Mixture of 1-Propanol + Benzonitrile, 4-nitro- + Ethyl Acetate

Excel

1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

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
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.

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 0.0023
283.15 0.0000 0.0027
288.15 0.0000 0.0033
293.15 0.0000 0.0041
298.15 0.0000 0.0050
303.15 0.0000 0.0062
308.15 0.0000 0.0076
313.15 0.0000 0.0091
318.15 0.0000 0.0108
278.15 0.1000 0.0053
283.15 0.1000 0.0063
288.15 0.1000 0.0075
293.15 0.1000 0.0091
298.15 0.1000 0.0112
303.15 0.1000 0.0135
308.15 0.1000 0.0163
313.15 0.1000 0.0194
318.15 0.1000 0.0229
278.15 0.2000 0.0093
283.15 0.2000 0.0108
288.15 0.2000 0.0129
293.15 0.2000 0.0154
298.15 0.2000 0.0187
303.15 0.2000 0.0224
308.15 0.2000 0.0269
313.15 0.2000 0.0318
318.15 0.2000 0.0374
278.15 0.3000 0.0133
283.15 0.3000 0.0155
288.15 0.3000 0.0183
293.15 0.3000 0.0217
298.15 0.3000 0.0261
303.15 0.3000 0.0311
308.15 0.3000 0.0373
313.15 0.3000 0.0440
318.15 0.3000 0.0517
278.15 0.4000 0.0169
283.15 0.4000 0.0196
288.15 0.4000 0.0231
293.15 0.4000 0.0272
298.15 0.4000 0.0325
303.15 0.4000 0.0386
308.15 0.4000 0.0461
313.15 0.4000 0.0544
318.15 0.4000 0.0641
278.15 0.5000 0.0200
283.15 0.5000 0.0231
288.15 0.5000 0.0272
293.15 0.5000 0.0320
298.15 0.5000 0.0380
303.15 0.5000 0.0449
308.15 0.5000 0.0537
313.15 0.5000 0.0634
318.15 0.5000 0.0748
278.15 0.6000 0.0217
283.15 0.6000 0.0263
288.15 0.6000 0.0317
293.15 0.6000 0.0379
298.15 0.6000 0.0451
303.15 0.6000 0.0534
308.15 0.6000 0.0628
313.15 0.6000 0.0735
318.15 0.6000 0.0856
278.15 0.7000 0.0253
283.15 0.7000 0.0306
288.15 0.7000 0.0368
293.15 0.7000 0.0440
298.15 0.7000 0.0522
303.15 0.7000 0.0617
308.15 0.7000 0.0724
313.15 0.7000 0.0847
318.15 0.7000 0.0985
278.15 0.8000 0.0295
283.15 0.8000 0.0356
288.15 0.8000 0.0427
293.15 0.8000 0.0510
298.15 0.8000 0.0605
303.15 0.8000 0.0713
308.15 0.8000 0.0836
313.15 0.8000 0.0976
318.15 0.8000 0.1134
278.15 0.9000 0.0370
283.15 0.9000 0.0423
288.15 0.9000 0.0493
293.15 0.9000 0.0569
298.15 0.9000 0.0665
303.15 0.9000 0.0778
308.15 0.9000 0.0925
313.15 0.9000 0.1099
318.15 0.9000 0.1307
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 0.0023
283.15 0.0000 0.0027
288.15 0.0000 0.0033
293.15 0.0000 0.0041
298.15 0.0000 0.0050
303.15 0.0000 0.0062
308.15 0.0000 0.0076
313.15 0.0000 0.0091
318.15 0.0000 0.0108
278.15 0.1000 0.0053
283.15 0.1000 0.0063
288.15 0.1000 0.0075
293.15 0.1000 0.0091
298.15 0.1000 0.0112
303.15 0.1000 0.0135
308.15 0.1000 0.0163
313.15 0.1000 0.0194
318.15 0.1000 0.0229
278.15 0.2000 0.0093
283.15 0.2000 0.0108
288.15 0.2000 0.0129
293.15 0.2000 0.0154
298.15 0.2000 0.0187
303.15 0.2000 0.0224
308.15 0.2000 0.0269
313.15 0.2000 0.0318
318.15 0.2000 0.0374
278.15 0.3000 0.0133
283.15 0.3000 0.0155
288.15 0.3000 0.0183
293.15 0.3000 0.0217
298.15 0.3000 0.0261
303.15 0.3000 0.0311
308.15 0.3000 0.0373
313.15 0.3000 0.0440
318.15 0.3000 0.0517
278.15 0.4000 0.0169
283.15 0.4000 0.0196
288.15 0.4000 0.0231
293.15 0.4000 0.0272
298.15 0.4000 0.0325
303.15 0.4000 0.0386
308.15 0.4000 0.0461
313.15 0.4000 0.0544
318.15 0.4000 0.0641
278.15 0.5000 0.0200
283.15 0.5000 0.0231
288.15 0.5000 0.0272
293.15 0.5000 0.0320
298.15 0.5000 0.0380
303.15 0.5000 0.0449
308.15 0.5000 0.0537
313.15 0.5000 0.0634
318.15 0.5000 0.0748
278.15 0.6000 0.0217
283.15 0.6000 0.0263
288.15 0.6000 0.0317
293.15 0.6000 0.0379
298.15 0.6000 0.0451
303.15 0.6000 0.0534
308.15 0.6000 0.0628
313.15 0.6000 0.0735
318.15 0.6000 0.0856
278.15 0.7000 0.0253
283.15 0.7000 0.0306
288.15 0.7000 0.0368
293.15 0.7000 0.0440
298.15 0.7000 0.0522
303.15 0.7000 0.0617
308.15 0.7000 0.0724
313.15 0.7000 0.0847
318.15 0.7000 0.0985
278.15 0.8000 0.0295
283.15 0.8000 0.0356
288.15 0.8000 0.0427
293.15 0.8000 0.0510
298.15 0.8000 0.0605
303.15 0.8000 0.0713
308.15 0.8000 0.0836
313.15 0.8000 0.0976
318.15 0.8000 0.1134
278.15 0.9000 0.0370
283.15 0.9000 0.0423
288.15 0.9000 0.0493
293.15 0.9000 0.0569
298.15 0.9000 0.0665
303.15 0.9000 0.0778
308.15 0.9000 0.0925
313.15 0.9000 0.1099
318.15 0.9000 0.1307
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