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)
369.66 40.29
377.33 52.07
378.11 53.38
378.59 54.37
379.52 56.01
380.35 57.3
381.07 58.69
381.84 60.07
382.55 61.43
383.04 62.61
383.86 64.03
370.49 41.48
384.46 65.43
385.13 66.73
385.64 67.7
386.53 69.74
387.08 70.74
387.58 72.02
388.24 73.29
388.78 74.7
389.46 76.06
390.04 77.65
371.19 42.64
390.60 78.73
391.29 80.42
391.73 81.38
392.35 82.99
392.55 83.42
393.89 86.83
394.26 87.98
394.68 89.08
395.39 90.72
395.76 91.92
372.26 44.02
396.37 93.38
396.86 94.72
397.26 96.04
397.70 97.26
398.30 98.8
398.75 100.02
399.18 101.32
399.56 102.59
400.13 104.16
401.02 106.99
373.05 45.37
401.45 108.04
401.76 109.22
402.25 110.79
402.73 112.04
403.02 113.1
403.56 114.64
403.97 116.02
404.32 117.33
404.70 118.57
405.20 120.05
373.83 46.58
405.59 121.55
405.99 122.71
406.47 124.36
406.72 125.41
407.04 126.49
407.47 128.01
407.84 129.32
408.31 130.79
408.66 132.03
408.96 133.33
374.87 48.12
409.37 134.61
409.70 136.01
410.13 137.57
410.36 138.47
410.86 140.29
411.08 141.19
411.53 142.69
411.88 144.17
412.24 145.56
412.59 146.81
375.76 49.58
412.90 148.01
413.19 149.35
413.61 150.84
413.93 152.16
414.27 153.49
414.48 154.57
414.80 155.86
415.25 157.54
415.49 158.72
415.75 159.8
376.36 50.55
416.19 161.46
416.51 162.9
416.74 164.01
1234; butyl ethanoate; 00080