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Mixture of Ethanol + Benzonitrile, 4-nitro- + 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

Benzonitrile, 4-nitro-

Name
Benzonitrile, 4-nitro-
InChI
InChI=1S/C7H4N2O2/c8-5-6-1-3-7(4-2-6)9(10)11/h1-4H
InChI Key
NKJIFDNZPGLLSH-UHFFFAOYSA-N
Formula
C7H4N2O2
SMILES
N#Cc1ccc([N+](=O)[O-])cc1
Mol. Weight (g/mol)
148.12
CAS
619-72-7

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 Benzonitrile, 4-nitro- (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 Benzonitrile, 4-nitro- (2) - Liquid
278.15 0.0000 0.0026
283.15 0.0000 0.0030
288.15 0.0000 0.0038
293.15 0.0000 0.0045
298.15 0.0000 0.0056
303.15 0.0000 0.0067
308.15 0.0000 0.0082
313.15 0.0000 0.0098
318.15 0.0000 0.0116
278.15 0.1000 0.0057
283.15 0.1000 0.0066
288.15 0.1000 0.0081
293.15 0.1000 0.0097
298.15 0.1000 0.0117
303.15 0.1000 0.0140
308.15 0.1000 0.0169
313.15 0.1000 0.0201
318.15 0.1000 0.0236
278.15 0.2000 0.0096
283.15 0.2000 0.0112
288.15 0.2000 0.0135
293.15 0.2000 0.0160
298.15 0.2000 0.0191
303.15 0.2000 0.0227
308.15 0.2000 0.0272
313.15 0.2000 0.0323
318.15 0.2000 0.0377
278.15 0.3000 0.0137
283.15 0.3000 0.0158
288.15 0.3000 0.0190
293.15 0.3000 0.0223
298.15 0.3000 0.0265
303.15 0.3000 0.0313
308.15 0.3000 0.0374
313.15 0.3000 0.0442
318.15 0.3000 0.0517
278.15 0.4000 0.0173
283.15 0.4000 0.0199
288.15 0.4000 0.0238
293.15 0.4000 0.0278
298.15 0.4000 0.0329
303.15 0.4000 0.0388
308.15 0.4000 0.0463
313.15 0.4000 0.0547
318.15 0.4000 0.0641
278.15 0.5000 0.0205
283.15 0.5000 0.0235
288.15 0.5000 0.0280
293.15 0.5000 0.0326
298.15 0.5000 0.0385
303.15 0.5000 0.0452
308.15 0.5000 0.0540
313.15 0.5000 0.0638
318.15 0.5000 0.0749
278.15 0.6000 0.0238
283.15 0.6000 0.0273
288.15 0.6000 0.0323
293.15 0.6000 0.0376
298.15 0.6000 0.0442
303.15 0.6000 0.0519
308.15 0.6000 0.0619
313.15 0.6000 0.0733
318.15 0.6000 0.0863
278.15 0.6998 0.0258
283.15 0.6998 0.0311
288.15 0.6998 0.0374
293.15 0.6998 0.0445
298.15 0.6998 0.0528
303.15 0.6998 0.0623
308.15 0.6998 0.0730
313.15 0.6998 0.0852
318.15 0.6998 0.0989
278.15 0.8000 0.0298
283.15 0.8000 0.0360
288.15 0.8000 0.0432
293.15 0.8000 0.0514
298.15 0.8000 0.0609
303.15 0.8000 0.0717
308.15 0.8000 0.0841
313.15 0.8000 0.0980
318.15 0.8000 0.1137
278.15 0.9000 0.0339
283.15 0.9000 0.0409
288.15 0.9000 0.0490
293.15 0.9000 0.0583
298.15 0.9000 0.0690
303.15 0.9000 0.0813
308.15 0.9000 0.0951
313.15 0.9000 0.1109
318.15 0.9000 0.1286
278.15 1.0000 0.0404
283.15 1.0000 0.0463
288.15 1.0000 0.0538
293.15 1.0000 0.0619
298.15 1.0000 0.0721
303.15 1.0000 0.0842
308.15 1.0000 0.1001
313.15 1.0000 0.1192
318.15 1.0000 0.1422

