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)
405.54 40.28
414.21 52.27
414.92 53.34
415.87 54.86
416.72 56.21
417.51 57.51
418.27 58.78
418.98 60.01
419.74 61.31
420.59 62.83
421.26 64.02
406.59 41.53
422.07 65.51
422.76 66.81
423.35 67.91
424.29 69.74
424.66 70.42
425.59 72.31
426.07 73.25
426.78 74.67
427.43 76.02
428.05 77.34
407.56 42.86
428.69 78.82
429.28 79.99
430.02 81.71
430.48 82.77
431.04 84.03
431.70 85.54
432.27 86.67
432.82 87.95
433.42 89.55
433.90 90.72
408.56 44.16
434.46 91.87
435.06 93.35
435.61 94.7
436.09 96.15
436.56 97.3
437.11 98.75
437.66 100.18
438.09 101.32
438.67 102.63
439.18 104.0
409.28 45.06
439.66 105.5
440.16 106.67
440.68 108.31
441.11 109.48
441.60 110.68
442.01 112.07
442.53 113.34
442.93 114.71
443.44 116.0
443.86 117.43
410.43 46.65
444.34 118.65
444.78 120.03
445.21 121.28
445.62 122.76
446.04 124.03
446.47 125.37
446.87 126.64
447.33 128.0
447.74 129.33
448.18 130.73
411.38 48.06
448.54 132.01
448.97 133.41
449.36 134.68
449.75 135.99
450.15 137.35
450.55 138.69
450.94 140.07
451.29 141.21
451.71 142.69
452.07 143.97
412.43 49.58
452.55 145.69
452.88 146.84
453.25 148.17
453.58 149.33
453.95 150.73
454.34 152.16
454.65 153.29
455.02 154.65
455.37 155.97
455.71 157.25
413.11 50.53
456.09 158.69
456.42 159.94
456.79 161.37
457.13 162.68
457.47 164.01
2420; butyl butanoate; 00752