Mixture of Ethanol, 2,2,2-trifluoro- + Quinoline

Excel

Ethanol, 2,2,2-trifluoro-

Name
Ethanol, 2,2,2-trifluoro-
InChI
InChI=1S/C2H3F3O/c3-2(4,5)1-6/h6H,1H2
InChI Key
RHQDFWAXVIIEBN-UHFFFAOYSA-N
Formula
C2H3F3O
SMILES
OCC(F)(F)F
Mol. Weight (g/mol)
100.04
CAS
75-89-8

Quinoline

Name
Quinoline
InChI
InChI=1S/C9H7N/c1-2-6-9-8(4-1)5-3-7-10-9/h1-7H
InChI Key
SMWDFEZZVXVKRB-UHFFFAOYSA-N
Formula
C9H7N
SMILES
c1ccc2ncccc2c1
Mol. Weight (g/mol)
129.16
CAS
91-22-5
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)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Ethanol, 2,2,2-trifluoro- (1) [ref]

Fixed Measured
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Pressure, kPa - Liquid Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Gas
0.0000 13.33 0.0000
0.0000 53.33 0.0000
0.0000 101.33 0.0000
0.0202 13.33 0.2957
0.0301 53.33 0.3641
0.0301 101.33 0.3602
0.0356 13.33 0.4829
0.0387 53.33 0.4744
0.0604 101.33 0.5581
0.0732 53.33 0.6893
0.0784 13.33 0.7397
0.1060 101.33 0.7822
0.1180 13.33 0.8536
0.1197 53.33 0.8166
0.1389 101.33 0.8521
0.1594 53.33 0.8882
0.1686 13.33 0.9159
0.1907 101.33 0.9098
0.2134 53.33 0.9310
0.2473 101.33 0.9506
0.2701 13.33 0.9680
0.2959 53.33 0.9670
0.2994 101.33 0.9704
0.3517 13.33 0.9817
0.3791 53.33 0.9834
0.3833 101.33 0.9829
0.4201 13.33 0.9900
0.4557 53.33 0.9922
0.5171 101.33 0.9951
0.5318 13.33 0.9945
0.5851 53.33 0.9961
0.6054 101.33 0.9980
0.6484 13.33 0.9965
0.6840 101.33 0.9985
0.7804 53.33 0.9974
0.8133 13.33 0.9978
0.8377 101.33 0.9990
0.8556 13.33 0.9989
0.9584 53.33 0.9982
1.0000 13.33 1.0000
1.0000 53.33 1.0000
1.0000 101.33 1.0000

Mole fraction of Ethanol, 2,2,2-trifluoro- (1) [ref]

Fixed Measured
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Pressure, kPa - Liquid Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Gas
0.0000 13.33 0.0000
0.0000 53.33 0.0000
0.0000 101.33 0.0000
0.0202 13.33 0.2957
0.0301 53.33 0.3641
0.0301 101.33 0.3602
0.0356 13.33 0.4829
0.0387 53.33 0.4744
0.0604 101.33 0.5581
0.0732 53.33 0.6893
0.0784 13.33 0.7397
0.1060 101.33 0.7822
0.1180 13.33 0.8536
0.1197 53.33 0.8166
0.1389 101.33 0.8521
0.1594 53.33 0.8882
0.1686 13.33 0.9159
0.1907 101.33 0.9098
0.2134 53.33 0.9310
0.2473 101.33 0.9506
0.2701 13.33 0.9680
0.2959 53.33 0.9670
0.2994 101.33 0.9704
0.3517 13.33 0.9817
0.3791 53.33 0.9834
0.3833 101.33 0.9829
0.4201 13.33 0.9900
0.4557 53.33 0.9922
0.5171 101.33 0.9951
0.5318 13.33 0.9945
0.5851 53.33 0.9961
0.6054 101.33 0.9980
0.6484 13.33 0.9965
0.6840 101.33 0.9985
0.7804 53.33 0.9974
0.8133 13.33 0.9978
0.8377 101.33 0.9990
0.8556 13.33 0.9989
0.9584 53.33 0.9982
1.0000 13.33 1.0000
1.0000 53.33 1.0000
1.0000 101.33 1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mass fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
293.15 1.0000 7.19
297.85 1.0000 9.52
312.15 1.0000 20.92
312.75 0.7604 17.53
315.25 0.6065 11.80
322.95 1.0000 36.00
326.95 0.7604 33.66
327.95 0.6065 22.33
328.45 1.0000 46.60
330.45 0.7604 42.46
332.55 0.4040 11.47
336.35 0.6065 33.46
338.15 0.7604 57.26
343.15 1.0000 88.34
343.45 0.2038 6.93
346.45 0.7604 84.99
350.55 0.4040 26.20
350.55 0.6065 61.39
351.15 0.7604 100.79
359.65 0.4040 40.73
360.35 0.6065 91.93
362.95 0.6065 100.59
363.85 0.2038 16.73
365.35 0.4040 52.66
374.85 0.4040 70.73
376.75 0.2038 29.26
381.95 0.4040 94.53
390.25 0.2038 51.06
399.15 0.2038 74.39
407.25 0.2038 97.79
408.35 0.0000 6.60
423.45 0.0000 11.60
434.25 0.0000 15.60
443.65 0.0000 23.46
450.75 0.0000 26.93
458.55 0.0000 33.06

