Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing Ortega, J.; Espiau, F.; Postigo, M.; Journal of Chemical & Engineering Data 2003, 48, 916-924
Data
T (K) P (kPa)
332.30 37.4
338.37 49.27
338.86 50.27
339.50 51.81
340.08 53.17
340.59 54.25
341.17 55.83
341.63 56.78
342.18 58.37
342.68 59.61
343.13 60.61
333.03 38.69
343.70 62.3
344.13 63.27
344.68 64.99
345.06 65.81
345.49 67.05
346.11 69.05
346.51 70.21
346.83 71.11
347.28 72.45
347.68 73.43
333.45 39.34
348.20 75.35
348.54 76.17
348.90 77.42
349.34 78.76
349.74 80.07
350.10 81.3
350.53 82.71
350.90 83.96
351.33 85.66
351.67 86.64
334.60 41.37
352.05 88.15
352.45 89.39
352.80 90.67
353.13 92.07
353.50 93.39
353.81 94.63
354.18 95.95
354.51 97.04
354.85 98.36
355.23 100.07
335.29 42.93
355.50 100.88
355.58 101.32
355.83 102.22
356.22 103.92
356.52 105.27
356.86 106.62
357.15 107.71
357.45 109.12
357.77 110.47
358.06 111.51
335.87 43.85
358.35 112.83
358.68 114.36
358.96 115.48
359.27 117.0
359.84 119.53
360.13 120.87
360.46 122.36
360.64 123.08
360.97 124.73
361.26 126.15
336.43 45.01
361.47 126.96
361.73 128.2
362.02 129.63
362.54 132.15
362.75 133.36
363.03 134.71
363.08 134.81
363.56 137.4
363.82 138.8
364.09 140.03
337.17 46.69
364.33 141.29
364.66 142.96
365.09 145.34
365.27 146.36
365.62 148.18
366.10 150.66
366.51 153.08
366.81 154.69
367.08 156.16
367.49 158.58
337.80 48.06
367.83 160.39
368.23 162.82
1086; tert-butanol; 00347