化工原理-精馏塔-逐板法计算理论塔板数的计算

R/(R+1)Xd/(R+1)Xf Xd Xw

0.8240325750.1742077510.650.990.01

X Y

0.985328950.99

0.9797187520.986150902

0.9730074110.981527917

0.9650170110.975997553

0.955557640.969413203

0.944434210.961618373

0.9314568380.952452304

0.9164552420.941758528

0.8992970810.929396724

0.8799093570.91525784

0.8583008570.899281724

0.8345823770.881475616

0.808980550.861930816

0.7818408990.840834076

0.7536168280.81847012

0.7248436370.795212566

0.6960999210.771502519

0.6679619220.747816761

该条件下进料位置＜0.6409582630.724630133

0.6127737850.699938975

0.5783946060.669119868

0.5376169660.631526992

0.4908258030.58693754

0.4391319170.535772433

0.3843599440.479246305

0.3288380960.419354358

0.2750236940.358642439

0.2250837370.299797575

0.1805749870.24518933

0.1423132110.196519991

0.1104291320.154681581

0.0845413560.119817042

0.0639621620.091509328

0.0478763550.069006432

0.0354676680.051416957

0.025*******.03784833

0.0188138510.027487587

0.0134068890.019637748

0.0093525410.013725353

0.0063225810.009292013

0.0042161260.009145654

0.0027456980.005966291

0.001722260.003746911

0.0010113860.002202192

0.0005183170.00112924

0.0001766560.000385031

-5.9928E-05-0.000130652

R a q提馏段斜率提馏段截距

4.68287 1.474061 1.093478-0.000934785