Mixture of 2-Pyrrolidinone, 1-methyl- + 1-Butanol

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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

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3
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Datasets

  1. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (2)
  3. Vapor Liquid Equilibrium at Constant Pressure (3)

Mole fraction of 1-Butanol (2) [ref]

Fixed Measured
Mole fraction of 1-Butanol (2) - Liquid Pressure, kPa - Liquid Mole fraction of 1-Butanol (2) - Gas
0.0000 10.00 0.0000
0.0110 10.00 0.0870
0.0160 10.00 0.1240
0.0450 10.00 0.2780
0.0830 10.00 0.4400
0.1350 10.00 0.5770
0.1590 10.00 0.6260
0.1850 10.00 0.6820
0.2490 10.00 0.7640
0.3410 10.00 0.8550
0.5680 10.00 0.9550
0.6550 10.00 0.9700
0.7400 10.00 0.9750
0.8650 10.00 0.9920
0.9270 10.00 0.9980
1.0000 10.00 1.0000
0.0000 25.00 0.0000
0.0130 25.00 0.0910
0.0210 25.00 0.1310
0.0490 25.00 0.2520
0.0630 25.00 0.3140
0.1020 25.00 0.4410
0.1300 25.00 0.5620
0.1820 25.00 0.6710
0.2710 25.00 0.7790
0.3160 25.00 0.8240
0.3710 25.00 0.8670
0.5130 25.00 0.9330
0.5790 25.00 0.9530
0.6350 25.00 0.9680
0.6860 25.00 0.9750
0.8730 25.00 0.9900
0.9280 25.00 0.9950
1.0000 25.00 1.0000
0.0000 50.00 0.0000
0.0140 50.00 0.0870
0.0190 50.00 0.1500
0.0520 50.00 0.2820
0.0690 50.00 0.3700
0.1090 50.00 0.4620
0.1820 50.00 0.6480
0.2860 50.00 0.7660
0.3480 50.00 0.8390
0.5280 50.00 0.9340
0.6550 50.00 0.9640
0.7080 50.00 0.9770
0.8550 50.00 0.9860
0.8900 50.00 0.9920
1.0000 50.00 1.0000

Mole fraction of 1-Butanol (2) [ref]

Fixed Measured
Mole fraction of 1-Butanol (2) - Liquid Pressure, kPa - Liquid Mole fraction of 1-Butanol (2) - Gas
0.0000 10.00 0.0000
0.0110 10.00 0.0870
0.0160 10.00 0.1240
0.0450 10.00 0.2780
0.0830 10.00 0.4400
0.1350 10.00 0.5770
0.1590 10.00 0.6260
0.1850 10.00 0.6820
0.2490 10.00 0.7640
0.3410 10.00 0.8550
0.5680 10.00 0.9550
0.6550 10.00 0.9700
0.7400 10.00 0.9750
0.8650 10.00 0.9920
0.9270 10.00 0.9980
1.0000 10.00 1.0000
0.0000 25.00 0.0000
0.0130 25.00 0.0910
0.0210 25.00 0.1310
0.0490 25.00 0.2520
0.0630 25.00 0.3140
0.1020 25.00 0.4410
0.1300 25.00 0.5620
0.1820 25.00 0.6710
0.2710 25.00 0.7790
0.3160 25.00 0.8240
0.3710 25.00 0.8670
0.5130 25.00 0.9330
0.5790 25.00 0.9530
0.6350 25.00 0.9680
0.6860 25.00 0.9750
0.8730 25.00 0.9900
0.9280 25.00 0.9950
1.0000 25.00 1.0000
0.0000 50.00 0.0000
0.0140 50.00 0.0870
0.0190 50.00 0.1500
0.0520 50.00 0.2820
0.0690 50.00 0.3700
0.1090 50.00 0.4620
0.1820 50.00 0.6480
0.2860 50.00 0.7660
0.3480 50.00 0.8390
0.5280 50.00 0.9340
0.6550 50.00 0.9640
0.7080 50.00 0.9770
0.8550 50.00 0.9860
0.8900 50.00 0.9920
1.0000 50.00 1.0000

