Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols Gierycz, P.; Kosowski, A.; Swietlik, R.; Journal of Chemical & Engineering Data 2009, 54, 2996-3001
Data
T (K) P (kPa)
314.470 6.08
322.030 9.8
366.180 79.95
366.632 81.35
367.043 82.63
367.470 84.03
367.885 85.39
368.270 86.71
368.680 88.05
369.080 89.41
369.430 90.67
369.790 91.91
322.680 10.19
370.195 93.33
370.555 94.44
370.940 96.0
371.320 97.35
371.650 98.59
323.150 10.48
323.410 10.64
324.050 11.04
324.720 11.47
325.270 11.84
325.920 12.31
326.660 12.81
327.320 13.16
315.360 6.43
328.280 14.03
329.050 14.61
329.910 15.31
330.490 15.79
331.110 16.31
331.580 16.71
332.170 17.25
332.810 17.87
333.150 18.2
333.280 18.33
316.210 6.81
333.650 18.68
334.230 19.24
334.690 19.71
335.190 20.2
335.690 20.71
336.280 21.33
336.770 21.85
337.230 22.35
337.720 22.87
338.080 23.28
317.610 7.45
338.600 23.87
339.070 24.43
339.500 24.95
339.900 25.43
340.340 25.97
340.950 26.79
341.400 27.36
341.870 27.99
342.340 28.63
342.890 29.37
318.570 7.92
343.150 29.76
343.320 29.97
343.810 30.67
344.250 31.31
344.710 31.99
345.145 32.63
345.600 33.33
346.025 33.99
346.455 34.67
346.860 35.32
319.370 8.35
347.280 36.01
347.650 36.63
348.055 37.31
348.455 37.99
348.845 38.64
349.210 39.29
349.585 39.95
350.155 40.97
350.745 42.05
351.255 43.03
319.580 8.45
351.740 43.96
352.265 44.97
353.085 46.6
353.150 46.75
353.600 47.65
354.060 48.61
354.530 49.61
355.000 50.63
355.455 51.63
355.805 52.39
320.180 8.77
356.230 53.33
356.800 54.63
357.370 55.96
357.990 57.41
358.500 58.67
359.055 60.03
359.615 61.41
360.13 62.73
360.610 63.97
361.095 65.29
321.050 9.23
361.640 66.71
362.100 67.99
362.630 69.43
363.075 70.69
363.575 72.12
364.000 73.36
364.475 74.72
364.900 76.0
365.333 77.31
365.763 78.65
225; (RS)-2-butanol; 00120