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)
305.21 39.85
311.59 51.81
345.26 169.24
345.47 170.37
345.84 171.92
345.96 173.2
312.76 53.53
313.38 54.58
313.74 55.9
314.18 57.49
314.88 58.59
315.56 60.05
316.06 61.43
316.57 62.5
317.05 63.9
305.85 41.28
318.34 66.51
318.69 67.81
319.37 69.23
319.93 70.45
320.11 71.01
320.34 71.9
320.65 73.35
321.34 74.58
321.46 75.27
321.72 76.13
306.84 42.46
322.07 77.22
322.36 77.87
322.62 78.83
323.07 80.15
323.49 81.23
324.29 82.59
324.58 83.84
324.95 85.23
325.33 86.76
325.71 87.86
307.84 44.04
326.25 89.23
326.63 90.98
327.08 92.06
327.54 93.46
328.00 94.82
328.17 96.1
328.96 97.67
329.38 99.14
329.55 100.18
329.86 101.32
308.13 45.37
330.09 102.6
330.43 104.14
330.97 105.19
331.43 106.75
331.76 107.92
332.06 109.42
332.52 110.71
332.77 112.16
333.10 113.39
333.60 114.47
308.75 46.97
333.94 115.87
334.06 117.43
334.27 118.52
334.73 120.12
335.06 121.46
335.23 122.57
335.73 123.95
336.07 125.35
336.48 126.88
336.86 127.85
309.72 48.14
337.19 129.37
337.53 130.87
337.78 131.93
337.90 133.48
338.15 134.72
338.66 136.16
338.82 137.37
339.07 138.56
339.41 140.07
339.66 141.45
310.17 49.41
339.95 142.53
340.33 144.04
340.49 145.51
340.95 146.43
341.08 147.88
341.45 149.13
341.79 150.58
342.00 151.93
342.37 153.34
342.46 154.61
311.19 50.42
342.85 155.92
343.21 157.52
343.36 158.57
343.46 160.01
343.67 161.1
344.09 162.7
344.46 164.2
344.67 165.28
344.88 166.78
345.05 168.02
881; methyl acetate; 00022