Mixture of Ethanol + Nitroxoline + Ethyl Acetate

Excel

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5

Nitroxoline

Name
Nitroxoline
InChI
InChI=1S/C9H6N2O3/c12-8-4-3-7(11(13)14)6-2-1-5-10-9(6)8/h1-5,12H
InChI Key
RJIWZDNTCBHXAL-UHFFFAOYSA-N
Formula
C9H6N2O3
SMILES
O=[N+]([O-])c1ccc(O)c2ncccc12
Mol. Weight (g/mol)
190.16
CAS
4008-48-4

Ethyl Acetate

Name
Ethyl Acetate
InChI
InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
InChI Key
XEKOWRVHYACXOJ-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
CCOC(C)=O
Mol. Weight (g/mol)
88.11
CAS
141-78-6
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Datasets

  1. Mole fraction (2)

Mole fraction of Nitroxoline (2) [ref]

Operational condition: Pressure, kPa = 101.1 (Liquid)

Fixed Measured
Temperature, K - Liquid Solvent: Mass fraction of Ethyl Acetate (3) - Liquid Mole fraction of Nitroxoline (2) - Liquid
278.15 0.1006 0.0007
283.15 0.1006 0.0008
288.15 0.1006 0.0011
293.15 0.1006 0.0012
298.15 0.1006 0.0015
303.15 0.1006 0.0017
308.15 0.1006 0.0021
313.15 0.1006 0.0025
278.15 0.2011 0.0009
283.15 0.2011 0.0011
288.15 0.2011 0.0013
293.15 0.2011 0.0015
298.15 0.2011 0.0018
303.15 0.2011 0.0022
308.15 0.2011 0.0025
313.15 0.2011 0.0031
278.15 0.2994 0.0011
283.15 0.2994 0.0013
288.15 0.2994 0.0015
293.15 0.2994 0.0019
298.15 0.2994 0.0022
303.15 0.2994 0.0027
308.15 0.2994 0.0031
313.15 0.2994 0.0037
278.15 0.4007 0.0014
283.15 0.4007 0.0016
288.15 0.4007 0.0019
293.15 0.4007 0.0024
298.15 0.4007 0.0027
303.15 0.4007 0.0033
308.15 0.4007 0.0038
313.15 0.4007 0.0045
278.15 0.4998 0.0017
283.15 0.4998 0.0020
288.15 0.4998 0.0023
293.15 0.4998 0.0028
298.15 0.4998 0.0032
303.15 0.4998 0.0039
308.15 0.4998 0.0045
313.15 0.4998 0.0054
278.15 0.6002 0.0020
283.15 0.6002 0.0023
288.15 0.6002 0.0029
293.15 0.6002 0.0034
298.15 0.6002 0.0040
303.15 0.6002 0.0048
308.15 0.6002 0.0056
313.15 0.6002 0.0066
278.15 0.6993 0.0024
283.15 0.6993 0.0027
288.15 0.6993 0.0033
293.15 0.6993 0.0039
298.15 0.6993 0.0048
303.15 0.6993 0.0055
308.15 0.6993 0.0066
313.15 0.6993 0.0078
278.15 0.8001 0.0027
283.15 0.8001 0.0033
288.15 0.8001 0.0038
293.15 0.8001 0.0046
298.15 0.8001 0.0055
303.15 0.8001 0.0064
308.15 0.8001 0.0074
313.15 0.8001 0.0089
278.15 0.9009 0.0031
283.15 0.9009 0.0036
288.15 0.9009 0.0044
293.15 0.9009 0.0051
298.15 0.9009 0.0062
303.15 0.9009 0.0073
308.15 0.9009 0.0084
313.15 0.9009 0.0100

Mole fraction of Nitroxoline (2) [ref]

Operational condition: Pressure, kPa = 101.1 (Liquid)

Fixed Measured
Temperature, K - Liquid Solvent: Mass fraction of Ethyl Acetate (3) - Liquid Mole fraction of Nitroxoline (2) - Liquid
278.15 0.1006 0.0007
283.15 0.1006 0.0008
288.15 0.1006 0.0011
293.15 0.1006 0.0012
298.15 0.1006 0.0015
303.15 0.1006 0.0017
308.15 0.1006 0.0021
313.15 0.1006 0.0025
278.15 0.2011 0.0009
283.15 0.2011 0.0011
288.15 0.2011 0.0013
293.15 0.2011 0.0015
298.15 0.2011 0.0018
303.15 0.2011 0.0022
308.15 0.2011 0.0025
313.15 0.2011 0.0031
278.15 0.2994 0.0011
283.15 0.2994 0.0013
288.15 0.2994 0.0015
293.15 0.2994 0.0019
298.15 0.2994 0.0022
303.15 0.2994 0.0027
308.15 0.2994 0.0031
313.15 0.2994 0.0037
278.15 0.4007 0.0014
283.15 0.4007 0.0016
288.15 0.4007 0.0019
293.15 0.4007 0.0024
298.15 0.4007 0.0027
303.15 0.4007 0.0033
308.15 0.4007 0.0038
313.15 0.4007 0.0045
278.15 0.4998 0.0017
283.15 0.4998 0.0020
288.15 0.4998 0.0023
293.15 0.4998 0.0028
298.15 0.4998 0.0032
303.15 0.4998 0.0039
308.15 0.4998 0.0045
313.15 0.4998 0.0054
278.15 0.6002 0.0020
283.15 0.6002 0.0023
288.15 0.6002 0.0029
293.15 0.6002 0.0034
298.15 0.6002 0.0040
303.15 0.6002 0.0048
308.15 0.6002 0.0056
313.15 0.6002 0.0066
278.15 0.6993 0.0024
283.15 0.6993 0.0027
288.15 0.6993 0.0033
293.15 0.6993 0.0039
298.15 0.6993 0.0048
303.15 0.6993 0.0055
308.15 0.6993 0.0066
313.15 0.6993 0.0078
278.15 0.8001 0.0027
283.15 0.8001 0.0033
288.15 0.8001 0.0038
293.15 0.8001 0.0046
298.15 0.8001 0.0055
303.15 0.8001 0.0064
308.15 0.8001 0.0074
313.15 0.8001 0.0089
278.15 0.9009 0.0031
283.15 0.9009 0.0036
288.15 0.9009 0.0044
293.15 0.9009 0.0051
298.15 0.9009 0.0062
303.15 0.9009 0.0073
308.15 0.9009 0.0084
313.15 0.9009 0.0100

Sources