liquid Mixtures of 1-Propanol (1) + 2-Propanol (2) + Water (3) at Different Temperatures and Ambient Pressure (81.5 kPa)
ρ_l	768.00	kg/m³	313.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρ_l	769.70	kg/m³	313.15	Investigation on molecular interactions of antibiotics in alcohols using volumetric and acoustic studies at different temperatures
ρ_l	767.81	kg/m³	313.15	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
ρ_l	768.00	kg/m³	313.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρ_l	768.80	kg/m³	313.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρ_l	768.02	kg/m³	313.15	Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols
ρ_l	767.99	kg/m³	313.15	Densities and Viscosities of Binary Mixtures Containing 1,3-Dimethylimidazolium Dimethylphosphate and Alcohols
ρ_l	768.00	kg/m³	313.15	Total Pressure Phase Equilibrium Measurements for the Binary Systems of n-Pentane + Cyclohexane and 1-Hexene + 2-Propanol
ρ_l	767.99	kg/m³	313.15	Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
ρ_l	768.00	kg/m³	313.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρ_l	768.18	kg/m³	313.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	767.93	kg/m³	313.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρ_l	768.00	kg/m³	313.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρ_l	767.60	kg/m³	313.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρ_l	767.80	kg/m³	313.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρ_l	768.00	kg/m³	313.15	Composition and Temperature Dependence of Density, Surface Tension, and Viscosity of EMIM DEP/MMIM DMP + Water + 1-Propanol/2-Propanol Ternary Mixtures and Their Mathematical Representation Using the Jouyban Acree Model
ρ_l	767.83	kg/m³	313.15	Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
ρ_l	768.02	kg/m³	313.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	768.20	kg/m³	313.15	Liquid Densities and Speed of Sound for Ionic Liquid (2-HEAA and 2-HDEAA) + Alcohol (1-Propanol and 2-Propanol) Mixtures at T = (293.15-323.15 K) and Atmospheric Pressure
ρ_l	768.48	kg/m³	313.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρ_l	768.07	kg/m³	313.15	Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρ_l	768.00	kg/m³	313.15	Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
ρ_l	767.85	kg/m³	313.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρ_l	767.92	kg/m³	313.15	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
ρ_l	763.47	kg/m³	318.15	Densities and Viscosities of Binary Mixtures Containing 1,3-Dimethylimidazolium Dimethylphosphate and Alcohols
ρ_l	763.49	kg/m³	318.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	763.40	kg/m³	318.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρ_l	763.90	kg/m³	318.15	Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρ_l	763.19	kg/m³	318.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρ_l	763.48	kg/m³	318.15	Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols
ρ_l	763.30	kg/m³	318.15	Mass density, sound velocity, mixing enthalpy, 1H NMR, Ab initio calculations and intermolecular interactions in binary mixtures of N-methylimidazole + water, +methanol, +ethanol, +1-propanol, +2-propanol
ρ_l	763.29	kg/m³	318.15	The excess molar volume and the molar surface Gibbs energy of the binary of the ether-functionalized ionic liquids [C22O1IM][TfO] with ethanol and isomeric propanols at T = (288.15-318.15) K
ρ_l	763.40	kg/m³	318.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρ_l	763.40	kg/m³	318.15	Thermophysical properties of binary mixtures of 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate ionic liquid with alcohols at several temperatures
ρ_l	763.40	kg/m³	318.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρ_l	763.41	kg/m³	318.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρ_l	763.61	kg/m³	318.15	Densities, surface tensions, and isobaric vapor-liquid equilibria for the mixtures of 2-propanol, water, and 1,2-propanediol
ρ_l	763.88	kg/m³	318.15	Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρ_l	763.28	kg/m³	318.15	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
ρ_l	763.51	kg/m³	318.15	Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρ_l	763.30	kg/m³	318.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρ_l	763.27	kg/m³	318.15	Thermophysical Characterization of the Mixtures of the Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate with 1-Propanol or 2-Propanol
ρ_l	763.10	kg/m³	318.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρ_l	763.40	kg/m³	318.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρ_l	763.65	kg/m³	318.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	763.40	kg/m³	318.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρ_l	758.71	kg/m³	323.15	Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
ρ_l	758.68	kg/m³	323.15	Volumetric Properties of Binary and Ternary Liquid Mixtures of 1-Propanol (1) + 2-Propanol (2) + Water (3) at Different Temperatures and Ambient Pressure (81.5 kPa)
ρ_l	758.60	kg/m³	323.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρ_l	759.31	kg/m³	323.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρ_l	758.80	kg/m³	323.15	Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρ_l	758.50	kg/m³	323.15	Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρ_l	759.00	kg/m³	323.15	Composition and Temperature Dependence of Density, Surface Tension, and Viscosity of EMIM DEP/MMIM DMP + Water + 1-Propanol/2-Propanol Ternary Mixtures and Their Mathematical Representation Using the Jouyban Acree Model
ρ_l	758.80	kg/m³	323.15	Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρ_l	758.80	kg/m³	323.15	Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρ_l	759.01	kg/m³	323.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	759.00	kg/m³	323.15	Liquid Densities and Speed of Sound for Ionic Liquid (2-HEAA and 2-HDEAA) + Alcohol (1-Propanol and 2-Propanol) Mixtures at T = (293.15-323.15 K) and Atmospheric Pressure
ρ_l	758.85	kg/m³	323.15	Densities and Viscosities of Binary Mixtures Containing 1,3-Dimethylimidazolium Dimethylphosphate and Alcohols
ρ_l	758.84	kg/m³	323.15	Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
ρ_l	759.00	kg/m³	323.15	Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
ρ_l	758.55	kg/m³	323.15	Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρ_l	758.68	kg/m³	323.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρ_l	758.79	kg/m³	323.15	Measurement and Correlation of the Excess Properties of Ternary Mixture of {x1[Hmim][BF4] + x21-Propanol + x32-Propanol} at Different Temperatures
ρ_l	758.80	kg/m³	323.15	Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρ_l	758.63	kg/m³	323.15	Osmotic coefficients and apparent molar volumes of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid in alcohols
ρ_l	758.64	kg/m³	323.15	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
ρ_l	758.70	kg/m³	323.15	Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
ρ_l	758.80	kg/m³	323.15	Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρ_l	759.70	kg/m³	323.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρ_l	758.89	kg/m³	323.15	Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρ_l	760.10	kg/m³	323.40	Effect of Al2O3 Nanoparticles Additives on the Density, Saturated Vapor Pressure, Surface Tension and Viscosity of Isopropyl Alcohol
ρ_l	753.89	kg/m³	328.15	Thermophysical Characterization of the Mixtures of the Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate with 1-Propanol or 2-Propanol
ρ_l	754.00	kg/m³	328.15	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
ρ_l	754.26	kg/m³	328.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	753.80	kg/m³	328.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρ_l	754.19	kg/m³	328.15	Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρ_l	753.91	kg/m³	328.15	Mass density, sound velocity, mixing enthalpy, 1H NMR, Ab initio calculations and intermolecular interactions in binary mixtures of N-methylimidazole + water, +methanol, +ethanol, +1-propanol, +2-propanol
ρ_l	753.88	kg/m³	328.15	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
ρ_l	753.12	kg/m³	328.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρ_l	754.84	kg/m³	328.15	Densities, surface tensions, and isobaric vapor-liquid equilibria for the mixtures of 2-propanol, water, and 1,2-propanediol
ρ_l	754.10	kg/m³	328.15	Thermophysical properties of binary mixtures of 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate ionic liquid with alcohols at several temperatures
ρ_l	749.39	kg/m³	333.15	Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
ρ_l	748.90	kg/m³	333.15	Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
ρ_l	749.68	kg/m³	333.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρ_l	750.00	kg/m³	333.15	Composition and Temperature Dependence of Density, Surface Tension, and Viscosity of EMIM DEP/MMIM DMP + Water + 1-Propanol/2-Propanol Ternary Mixtures and Their Mathematical Representation Using the Jouyban Acree Model
ρ_l	750.00	kg/m³	333.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρ_l	749.25	kg/m³	333.15	Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρ_l	749.06	kg/m³	333.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρ_l	749.01	kg/m³	333.15	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
ρ_l	749.16	kg/m³	333.15	Measurement and Correlation of the Excess Properties of Ternary Mixture of {x1[Hmim][BF4] + x21-Propanol + x32-Propanol} at Different Temperatures
ρ_l	744.02	kg/m³	338.15	Thermophysical Characterization of the Mixtures of the Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate with 1-Propanol or 2-Propanol
ρ_l	743.66	kg/m³	338.15	Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρ_l	739.50	kg/m³	343.15	Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρ_l	738.91	kg/m³	343.15	Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) K
ρ_l	739.53	kg/m³	343.15	Densities and Excess Properties of Primary Amines in Alcoholic Solutions
ρ_l	741.00	kg/m³	343.30	Effect of Al2O3 Nanoparticles Additives on the Density, Saturated Vapor Pressure, Surface Tension and Viscosity of Isopropyl Alcohol
Δ_fusS	[28.70; 29.21]	J/mol×K	[184.60; 185.20]
Δ_fusS	28.72	J/mol×K	184.60	NIST
Δ_fusS	28.70	J/mol×K	184.60	NIST
Δ_fusS	29.09	J/mol×K	184.67	NIST
Δ_fusS	29.21	J/mol×K	185.20	NIST
c_sound,fluid	[1032.57; 1208.50]	m/s	[278.15; 328.15]