Mole fraction of Benzonitrile, 4-nitro- (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 Benzonitrile, 4-nitro- (2) - Liquid
278.15 0.0000 0.0026
283.15 0.0000 0.0030
288.15 0.0000 0.0038
293.15 0.0000 0.0045
298.15 0.0000 0.0056
303.15 0.0000 0.0067
308.15 0.0000 0.0082
313.15 0.0000 0.0098
318.15 0.0000 0.0116
278.15 0.1000 0.0057
283.15 0.1000 0.0066
288.15 0.1000 0.0081
293.15 0.1000 0.0097
298.15 0.1000 0.0117
303.15 0.1000 0.0140
308.15 0.1000 0.0169
313.15 0.1000 0.0201
318.15 0.1000 0.0236
278.15 0.2000 0.0096
283.15 0.2000 0.0112
288.15 0.2000 0.0135
293.15 0.2000 0.0160
298.15 0.2000 0.0191
303.15 0.2000 0.0227
308.15 0.2000 0.0272
313.15 0.2000 0.0323
318.15 0.2000 0.0377
278.15 0.3000 0.0137
283.15 0.3000 0.0158
288.15 0.3000 0.0190
293.15 0.3000 0.0223
298.15 0.3000 0.0265
303.15 0.3000 0.0313
308.15 0.3000 0.0374
313.15 0.3000 0.0442
318.15 0.3000 0.0517
278.15 0.4000 0.0173
283.15 0.4000 0.0199
288.15 0.4000 0.0238
293.15 0.4000 0.0278
298.15 0.4000 0.0329
303.15 0.4000 0.0388
308.15 0.4000 0.0463
313.15 0.4000 0.0547
318.15 0.4000 0.0641
278.15 0.5000 0.0205
283.15 0.5000 0.0235
288.15 0.5000 0.0280
293.15 0.5000 0.0326
298.15 0.5000 0.0385
303.15 0.5000 0.0452
308.15 0.5000 0.0540
313.15 0.5000 0.0638
318.15 0.5000 0.0749
278.15 0.6000 0.0238
283.15 0.6000 0.0273
288.15 0.6000 0.0323
293.15 0.6000 0.0376
298.15 0.6000 0.0442
303.15 0.6000 0.0519
308.15 0.6000 0.0619
313.15 0.6000 0.0733
318.15 0.6000 0.0863
278.15 0.6998 0.0258
283.15 0.6998 0.0311
288.15 0.6998 0.0374
293.15 0.6998 0.0445
298.15 0.6998 0.0528
303.15 0.6998 0.0623
308.15 0.6998 0.0730
313.15 0.6998 0.0852
318.15 0.6998 0.0989
278.15 0.8000 0.0298
283.15 0.8000 0.0360
288.15 0.8000 0.0432
293.15 0.8000 0.0514
298.15 0.8000 0.0609
303.15 0.8000 0.0717
308.15 0.8000 0.0841
313.15 0.8000 0.0980
318.15 0.8000 0.1137
278.15 0.9000 0.0339
283.15 0.9000 0.0409
288.15 0.9000 0.0490
293.15 0.9000 0.0583
298.15 0.9000 0.0690
303.15 0.9000 0.0813
308.15 0.9000 0.0951
313.15 0.9000 0.1109
318.15 0.9000 0.1286
278.15 1.0000 0.0404
283.15 1.0000 0.0463
288.15 1.0000 0.0538
293.15 1.0000 0.0619
298.15 1.0000 0.0721
303.15 1.0000 0.0842
308.15 1.0000 0.1001
313.15 1.0000 0.1192
318.15 1.0000 0.1422

Sources