Excess Properties and Isobaric Vapor-Liquid Equilibria for Binary Mixtures of Methyl Esters + tert-Butanol Ortega, J.; Espiau, F.; Postigo, M.; Journal of Chemical & Engineering Data 2004, 49, 1602-1612
Data
T (K) P (kPa)
325.88 40.08
333.19 53.37
334.04 54.63
334.49 55.93
335.63 57.49
335.97 58.57
336.70 60.05
337.50 61.5
338.06 62.73
338.52 64.17
339.43 66.58
327.07 42.57
339.71 67.89
340.73 69.17
341.07 70.53
341.52 71.89
341.72 72.42
342.35 73.37
342.60 75.37
342.88 75.83
343.25 75.91
343.95 77.99
328.03 44.13
344.15 78.43
344.25 78.74
344.75 79.89
345.40 82.35
345.65 82.59
346.32 84.18
346.57 85.43
346.65 86.74
347.23 87.87
347.40 88.1
329.00 45.29
348.15 90.74
348.73 91.95
348.98 93.23
349.23 94.6
349.73 96.03
350.23 97.26
350.59 98.7
350.99 100.0
351.65 101.32
352.23 102.75
329.68 46.72
352.40 103.87
352.82 105.43
352.90 106.58
353.73 107.82
353.82 109.39
354.15 110.78
354.57 112.07
354.82 113.15
355.65 114.82
355.74 115.9
330.24 47.97
355.82 117.13
356.32 118.57
356.90 120.15
357.15 121.17
357.39 122.81
357.90 123.81
358.24 124.65
358.48 126.73
358.65 127.87
358.98 129.37
330.70 49.34
359.32 130.43
359.48 130.89
359.98 133.25
360.40 134.57
360.57 135.81
361.08 137.35
361.40 138.56
361.73 140.0
361.90 141.21
362.44 142.57
332.00 50.58
362.57 144.11
363.07 145.35
363.40 146.48
363.73 148.09
363.91 149.39
364.40 151.04
364.57 152.48
364.90 153.26
364.99 154.82
365.38 156.06
332.74 51.89
365.48 156.17
365.82 158.49
365.90 159.73
366.15 160.57
366.57 162.57
366.65 163.38
367.15 165.17
367.40 166.74
367.82 167.89
2720; methyl propanoate; 00830