c_sound,fluid	1208.50	m/s	278.15	Ultrasonic and Volumetric Properties of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with 2-Propanol or Tetrahydrofuran at Several Temperatures
c_sound,fluid	1191.88	m/s	283.15	Thermophysical study of the binary mixtures of N,N-dimethylacetamide with 2-propanol and 2-butanol
c_sound,fluid	1173.07	m/s	288.15	Ultrasonic and Volumetric Properties of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with 2-Propanol or Tetrahydrofuran at Several Temperatures
c_sound,fluid	1157.30	m/s	293.15	Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
c_sound,fluid	1139.17	m/s	298.15	Thermophysical study of the binary mixtures of N,N-dimethylacetamide with 2-propanol and 2-butanol
c_sound,fluid	1138.16	m/s	298.15	Ultrasonic and Volumetric Properties of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with 2-Propanol or Tetrahydrofuran at Several Temperatures
c_sound,fluid	1104.80	m/s	308.15	Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
c_sound,fluid	1103.25	m/s	308.15	Ultrasonic and Volumetric Properties of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with 2-Propanol or Tetrahydrofuran at Several Temperatures
c_sound,fluid	1086.62	m/s	313.15	Thermophysical study of the binary mixtures of N,N-dimethylacetamide with 2-propanol and 2-butanol
c_sound,fluid	1068.09	m/s	318.15	Ultrasonic and Volumetric Properties of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with 2-Propanol or Tetrahydrofuran at Several Temperatures
c_sound,fluid	1051.60	m/s	323.15	Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
c_sound,fluid	1032.57	m/s	328.15	Ultrasonic and Volumetric Properties of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with 2-Propanol or Tetrahydrofuran at Several Temperatures
γ	[0.02; 0.02]	N/m	[288.15; 333.20]

