精馏塔理论板数计算程序

来源：意榕旅游网

平衡线图解法求理论板数程序阶梯线精馏进料序号x1020.001730.003540.012350.014160.019870.025880.03390.0357100.0525110.074120.0872130.1079140.1289150.1635160.1912170.2327180.2684190.2942200.35240.40210.45430.50220.56280.62430.71730.78980.82310.84260.85740.8720.91850.92950.9380.98851

yxtytXYX00.985

0.9850.00000.42600.44200.0125#NAME?0.9850.9850.9850.4420.025#NAME?#NAME?α1α0φ10.0889#NAME?#NAME?0.56750.4260061104080.0975#NAME?#NAME?0.1214#NAME?#NAME?0.1589#NAME?#NAME?0.1882#NAME?#NAME?0.2145#NAME?#NAME?0.2746#NAME?#NAME?0.356#NAME?#NAME?0.395#NAME?#NAME?0.44#NAME?#NAME?0.4776#NAME?#NAME?0.537#NAME?#NAME?0.5724#NAME?#NAME?0.6162#NAME?#NAME?0.6483#NAME?#NAME?0.6658#NAME?#NAME?0.7044#NAME?#NAME?0.7341#NAME?#NAME?0.7595#NAME?#NAME?0.7853#NAME?#NAME?0.8123#NAME?#NAME?0.835#NAME?#NAME?0.8773#NAME?#NAME?0.9098#NAME?#NAME?0.9225#NAME?#NAME?0.93#NAME?#NAME?0.9385#NAME?#NAME?0.9422#NAME?#NAME?0.9638#NAME?#NAME?0.9682#NAME?#NAME?0.9712#NAME?#NAME?0.9947#NAME?#NAME?1

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#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?#NAME?

进料YxD0.44200.00560.0056xF0.6768620.4420.676862xWφ0γ1γ0R061104031.5382-0.0030qX提馏Y01

010.9850.4420.00561.312

1_xd0.442_yd0.676862

g0.426038J0.426038

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