根据α=2.546
x y 0.94870.94870.94870.94870.94870.948690.8789660.948690.8789660.948690.7906070.9057760.8789660.9057760.6923430.85140.7906070.9057760.5977270.7909280.7906070.85140.5184540.7327010.6923430.85140.4594160.6839160.6923430.7909280.4191940.6475850.5977270.7909280.3930790.622491X F =0.41960.5977270.7327010.3549290.5834820.5184540.7327010.3039730.5264930.5184540.6839160.2434820.4503750.4594160.6839160.1809640.3600140.4594160.6475850.1249530.2666250.4191940.6475850.0808410.1829550.4191940.6224910.0494960.117060.3930790.6224910.0288160.0702380.3930790.5834820.0158320.0393460.3549290.5834820.0079320.019950.3549290.5264930.0032170.008149x w =0.0075
0.3039730.5264930.3039730.4503750.94870.94870.2434820.45037500.364885
0.2434820.3600140.1809640.3600140.00750.00750.1809640.2666250.41960.623090.1249530.2666250.1249530.182955000.0808410.18295511
0.0808410.117060.0494960.117060.0494960.0702380.0288160.0702380.0288160.0393460.0158320.0393460.0158320.019950.0079320.019950.0079320.0081490.0032170.008149
精馏段操作线方程:提馏段操作线方程:y=0.6154x+0.36487y=1.4938x-0.0037溜出液，釜液中的组成成分为x D =0.9487,x w =0.0075平衡线方程:y=2.546x/(1+1.54
精馏段直线
提馏段直线全回流直线
精馏段有6块板提馏段有13快板
+1.546x)
x=y/(2.546-1.546y)
00
0.010.025
0.030.0711
0.050.112
0.10.208
0.150.294
0.20.372
0.250.442
0.30.507
0.350.566
0.40.619
0.450.667
0.50.713
0.550.755
0.60.791
0.650.825
0.70.857
0.750.885
0.80.912
0.850.936
0.90.959
0.950.98
0.970.988
0.990.9961
11