γ	0.02	N/m	288.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
γ	0.02	N/m	288.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ	0.02	N/m	288.15	The molar surface Gibbs energy and its application to the binary mixtures of N-butylpyridinium dicyanamide [C4py][DCA] with alcohols
γ	0.02	N/m	293.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	293.15	The molar surface Gibbs energy and its application to the binary mixtures of N-butylpyridinium dicyanamide [C4py][DCA] with alcohols
γ	0.02	N/m	293.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
γ	0.02	N/m	298.15	Effect of temperature and composition on the surface tension and surface properties of binary mixtures containing DMSO and short chain alcohols
γ	0.02	N/m	298.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ	0.02	N/m	298.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary Mixtures of 2-Propanol + Benzyl Alcohol, + 2-Phenylethanol and Benzyl Alcohol + 2-Phenylethanol at T ) (298.15, 308.15, and 318.15) K
γ	0.02	N/m	298.15	Experimental Data and Correlation of Surface Tensions of the Binary and Ternary Systems of Water + Acetonitrile + 2-Propanol at 298.15 K and Atmospheric Pressure
γ	0.02	N/m	298.15	The molar surface Gibbs energy and its application to the binary mixtures of N-butylpyridinium dicyanamide [C4py][DCA] with alcohols
γ	0.02	N/m	298.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	303.15	The molar surface Gibbs energy and its application to the binary mixtures of N-butylpyridinium dicyanamide [C4py][DCA] with alcohols
γ	0.02	N/m	303.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	303.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
γ	0.02	N/m	308.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary Mixtures of 2-Propanol + Benzyl Alcohol, + 2-Phenylethanol and Benzyl Alcohol + 2-Phenylethanol at T ) (298.15, 308.15, and 318.15) K
γ	0.02	N/m	308.15	Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ	0.02	N/m	308.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	308.15	Effect of temperature and composition on the surface tension and surface properties of binary mixtures containing DMSO and short chain alcohols
γ	0.02	N/m	308.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
γ	0.02	N/m	308.15	The molar surface Gibbs energy and its application to the binary mixtures of N-butylpyridinium dicyanamide [C4py][DCA] with alcohols
γ	0.02	N/m	313.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	313.15	The molar surface Gibbs energy and its application to the binary mixtures of N-butylpyridinium dicyanamide [C4py][DCA] with alcohols
γ	0.02	N/m	313.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
γ	0.02	N/m	318.15	Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary Mixtures of 2-Propanol + Benzyl Alcohol, + 2-Phenylethanol and Benzyl Alcohol + 2-Phenylethanol at T ) (298.15, 308.15, and 318.15) K
γ	0.02	N/m	318.15	The molar surface Gibbs energy and its application to the binary mixtures of N-butylpyridinium dicyanamide [C4py][DCA] with alcohols
γ	0.02	N/m	318.15	Effect of temperature and composition on the surface tension and surface properties of binary mixtures containing DMSO and short chain alcohols
γ	0.02	N/m	318.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	323.15	Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ	0.02	N/m	323.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
γ	0.02	N/m	328.15	Effect of temperature and composition on the surface tension and surface properties of binary mixtures containing DMSO and short chain alcohols
γ	0.02	N/m	333.20	Surface tension and interfacial compositions of binary glycerol/alcohol mixtures

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
T_boil	355.01	K	100.00	Isobaric Vapor-Liquid Equilibria for Water + 2-Propanol + 1-Butyl-3-methylimidazolium Tetrafluoroborate

Datasets

Molar heat capacity at constant pressure, J/K/mol (1)
Viscosity, Pa*s (1)
Refractive index (Na D-line) (2)
Mass density, kg/m3 (8)
Speed of sound, m/s (2)
Molar volume, m3/mol (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
253.15	100.00	129.40
253.15	20000.00	126.10
253.15	40000.00	125.80
258.15	100.00	130.60
258.15	20000.00	128.30
258.15	40000.00	127.30
263.15	100.00	132.60
263.15	20000.00	130.70
263.15	40000.00	129.20
268.15	100.00	135.00
268.15	20000.00	133.40
268.15	40000.00	131.50
273.15	100.00	138.00
273.15	20000.00	136.30
273.15	40000.00	134.00
278.15	100.00	141.40
278.15	20000.00	139.40
278.15	40000.00	136.80
283.15	100.00	145.10
283.15	20000.00	142.60
283.15	40000.00	140.00
288.15	100.00	148.90
288.15	20000.00	146.00
288.15	40000.00	143.30
293.15	100.00	152.90
293.15	20000.00	149.60
293.15	40000.00	146.90
298.15	100.00	157.00
298.15	20000.00	153.30
298.15	40000.00	150.70
303.15	100.00	161.10
303.15	20000.00	157.10
303.15	40000.00	154.70
308.15	100.00	165.00
308.15	20000.00	161.10
308.15	40000.00	159.00
313.15	100.00	168.60
313.15	20000.00	165.00
313.15	40000.00	163.30
318.15	100.00	171.90
318.15	20000.00	169.10
318.15	40000.00	167.80
323.15	100.00	174.90
323.15	20000.00	173.20
323.15	40000.00	172.40
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	81.50	0.0021
Reference

