Vapor-Liquid Equilibria at 101.32 kPa and Excess Properties of Binary Mixtures of Butyl Esters + tert-Butyl Alcohol Ortega, J.; Espiau, F.; Postigo, M.; Journal of Chemical & Engineering Data 2005, 50, 444-454
Data
T (K) P (kPa)
387.18 40.26
395.28 52.03
396.18 53.34
396.91 54.73
397.72 56.1
398.53 57.26
399.29 58.69
400.03 60.1
400.72 61.25
401.38 62.7
402.18 64.23
388.03 41.4
402.86 65.35
403.54 66.67
404.16 67.83
404.90 69.61
405.46 70.61
406.11 71.99
406.78 73.29
407.36 74.67
408.00 76.11
408.63 77.38
389.10 42.6
409.19 78.73
409.80 80.02
410.38 81.65
410.93 82.73
411.48 83.95
412.00 85.51
412.55 86.67
413.02 87.99
413.63 89.54
414.13 90.67
390.14 44.02
414.66 91.88
415.18 93.32
415.73 94.7
416.21 96.14
416.69 97.24
417.14 98.74
417.68 100.02
418.07 101.32
418.58 102.59
419.08 104.03
391.06 45.33
419.61 105.43
420.08 106.86
420.46 108.04
420.89 109.22
421.38 110.68
421.80 112.04
422.28 113.36
422.69 114.63
423.12 116.04
423.56 117.36
391.78 46.65
423.97 118.81
424.39 120.03
424.78 121.33
425.20 122.73
425.60 124.01
426.04 125.41
426.39 126.63
426.82 128.04
427.21 129.35
427.63 130.85
392.85 48.02
427.95 131.99
428.39 133.39
428.76 134.72
429.12 136.0
429.52 137.44
429.87 138.73
430.23 140.03
430.57 141.24
430.99 142.76
431.29 143.91
393.76 49.46
431.72 145.53
432.06 146.8
432.41 148.15
432.75 149.39
433.09 150.7
433.56 152.56
433.73 153.22
434.38 155.77
434.75 157.26
435.15 158.82
394.42 50.55
435.38 159.81
435.80 161.5
436.10 162.68
436.43 164.04
3694; butyl propanoate; 00750