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mass fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
293.15 1.0000 7.19
297.85 1.0000 9.52
312.15 1.0000 20.92
312.75 0.7604 17.53
315.25 0.6065 11.80
322.95 1.0000 36.00
326.95 0.7604 33.66
327.95 0.6065 22.33
328.45 1.0000 46.60
330.45 0.7604 42.46
332.55 0.4040 11.47
336.35 0.6065 33.46
338.15 0.7604 57.26
343.15 1.0000 88.34
343.45 0.2038 6.93
346.45 0.7604 84.99
350.55 0.4040 26.20
350.55 0.6065 61.39
351.15 0.7604 100.79
359.65 0.4040 40.73
360.35 0.6065 91.93
362.95 0.6065 100.59
363.85 0.2038 16.73
365.35 0.4040 52.66
374.85 0.4040 70.73
376.75 0.2038 29.26
381.95 0.4040 94.53
390.25 0.2038 51.06
399.15 0.2038 74.39
407.25 0.2038 97.79
408.35 0.0000 6.60
423.45 0.0000 11.60
434.25 0.0000 15.60
443.65 0.0000 23.46
450.75 0.0000 26.93
458.55 0.0000 33.06

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 13.33 435.45
0.0000 53.33 483.15
0.0000 101.33 510.85
0.0202 13.33 425.65
0.0301 53.33 466.05
0.0301 101.33 491.25
0.0356 13.33 417.65
0.0387 53.33 460.15
0.0604 101.33 477.25
0.0732 53.33 443.85
0.0784 13.33 400.95
0.1060 101.33 455.45
0.1180 13.33 388.15
0.1197 53.33 428.25
0.1389 101.33 442.85
0.1594 53.33 417.15
0.1686 13.33 376.35
0.1907 101.33 429.55
0.2134 53.33 404.55
0.2473 101.33 416.45
0.2701 13.33 359.05
0.2959 53.33 389.45
0.2994 101.33 406.35
0.3517 13.33 347.45
0.3791 53.33 376.65
0.3833 101.33 394.25
0.4201 13.33 339.65
0.4557 53.33 367.65
0.5171 101.33 378.85
0.5318 13.33 328.85
0.5851 53.33 355.95
0.6054 101.33 369.35
0.6484 13.33 318.65
0.6840 101.33 362.85
0.7804 53.33 341.05
0.8133 13.33 310.15
0.8377 101.33 353.55
0.8556 13.33 308.65
0.9584 53.33 332.55
1.0000 13.33 304.05
1.0000 53.33 331.75
1.0000 101.33 347.15

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of Ethanol, 2,2,2-trifluoro- (1) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 13.33 435.45
0.0000 53.33 483.15
0.0000 101.33 510.85
0.0202 13.33 425.65
0.0301 53.33 466.05
0.0301 101.33 491.25
0.0356 13.33 417.65
0.0387 53.33 460.15
0.0604 101.33 477.25
0.0732 53.33 443.85
0.0784 13.33 400.95
0.1060 101.33 455.45
0.1180 13.33 388.15
0.1197 53.33 428.25
0.1389 101.33 442.85
0.1594 53.33 417.15
0.1686 13.33 376.35
0.1907 101.33 429.55
0.2134 53.33 404.55
0.2473 101.33 416.45
0.2701 13.33 359.05
0.2959 53.33 389.45
0.2994 101.33 406.35
0.3517 13.33 347.45
0.3791 53.33 376.65
0.3833 101.33 394.25
0.4201 13.33 339.65
0.4557 53.33 367.65
0.5171 101.33 378.85
0.5318 13.33 328.85
0.5851 53.33 355.95
0.6054 101.33 369.35
0.6484 13.33 318.65
0.6840 101.33 362.85
0.7804 53.33 341.05
0.8133 13.33 310.15
0.8377 101.33 353.55
0.8556 13.33 308.65
0.9584 53.33 332.55
1.0000 13.33 304.05
1.0000 53.33 331.75
1.0000 101.33 347.15

Sources