Refractive index (Na D-line)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	101.33	1.3752
293.15	101.00	1.3772
303.15	101.00	1.3729
313.15	101.00	1.3685
323.15	101.00	1.3636
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	100.00	1.375
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	313.15	767.67
5000.00	313.15	772.3
10000.00	313.15	776.83
15000.00	313.15	781.04
20000.00	313.15	785.09
25000.00	313.15	788.94
30000.00	313.15	792.51
35000.00	313.15	796.05
40000.00	313.15	799.39
50000.00	313.15	805.89
60000.00	313.15	811.8
70000.00	313.15	817.44
80000.00	313.15	822.71
90000.00	313.15	827.67
100000.00	313.15	832.64
110000.00	313.15	837.15
120000.00	313.15	841.57
130000.00	313.15	845.79
140000.00	313.15	849.83
100.00	323.15	758.87
5000.00	323.15	763.96
10000.00	323.15	768.84
15000.00	323.15	773.34
20000.00	323.15	777.63
25000.00	323.15	781.69
30000.00	323.15	785.6
35000.00	323.15	789.17
40000.00	323.15	792.74
50000.00	323.15	799.4
60000.00	323.15	805.57
70000.00	323.15	811.34
80000.00	323.15	816.78
90000.00	323.15	822.03
100000.00	323.15	826.88
110000.00	323.15	831.63
120000.00	323.15	836.11
130000.00	323.15	840.39
140000.00	323.15	844.6
100.00	333.15	749.24
5000.00	333.15	754.45
10000.00	333.15	759.66
15000.00	333.15	764.42
20000.00	333.15	768.95
25000.00	333.15	773.18
30000.00	333.15	777.21
35000.00	333.15	781.18
40000.00	333.15	784.88
50000.00	333.15	791.92
60000.00	333.15	798.25
70000.00	333.15	804.32
80000.00	333.15	810.15
90000.00	333.15	815.49
100000.00	333.15	820.8
110000.00	333.15	825.59
120000.00	333.15	830.23
130000.00	333.15	834.5
140000.00	333.15	838.74
100.00	343.15	738.88
5000.00	343.15	744.75
10000.00	343.15	750.17
15000.00	343.15	755.4
20000.00	343.15	760.17
25000.00	343.15	764.81
30000.00	343.15	769.03
35000.00	343.15	773.28
40000.00	343.15	777.23
50000.00	343.15	784.53
60000.00	343.15	791.22
70000.00	343.15	797.48
80000.00	343.15	803.44
90000.00	343.15	808.87
100000.00	343.15	814.1
110000.00	343.15	819.16
120000.00	343.15	823.87
130000.00	343.15	828.44
140000.00	343.15	832.84
100.00	353.15	728.44
5000.00	353.15	734.66
10000.00	353.15	740.52
15000.00	353.15	745.99
20000.00	353.15	751.21
25000.00	353.15	756.02
30000.00	353.15	760.43
35000.00	353.15	764.79
40000.00	353.15	768.87
50000.00	353.15	777.01
60000.00	353.15	783.94
70000.00	353.15	790.65
80000.00	353.15	796.56
90000.00	353.15	802.3
100000.00	353.15	807.6
110000.00	353.15	812.87
120000.00	353.15	817.76
130000.00	353.15	822.37
140000.00	353.15	826.85
5000.00	363.15	723.93
10000.00	363.15	730.44
15000.00	363.15	736.42
20000.00	363.15	741.95
25000.00	363.15	747.05
30000.00	363.15	751.95
35000.00	363.15	756.37
40000.00	363.15	760.76
50000.00	363.15	769.06
60000.00	363.15	776.43
70000.00	363.15	783.33
80000.00	363.15	789.52
90000.00	363.15	795.58
100000.00	363.15	801.38
110000.00	363.15	806.5
120000.00	363.15	811.57
130000.00	363.15	816.39
140000.00	363.15	820.9
5000.00	373.15	712.57
10000.00	373.15	719.75
15000.00	373.15	726.13
20000.00	373.15	732.08
25000.00	373.15	737.65
30000.00	373.15	742.73
35000.00	373.15	747.59
40000.00	373.15	752.29
50000.00	373.15	760.75
60000.00	373.15	768.5
70000.00	373.15	775.82
80000.00	373.15	782.24
90000.00	373.15	788.49
100000.00	373.15	794.34
110000.00	373.15	799.85
120000.00	373.15	805.17
130000.00	373.15	810.06
140000.00	373.15	814.94
5000.00	383.15	700.32
10000.00	383.15	708.06
15000.00	383.15	715.03
20000.00	383.15	721.43
25000.00	383.15	727.35
30000.00	383.15	732.77
35000.00	383.15	737.95
40000.00	383.15	742.76
50000.00	383.15	751.85
60000.00	383.15	760.06
70000.00	383.15	767.53
80000.00	383.15	774.49
90000.00	383.15	780.94
100000.00	383.15	786.9
110000.00	383.15	792.77
120000.00	383.15	798.27
130000.00	383.15	803.3
140000.00	383.15	808.26
5000.00	393.15	687.82
10000.00	393.15	696.15
15000.00	393.15	703.77
20000.00	393.15	710.73
25000.00	393.15	717.07
30000.00	393.15	722.91
35000.00	393.15	728.4
40000.00	393.15	733.66
50000.00	393.15	743.39
60000.00	393.15	751.87
70000.00	393.15	759.71
80000.00	393.15	766.86
90000.00	393.15	773.67
100000.00	393.15	779.96
110000.00	393.15	785.9
120000.00	393.15	791.54
130000.00	393.15	796.8
140000.00	393.15	801.97
5000.00	403.15	674.03
10000.00	403.15	683.54
15000.00	403.15	691.9
20000.00	403.15	699.4
25000.00	403.15	706.26
30000.00	403.15	712.66
35000.00	403.15	718.38
40000.00	403.15	724.01
50000.00	403.15	734.72
60000.00	403.15	743.58
70000.00	403.15	751.89
80000.00	403.15	759.17
90000.00	403.15	766.2
100000.00	403.15	772.7
110000.00	403.15	778.85
120000.00	403.15	784.7
130000.00	403.15	790.2
140000.00	403.15	795.51
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
117.90	280.21	797.61
186.70	300.09	780.22
202.70	325.12	757.05
220.40	350.14	731.92
349.50	375.01	702.23
407.60	392.57	679.26
439.60	280.21	797.89
609.40	325.12	757.49
610.50	300.09	780.62
663.40	350.14	732.49
703.30	375.01	702.82
888.70	392.57	680.18
938.70	280.21	798.29
953.40	300.09	780.94
960.00	325.12	757.87
1046.80	375.01	703.38
1071.20	350.14	733.03
1171.40	392.57	680.72
1253.90	325.12	758.21
1328.40	280.21	798.62
1339.50	300.09	781.31
1412.60	350.14	733.49
1437.50	375.01	704.01
1526.60	392.57	681.39
1638.80	325.12	758.63
1656.60	280.21	798.89
1722.10	300.09	781.66
1791.60	375.01	704.58
1844.70	350.14	734.07
1897.40	392.57	682.08
1944.90	280.21	799.14
2021.00	325.12	759.06
2044.80	300.09	781.96
2161.70	375.01	705.16
2226.70	350.14	734.58
2272.30	392.57	682.77
2328.80	325.12	759.39
2440.60	280.21	799.56
2446.40	300.09	782.34
2545.70	375.01	705.76
2619.10	392.57	683.41
2644.70	350.14	735.11
2655.80	325.15	759.75
2834.60	300.09	782.7
2842.70	350.14	735.41
2850.60	280.21	799.88
2909.90	375.01	706.34
3014.90	325.12	760.15
3050.40	392.57	684.2
3198.00	280.21	800.17
3224.90	300.09	783.06
3286.90	350.14	735.99
3321.40	325.12	760.48
3364.10	375.01	707.04
3411.20	392.57	684.86
3630.70	350.14	736.45
3659.40	325.12	760.85
3671.10	300.09	783.47
