图解法求理论板数程序
平衡线阶梯线精馏进料序号x y xt yt X Y X
10.89430.89430.83260.83260.00000.27750.3414
20.74700.7815#NAME?0.83260.83260.83260.3414
30.67600.7385#NAME?#NAME?α1α0φ1
40.57320.6840#NAME?#NAME?0.66670.277506110408
50.52000.6599#NAME?#NAME?
60.50800.6560#NAME?#NAME?
70.39700.6120#NAME?#NAME?
80.32700.5830#NAME?#NAME?
90.26100.5580#NAME?#NAME?
100.23400.5450#NAME?#NAME?
110.16600.5090#NAME?#NAME?
120.12400.4700#NAME?#NAME?
130.09670.4375#NAME?#NAME?
140.07200.3890#NAME?#NAME?
150.01900.1700#NAME?#NAME?
160.00000.0000#NAME?#NAME?
17#NAME?#NAME?
18#NAME?#NAME?
19#NAME?#NAME?
20#NAME?#NAME?
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011
Y X Y xD 0.83260.34140.01610.0161xF 0.34140.5051330.34140.505133xW 0.0161φ0γ1γ0R 206110408 1.5033-0.0081q 1
g 0.277533
_xd 0.3414J 0.277533_yd 0.505133提馏进料