Mixture of 2-Pyrrolidinone, 1-methyl- + Acetic acid

Excel

2-Pyrrolidinone, 1-methyl-

Name
2-Pyrrolidinone, 1-methyl-
InChI
InChI=1S/C5H9NO/c1-6-4-2-3-5(6)7/h2-4H2,1H3
InChI Key
SECXISVLQFMRJM-UHFFFAOYSA-N
Formula
C5H9NO
SMILES
CN1CCCC1=O
Mol. Weight (g/mol)
99.13
CAS
872-50-4

Acetic acid

Name
Acetic acid
InChI
InChI=1S/C2H4O2/c1-2(3)4/h1H3,(H,3,4)
InChI Key
QTBSBXVTEAMEQO-UHFFFAOYSA-N
Formula
C2H4O2
SMILES
CC(=O)O
Mol. Weight (g/mol)
60.05
CAS
64-19-7
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. Tboil - Boiling temperature at pressure P, K (2)
  3. Vapor Liquid Equilibrium at Constant Pressure (2)

Mole fraction of Acetic acid (2) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Acetic acid (2) - Liquid Mole fraction of Acetic acid (2) - Gas
0.0600 0.1123
0.1081 0.2112
0.1761 0.3266
0.2443 0.4606
0.3035 0.5834
0.3452 0.6593
0.3924 0.7231
0.4418 0.7910
0.4690 0.8186
0.5030 0.8730
0.5390 0.9045
0.5598 0.9167
0.5803 0.9340
0.6104 0.9506
0.6556 0.9631
0.6864 0.9683
0.7112 0.9808
0.7549 0.9822
0.7935 0.9877
0.8319 0.9900
0.8661 0.9931

Mole fraction of Acetic acid (2) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Acetic acid (2) - Liquid Mole fraction of Acetic acid (2) - Gas
0.0600 0.1123
0.1081 0.2112
0.1761 0.3266
0.2443 0.4606
0.3035 0.5834
0.3452 0.6593
0.3924 0.7231
0.4418 0.7910
0.4690 0.8186
0.5030 0.8730
0.5390 0.9045
0.5598 0.9167
0.5803 0.9340
0.6104 0.9506
0.6556 0.9631
0.6864 0.9683
0.7112 0.9808
0.7549 0.9822
0.7935 0.9877
0.8319 0.9900
0.8661 0.9931

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Acetic acid (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0600 475.02
0.1081 472.68
0.1761 470.40
0.2443 467.13
0.3035 463.42
0.3452 460.54
0.3924 456.52
0.4418 451.92
0.4690 448.17
0.5030 444.28
0.5390 440.81
0.5598 437.56
0.5803 435.11
0.6104 430.83
0.6556 424.42
0.6864 420.45
0.7112 417.71
0.7549 411.22
0.7935 407.99
0.8319 403.67
0.8661 400.75

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Acetic acid (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0600 475.02
0.1081 472.68
0.1761 470.40
0.2443 467.13
0.3035 463.42
0.3452 460.54
0.3924 456.52
0.4418 451.92
0.4690 448.17
0.5030 444.28
0.5390 440.81
0.5598 437.56
0.5803 435.11
0.6104 430.83
0.6556 424.42
0.6864 420.45
0.7112 417.71
0.7549 411.22
0.7935 407.99
0.8319 403.67
0.8661 400.75

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Acetic acid (2) - Liquid y1[mol/mol] of Acetic acid (2) - Vapour
477.01 0.0000 0.0000
475.02 0.0600 0.1123
472.68 0.1081 0.2112
470.4 0.1761 0.3266
467.13 0.2443 0.4606
463.42 0.3035 0.5834
460.54 0.3452 0.6593
456.52 0.3924 0.7231
451.92 0.4418 0.7910
448.17 0.4690 0.8186
444.28 0.5030 0.8730
440.81 0.5390 0.9045
437.56 0.5598 0.9167
435.11 0.5803 0.9340
430.83 0.6104 0.9506
424.42 0.6556 0.9631
420.45 0.6864 0.9683
417.71 0.7112 0.9808
411.22 0.7549 0.9822
407.99 0.7935 0.9877
403.67 0.8319 0.9900
400.75 0.8661 0.9931
390.85 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 26.67 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of Acetic acid (2) - Liquid y1[mol/mol] of Acetic acid (2) - Vapour
428.65 0.0000 0.0000
428.35 0.1128 0.1627
427.8 0.1490 0.2294
426.8 0.1941 0.3207
425.5 0.2368 0.4129
423.15 0.2894 0.5287
419.95 0.3453 0.6462
414.15 0.4127 0.7688
403.5 0.5091 0.8927
390.85 0.5968 0.9550
374.65 0.7312 0.9917
364.1 0.8175 0.9979
353.0 1.0000 1.0000

Sources