3677.60	375.01	707.53
3679.10	280.21	800.56
3835.00	392.57	685.63
4004.10	325.12	761.22
4012.20	350.14	736.94
4071.10	280.21	800.9
4074.10	300.09	783.84
4083.20	375.01	708.16
4095.70	392.57	686.12
4362.50	300.09	784.11
4394.60	350.14	737.43
4399.20	325.12	761.65
4437.70	280.21	801.19
4515.70	375.01	708.82
4524.90	392.57	686.89
4691.20	325.12	761.97
4757.60	350.14	737.91
4771.80	300.09	784.48
4832.60	280.21	801.5
4853.50	375.01	709.33
4902.80	392.57	687.57
5010.70	325.12	762.32
5182.10	280.21	801.8
5197.90	350.14	738.48
5226.50	300.09	784.89
5280.20	375.01	709.98
5283.50	392.57	688.24
5383.40	325.12	762.71
5559.10	280.21	802.1
5577.90	350.14	738.96
5579.20	300.09	785.21
5646.90	375.01	710.53
5730.50	325.12	763.08
5775.90	392.57	689.09
5910.00	280.21	802.39
5939.30	350.14	739.42
6001.60	300.09	785.59
6039.60	392.57	689.55
6138.10	375.01	711.26
6143.60	325.12	763.52
6321.30	350.14	739.89
6334.90	280.21	802.73
6427.20	300.09	785.98
6447.10	375.01	711.73
6476.60	392.57	690.3
6525.60	325.12	763.91
6730.90	350.14	740.41
6750.90	280.21	803.06
6780.30	300.09	786.29
6880.90	375.01	712.37
6889.70	392.57	691.01
6903.20	325.12	764.31
7119.70	350.14	740.89
7166.50	281.21	803.39
7214.70	300.09	786.68
7269.80	375.01	712.94
7293.80	325.12	764.72
7348.00	392.57	691.78
7564.40	350.14	741.45
7592.00	280.21	803.74
7629.90	300.09	787.05
7661.90	325.12	765.11
7728.00	392.57	692.42
7772.40	375.01	713.68
7918.60	325.12	765.38
7988.50	350.14	741.97
7999.00	280.21	804.07
8020.30	300.09	787.4
8119.20	375.01	714.18
8172.70	392.57	693.17
8254.40	325.12	765.72
8329.00	280.21	804.33
8417.50	300.09	787.75
8472.50	350.14	742.55
8557.20	375.01	714.81
8598.30	392.57	693.88
8755.50	325.12	766.24
8805.70	300.09	788.1
8817.00	280.21	804.7
8925.80	350.14	743.13
8987.30	375.01	715.42
9018.50	392.57	694.57
9212.90	300.09	788.45
9280.80	350.14	743.56
9350.60	280.21	805.11
9405.00	392.57	695.2
9423.80	375.01	716.04
9621.50	300.09	788.81
9658.50	280.21	805.38
9676.30	350.14	744.05
9837.90	392.57	695.89
9842.20	375.01	716.64
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	785.0
293.15	10000.00	793.2
293.15	20000.00	800.6
293.15	30000.00	807.4
293.15	40000.00	813.7
293.15	50000.00	819.6
293.15	60000.00	825.1
293.15	70000.00	830.4
293.15	80000.00	835.3
293.15	90000.00	840.1
293.15	100000.00	844.6
293.15	110000.00	848.9
293.15	120000.00	853.1
293.15	130000.00	857.1
293.15	140000.00	861.0
303.15	100.00	776.6
303.15	10000.00	785.3
303.15	20000.00	793.3
303.15	30000.00	800.2
303.15	40000.00	806.9
303.15	50000.00	813.1
303.15	60000.00	818.9
303.15	70000.00	824.3
303.15	80000.00	829.1
303.15	90000.00	834.2
303.15	100000.00	838.8
303.15	110000.00	843.1
303.15	120000.00	847.3
303.15	130000.00	851.4
303.15	140000.00	855.2
313.15	100.00	767.8
313.15	10000.00	777.1
313.15	20000.00	785.4
313.15	30000.00	792.9
313.15	40000.00	799.8
313.15	50000.00	806.2
313.15	60000.00	812.1
313.15	70000.00	817.6
313.15	80000.00	822.8
313.15	90000.00	827.8
313.15	100000.00	832.6
313.15	110000.00	837.3
313.15	120000.00	841.5
313.15	130000.00	845.8
313.15	140000.00	849.7
323.15	100.00	758.7
323.15	10000.00	768.6
323.15	20000.00	777.3
323.15	30000.00	785.2
323.15	40000.00	792.4
323.15	50000.00	799.0
323.15	60000.00	805.2
323.15	70000.00	811.0
323.15	80000.00	816.4
323.15	90000.00	821.6
323.15	100000.00	826.6
323.15	110000.00	831.3
323.15	120000.00	835.7
323.15	130000.00	840.0
323.15	140000.00	844.2
333.15	100.00	749.2
333.15	10000.00	759.7
333.15	20000.00	769.1
333.15	30000.00	777.4
333.15	40000.00	785.0
333.15	50000.00	792.0
333.15	60000.00	798.5
333.15	70000.00	804.5
333.15	80000.00	810.1
333.15	90000.00	815.6
333.15	100000.00	820.6
333.15	110000.00	825.4
333.15	120000.00	830.0
333.15	130000.00	834.4
333.15	140000.00	838.5
343.15	100.00	738.8
343.15	10000.00	750.2
343.15	20000.00	760.1
343.15	30000.00	768.8
343.15	40000.00	776.8
343.15	50000.00	784.1
343.15	60000.00	790.9
343.15	70000.00	797.1
343.15	80000.00	803.0
343.15	90000.00	808.6
343.15	100000.00	813.9
343.15	110000.00	818.9
343.15	120000.00	823.8
343.15	130000.00	828.3
343.15	140000.00	832.7
353.15	100.00	728.3
353.15	10000.00	740.5
353.15	20000.00	751.1
353.15	30000.00	760.6
353.15	40000.00	768.9
353.15	50000.00	776.6
353.15	60000.00	783.7
353.15	70000.00	790.3
353.15	80000.00	796.4
353.15	90000.00	802.1
353.15	100000.00	807.5
353.15	110000.00	812.6
353.15	120000.00	817.5
353.15	130000.00	822.3
353.15	140000.00	826.7
363.15	10000.00	730.2
363.15	20000.00	741.7
363.15	30000.00	751.7
363.15	40000.00	760.6
363.15	50000.00	768.7
363.15	60000.00	776.0
363.15	70000.00	782.8
363.15	80000.00	789.2
363.15	90000.00	795.2
363.15	100000.00	800.8
363.15	110000.00	806.2
363.15	120000.00	811.3
363.15	130000.00	816.2
363.15	140000.00	820.8
373.15	10000.00	719.5
373.15	20000.00	731.9
373.15	30000.00	742.6
373.15	40000.00	752.1
373.15	50000.00	760.5
373.15	60000.00	768.2
373.15	70000.00	775.4
373.15	80000.00	782.1
373.15	90000.00	788.4
373.15	100000.00	794.2
373.15	110000.00	799.8
373.15	120000.00	805.0
373.15	130000.00	810.0
373.15	140000.00	814.7
383.15	10000.00	708.0
383.15	20000.00	721.5
383.15	30000.00	732.9
383.15	40000.00	743.1
383.15	50000.00	752.0
383.15	60000.00	760.1
383.15	70000.00	767.6
383.15	80000.00	774.6
383.15	90000.00	781.0
383.15	100000.00	787.1
383.15	110000.00	792.8
383.15	120000.00	798.3
383.15	130000.00	803.5
383.15	140000.00	808.5
393.15	10000.00	696.3
393.15	20000.00	710.9
393.15	30000.00	723.2
393.15	40000.00	733.7
393.15	50000.00	743.1
393.15	60000.00	751.7
393.15	70000.00	759.6
393.15	80000.00	766.6
393.15	90000.00	773.6
393.15	100000.00	779.9
393.15	110000.00	785.9
393.15	120000.00	791.5
393.15	130000.00	796.8
393.15	140000.00	801.6
403.15	10000.00	683.7
403.15	20000.00	699.5
403.15	30000.00	712.8
403.15	40000.00	724.1
403.15	50000.00	734.2
403.15	60000.00	743.2
403.15	70000.00	751.4
403.15	80000.00	758.9
403.15	90000.00	766.0
403.15	100000.00	772.5
403.15	110000.00	778.7