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of 1-Butanol (2) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 10.00 399.53
0.0110 10.00 397.98
0.0160 10.00 397.06
0.0450 10.00 393.15
0.0830 10.00 388.47
0.1350 10.00 383.73
0.1590 10.00 380.51
0.1850 10.00 377.39
0.2490 10.00 372.68
0.3410 10.00 365.38
0.5680 10.00 350.55
0.6550 10.00 347.35
0.7400 10.00 343.89
0.8650 10.00 340.65
0.9270 10.00 339.22
1.0000 10.00 337.80
0.0000 25.00 425.91
0.0130 25.00 423.60
0.0210 25.00 422.54
0.0490 25.00 418.32
0.0630 25.00 416.11
0.1020 25.00 411.16
0.1300 25.00 407.16
0.1820 25.00 401.60
0.2710 25.00 393.54
0.3160 25.00 389.56
0.3710 25.00 384.68
0.5130 25.00 374.41
0.5790 25.00 370.44
0.6350 25.00 367.98
0.6860 25.00 365.31
0.8730 25.00 358.90
0.9280 25.00 357.27
1.0000 25.00 355.78
0.0000 50.00 448.97
0.0140 50.00 446.08
0.0190 50.00 444.56
0.0520 50.00 439.55
0.0690 50.00 436.22
0.1090 50.00 430.81
0.1820 50.00 421.48
0.2860 50.00 411.75
0.3480 50.00 406.06
0.5280 50.00 393.37
0.6550 50.00 386.84
0.7080 50.00 383.86
0.8550 50.00 378.08
0.8900 50.00 376.60
1.0000 50.00 371.94

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of 1-Butanol (2) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 10.00 399.53
0.0110 10.00 397.98
0.0160 10.00 397.06
0.0450 10.00 393.15
0.0830 10.00 388.47
0.1350 10.00 383.73
0.1590 10.00 380.51
0.1850 10.00 377.39
0.2490 10.00 372.68
0.3410 10.00 365.38
0.5680 10.00 350.55
0.6550 10.00 347.35
0.7400 10.00 343.89
0.8650 10.00 340.65
0.9270 10.00 339.22
1.0000 10.00 337.80
0.0000 25.00 425.91
0.0130 25.00 423.60
0.0210 25.00 422.54
0.0490 25.00 418.32
0.0630 25.00 416.11
0.1020 25.00 411.16
0.1300 25.00 407.16
0.1820 25.00 401.60
0.2710 25.00 393.54
0.3160 25.00 389.56
0.3710 25.00 384.68
0.5130 25.00 374.41
0.5790 25.00 370.44
0.6350 25.00 367.98
0.6860 25.00 365.31
0.8730 25.00 358.90
0.9280 25.00 357.27
1.0000 25.00 355.78
0.0000 50.00 448.97
0.0140 50.00 446.08
0.0190 50.00 444.56
0.0520 50.00 439.55
0.0690 50.00 436.22
0.1090 50.00 430.81
0.1820 50.00 421.48
0.2860 50.00 411.75
0.3480 50.00 406.06
0.5280 50.00 393.37
0.6550 50.00 386.84
0.7080 50.00 383.86
0.8550 50.00 378.08
0.8900 50.00 376.60
1.0000 50.00 371.94

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 10 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of 1-Butanol (2) - Liquid y1[mol/mol] of 1-Butanol (2) - Vapour
399.53 0.0000 0.0000
397.98 0.0110 0.0870
397.06 0.0160 0.1240
393.15 0.0450 0.2780
388.47 0.0830 0.4400
383.73 0.1350 0.5770
380.51 0.1590 0.6260
377.39 0.1850 0.6820
372.68 0.2490 0.7640
365.38 0.3410 0.8550
350.55 0.5680 0.9550
347.35 0.6550 0.9700
343.89 0.7400 0.9750
340.65 0.8650 0.9920
339.22 0.9270 0.9980
337.8 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 25 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of 1-Butanol (2) - Liquid y1[mol/mol] of 1-Butanol (2) - Vapour
425.91 0.0000 0.0000
423.6 0.0130 0.0910
422.54 0.0210 0.1310
418.32 0.0490 0.2520
416.11 0.0630 0.3140
411.16 0.1020 0.4410
407.16 0.1300 0.5620
401.6 0.1820 0.6710
393.54 0.2710 0.7790
389.56 0.3160 0.8240
384.68 0.3710 0.8670
374.41 0.5130 0.9330
370.44 0.5790 0.9530
367.98 0.6350 0.9680
365.31 0.6860 0.9750
358.9 0.8730 0.9900
357.27 0.9280 0.9950
355.78 1.0000 1.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 50 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of 1-Butanol (2) - Liquid y1[mol/mol] of 1-Butanol (2) - Vapour
448.97 0.0000 0.0000
446.08 0.0140 0.0870
444.56 0.0190 0.1500
439.55 0.0520 0.2820
436.22 0.0690 0.3700
430.81 0.1090 0.4620
421.48 0.1820 0.6480
411.75 0.2860 0.7660
406.06 0.3480 0.8390
393.37 0.5280 0.9340
386.84 0.6550 0.9640
383.86 0.7080 0.9770
378.08 0.8550 0.9860
376.6 0.8900 0.9920
371.94 1.0000 1.0000

Sources