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)
351.93 39.8
359.21 52.07
360.03 53.37
360.58 54.63
361.30 56.03
362.07 57.3
362.78 58.74
363.41 60.03
363.94 61.37
364.53 62.61
365.28 64.01
352.90 41.34
365.82 65.43
366.39 66.7
366.97 67.81
367.70 69.73
368.21 70.69
368.77 72.02
369.20 73.27
369.77 74.67
370.39 76.02
371.01 77.77
353.61 42.56
371.35 78.69
371.83 79.9
372.32 81.22
372.98 82.86
373.23 83.42
374.00 85.54
374.46 86.83
374.80 87.98
375.42 89.51
375.83 90.7
354.63 44.01
376.18 91.92
376.53 92.98
377.23 94.84
377.54 95.98
377.91 97.12
378.53 98.83
378.91 100.02
379.33 101.32
379.63 102.5
380.17 104.07
355.48 45.4
380.63 105.51
381.03 106.83
381.30 107.92
381.70 109.24
382.22 110.8
382.51 112.0
382.90 113.36
383.32 114.6
383.66 116.0
384.03 117.36
356.16 46.69
384.40 118.6
384.83 120.01
385.23 121.48
385.51 122.69
385.84 123.93
386.31 125.48
386.58 126.69
386.93 128.01
387.32 129.35
387.69 130.79
357.06 48.04
387.92 131.85
388.37 133.41
388.60 134.53
389.06 136.15
389.38 137.47
389.73 138.88
390.04 140.17
390.26 141.21
390.58 142.57
390.85 143.71
357.83 49.58
391.31 145.47
391.62 146.81
391.84 147.92
392.24 149.45
392.42 150.41
392.86 152.16
393.36 154.53
393.76 156.14
393.97 157.28
394.32 158.68
358.51 50.55
394.63 160.14
394.90 161.36
395.19 162.84
395.48 164.08
1803; butyl formate; 00609