403.15	120000.00	784.5
403.15	130000.00	790.1
403.15	140000.00	795.4
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
302.90	1040.00	778.1
302.90	2000.00	778.9
302.90	2990.00	779.8
302.90	4060.00	780.8
302.90	5010.00	781.6
302.90	6000.00	782.5
302.90	7020.00	783.4
302.90	8020.00	784.3
302.90	9000.00	785.1
302.90	10000.00	786.0
323.00	1000.00	760.6
323.00	2020.00	761.6
323.00	3000.00	762.7
323.00	4070.00	763.7
323.00	5000.00	764.7
323.00	6010.00	765.7
323.00	7020.00	766.7
323.00	8010.00	767.7
323.00	9010.00	768.6
323.00	10020.00	769.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	785.4
293.15	1000.00	786.2
293.15	5000.00	789.6
293.15	10000.00	793.6
293.15	15000.00	797.4
293.15	20000.00	801.1
293.15	25000.00	804.5
293.15	30000.00	807.9
293.15	35000.00	811.2
293.15	40000.00	814.2
293.15	45000.00	817.2
293.15	50000.00	820.1
293.15	55000.00	822.9
293.15	60000.00	825.6
293.15	65000.00	828.2
293.15	70000.00	830.8
293.15	80000.00	835.8
293.15	90000.00	840.5
293.15	100000.00	845.0
293.15	110000.00	849.4
293.15	120000.00	853.5
293.15	130000.00	857.6
293.15	140000.00	861.2
298.15	100.00	781.4
298.15	1000.00	782.1
298.15	5000.00	785.6
298.15	10000.00	789.8
298.15	15000.00	793.7
298.15	20000.00	797.3
298.15	25000.00	800.9
298.15	30000.00	804.3
298.15	35000.00	807.7
298.15	40000.00	810.8
298.15	45000.00	813.8
298.15	50000.00	816.7
298.15	55000.00	819.7
298.15	60000.00	822.5
298.15	65000.00	825.2
298.15	70000.00	827.6
298.15	80000.00	832.8
298.15	90000.00	837.5
298.15	100000.00	842.3
298.15	110000.00	846.4
298.15	120000.00	850.8
298.15	130000.00	854.8
298.15	140000.00	858.7
313.15	100.00	768.2
313.15	1000.00	769.1
313.15	5000.00	773.0
313.15	10000.00	777.4
313.15	15000.00	781.8
313.15	20000.00	785.7
313.15	25000.00	789.5
313.15	30000.00	793.3
313.15	35000.00	796.9
313.15	40000.00	800.1
313.15	45000.00	803.4
313.15	50000.00	806.5
313.15	55000.00	809.6
313.15	60000.00	812.5
313.15	65000.00	815.4
313.15	70000.00	818.2
313.15	80000.00	823.4
313.15	90000.00	828.5
313.15	100000.00	833.1
313.15	110000.00	837.8
313.15	120000.00	842.1
313.15	130000.00	846.4
313.15	140000.00	850.4
333.15	100.00	749.4
333.15	1000.00	750.5
333.15	5000.00	754.9
333.15	10000.00	760.0
333.15	15000.00	764.9
333.15	20000.00	769.3
333.15	25000.00	773.6
333.15	30000.00	777.7
333.15	35000.00	781.5
333.15	40000.00	785.3
333.15	45000.00	788.9
333.15	50000.00	792.3
333.15	55000.00	795.6
333.15	60000.00	798.7
333.15	65000.00	801.8
333.15	70000.00	804.8
333.15	80000.00	810.5
333.15	90000.00	815.9
333.15	100000.00	820.9
333.15	110000.00	825.8
333.15	120000.00	830.4
333.15	130000.00	834.8
333.15	140000.00	839.2
353.15	1000.00	729.8
353.15	5000.00	735.0
353.15	10000.00	741.0
353.15	15000.00	746.5
353.15	20000.00	751.7
353.15	25000.00	756.5
353.15	30000.00	761.0
353.15	35000.00	765.4
353.15	40000.00	769.3
353.15	45000.00	773.3
353.15	50000.00	777.0
353.15	55000.00	780.6
353.15	60000.00	784.0
353.15	65000.00	787.4
353.15	70000.00	790.6
353.15	80000.00	796.7
353.15	90000.00	802.6
353.15	100000.00	808.0
353.15	110000.00	813.2
353.15	120000.00	818.1
353.15	130000.00	822.8
353.15	140000.00	827.3
373.15	1000.00	706.6
373.15	5000.00	712.8
373.15	10000.00	719.9
373.15	15000.00	726.3
373.15	20000.00	732.0
373.15	25000.00	737.7
373.15	30000.00	742.9
373.15	35000.00	747.8
373.15	40000.00	752.2
373.15	45000.00	756.6
373.15	50000.00	760.7
373.15	55000.00	764.7
373.15	60000.00	768.6
373.15	65000.00	772.1
373.15	70000.00	775.6
373.15	80000.00	782.3
373.15	90000.00	788.5
373.15	100000.00	794.4
373.15	110000.00	799.9
373.15	120000.00	805.3
373.15	130000.00	810.2
373.15	140000.00	815.1
393.15	1000.00	680.4
393.15	5000.00	688.2
393.15	10000.00	696.7
393.15	15000.00	704.4
393.15	20000.00	711.4
393.15	25000.00	717.6
393.15	30000.00	723.5
393.15	35000.00	729.0
393.15	40000.00	734.2
393.15	45000.00	739.0
393.15	50000.00	743.5
393.15	55000.00	747.9
393.15	60000.00	752.1
393.15	65000.00	756.1
393.15	70000.00	760.0
393.15	80000.00	767.2
393.15	90000.00	773.9
393.15	100000.00	780.2
393.15	110000.00	786.2
393.15	120000.00	791.8
393.15	130000.00	797.2
393.15	140000.00	802.3
303.15	100.00	777.0
293.15	100.00	785.46
313.15	100.00	768.21
323.15	100.00	759.07
298.15	100.00	781.27
333.15	100.00	749.42
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	81.50	780.99
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	781.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	793.7
283.15	5000.00	797.5
283.15	10000.00	801.3
283.15	20000.00	808.9
283.18	15000.00	805.2
298.15	100.00	781.2
298.15	5000.00	785.5
298.15	10000.00	789.7
298.15	15000.00	793.8
298.15	20000.00	797.6
313.15	100.00	768.1
313.15	5000.00	773.0
313.15	10000.00	777.5
313.15	15000.00	781.9
313.15	20000.00	786.1
328.15	100.00	754.4
328.15	5000.00	759.6
328.15	15000.00	769.5
328.15	20000.00	774.0
328.18	10000.00	764.8
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
253.15	99.00	1300.967
253.15	5138.00	1328.819
253.15	10106.00	1354.875
253.15	15136.00	1380.021
253.15	20143.00	1404.015
253.15	25229.00	1427.462
253.15	30036.00	1448.868
273.15	100.00	1227.88
273.15	5275.00	1258.803
273.15	10173.00	1286.447
273.15	15164.00	1313.265
273.15	20289.00	1339.577
273.15	25102.00	1363.26
273.15	30264.00	1387.65
293.15	100.00	1157.361
293.15	5085.00	1189.739
293.15	10183.00	1220.822
293.15	15273.00	1250.197
293.15	20239.00	1277.428
293.15	25220.00	1303.56
293.15	30278.00	1328.856
313.15	100.00	1087.156
313.15	5177.00	1123.06
313.15	10104.00	1155.744
313.15	15187.00	1187.465
313.15	20126.00	1216.587
313.15	25138.00	1244.664
313.15	30110.00	1271.13
333.15	100.00	1015.957
333.15	5048.00	1054.493
333.15	10038.00	1090.587
333.15	15065.00	1124.563
333.15	20102.00	1156.534
333.15	25093.00	1186.433
333.15	30014.00	1214.42
353.15	100.00	940.503
353.15	5080.00	983.885
353.15	10091.00	1023.857
353.15	15114.00	1060.82
353.15	20132.00	1095.253
353.15	25164.00	1127.605
353.15	30380.00	1159.239
Reference

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
299.79	86.00	1132.8
349.93	138.00	950.4
217.77	143.00	1445.1
249.84	159.00	1317.8
399.64	492.00	745.0
299.80	865.00	1138.2
249.86	992.00	1322.3
217.84	1031.00	1449.0
399.63	1090.00	752.7
349.94	1099.00	958.9
450.06	1639.00	499.2
349.97	1915.00	966.0
399.63	1986.00	764.1
249.87	2039.00	1328.0
299.81	2097.00	1146.6
450.04	2190.00	512.0
217.84	2256.00	1454.8
249.85	4937.00	1343.6
349.97	5044.00	992.5
299.81	5133.00	1166.5
399.62	5275.00	802.7
217.88	6084.00	1472.2
500.17	7568.00	371.1
217.00	8951.00	1489.1
249.85	9128.00	1365.3
500.15	9582.00	424.0
299.79	9677.00	1195.1
349.97	9682.00	1029.2
399.62	9782.00	850.0
249.86	10803.00	1373.6
249.85	19905.00	1417.6
299.80	20194.00	1256.1
399.61	20985.00	948.9
349.98	21490.00	1111.7
450.02	22115.00	792.1
500.11	22653.00	636.6
216.95	24689.00	1556.1
399.63	38384.00	1071.2
299.80	39488.00	1353.7
500.25	40483.00	812.4
216.87	41140.00	1619.7
249.85	41768.00	1512.2
349.98	42396.00	1232.7
449.97	42419.00	957.3
249.85	59235.00	1579.4
216.89	60566.00	1688.1
299.81	60935.00	1447.1
349.97	61179.00	1324.0
449.98	61580.00	1076.2
500.27	61769.00	961.8
399.63	61965.00	1203.3
216.90	78557.00	1746.2
249.85	80375.00	1653.1
500.27	80461.00	1067.0
399.61	80647.00	1291.3
349.97	81377.00	1409.9
299.89	81993.00	1527.9
449.99	82381.00	1183.6
249.85	96644.00	1705.5
349.97	96752.00	1469.0
299.88	97237.00	1581.4
399.60	97607.00	1362.4
450.00	97646.00	1252.6
500.27	98305.00	1153.8
216.97	98400.00	1805.5
216.96	121241.00	1868.7
399.66	122092.00	1454.2
450.00	122429.00	1352.4
299.85	123509.00	1665.9
349.94	123510.00	1562.0
500.28	123715.00	1261.3
249.85	124462.00	1787.6
Reference

Molar volume, m3/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar volume, m3/mol - Liquid
298.15	100.00	0.0001
298.15	10000.00	0.0001
313.15	100.00	0.0001
313.15	10000.00	0.0001
328.15	100.00	0.0001
328.15	10000.00	0.0001
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 4733.35]	kPa	[272.89; 508.31]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.60031e+01
Coefficient B			-3.41274e+03
Coefficient C			-5.57370e+01
Temperature range, min.			272.89
Temperature range, max.			508.31

P_vap	1.33	kPa	272.89	Calculated Property
P_vap	7.22	kPa	299.05	Calculated Property
P_vap	28.18	kPa	325.21	Calculated Property
P_vap	86.40	kPa	351.36	Calculated Property
P_vap	220.84	kPa	377.52	Calculated Property
P_vap	490.18	kPa	403.68	Calculated Property
P_vap	973.21	kPa	429.84	Calculated Property
P_vap	1766.54	kPa	455.99	Calculated Property
P_vap	2980.40	kPa	482.15	Calculated Property
P_vap	4733.35	kPa	508.31	Calculated Property
P_vap	[3.30e-05; 4751.86]	kPa	[185.28; 508.31]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			7.13411e+01
Coefficient B			-7.69090e+03
Coefficient C			-7.69405e+00
Coefficient D			7.65635e-07
Temperature range, min.			185.28
Temperature range, max.			508.31

P_vap	3.30e-05	kPa	185.28	Calculated Property
P_vap	7.19e-03	kPa	221.17	Calculated Property
P_vap	0.29	kPa	257.06	Calculated Property
P_vap	4.27	kPa	292.96	Calculated Property
P_vap	31.34	kPa	328.85	Calculated Property
P_vap	143.80	kPa	364.74	Calculated Property
P_vap	471.71	kPa	400.63	Calculated Property
P_vap	1209.10	kPa	436.53	Calculated Property
P_vap	2574.02	kPa	472.42	Calculated Property
P_vap	4751.86	kPa	508.31	Calculated Property

Similar Compounds

Find more compounds similar to Isopropyl Alcohol.

Mixtures

Find more mixtures with Isopropyl Alcohol.

Sources

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.

Chemical Properties of Isopropyl Alcohol (CAS 67-63-0)

Contents