过程强化作业汇总

化工过程强化技术作业 Assign 3 Boiling point ROM Calculation MATLAB编程代码如下 function gairanawi 11 sonT 1IB; 2Me; 3MTBE x[0. 2, 0. 5, 0. 3]; v[99. 33, 44. 44, 118. 8]; A [0, 169. 9953, -60.1085; 2576. 8532, 0, 1483. 2478; 271.5669, -406. 3902, 01; vv/l 000000.0; msizeA, 2; for il ro for jl m 1 anandai jvj/vi*exp-l*Ai, j/l. 98721*T; end end il ； while i4., sigroal ix*lainrndai,; sigma2ix* 1 aininda. i; sigina3x*1 airanda1, lairanda2, lammda3, ; Ingairanail-sigmal i-sigma2i/sigma3; gairanaiexplngairanai; iil; end function pastatoineT atoineA[20. 64556, 23. 49989, 20. 71616]; atoineB[-2125. 74886, -3643. 31362,-2571. 58460]; atoineC[-33.160, -33. 434, -48. 406]; il while i4 pastiexpat oineAiat oineBi/TatoineCi; iil; end function G二GT x [0. 2, 0. 5, 0. 3]; il； p101325; while i4 kipast i*gaimai/p; i二i1; end Glogk*xJ ; 程序运行结果 1 Command Window 11300 T2350; T3TlT2/2 while absGT30. 001 if GT30 11300T2T3T3TlT2/2 else T1T3T2T2T3TlT2/2 end end T3 T3 304.3945 Setup Components Properties 申也 由亡J 由仁］ 亩包 iQ In O o 弱 a Specifications Property s Estimation Molecular Structure Parameters Data Analysis Prop-Sets Advanced Flowsheet Sections | Referenced | Base Petroleum calculation options Free-water |S STEAM-TA Modify property models Vapor EOS Data set Water solubility Liquid gamma Data set |esig |gmrendn』 庄］园Streams 白Blocks s-a bi Electrolyte calculation options Chemistry ID R Use true-components HLMX86 |VLMX01 3 Liquid enthalpy Liquid volume Pointing correction p Heat of mixing 沸点T304C Assign 5 Investigate Influence of Activity Coefficient Model Parameters 选取三元体系water methanol ethanol 334 用Aspen进行程序程序在打包附件模拟 。Specifications n 回亟厂n。同“Illg ,| i 口|制回 Hcurves Dynamic Block Options EO Variables UC ♦ 通过不断变换红色圈内的方法得到不同的结果 NRTL模型 *s latysis j PT-1 Q Results Summary n Status earns n vergence Results PRES TOTAL PBUB TOTAL PDEW TOTAL TBUB TOTAL TDEW ▼ ▼ ▼ cJ [cJ 1 0.1285547 0.1034123 74.3167061 77.5460061 Generic analysis results Wilson 模型 nesuns Analysis Q PT-1 Q Results ams ks ults Summary Run Status Streams Convergence PRES TOTAL PBUB TOTAL PDEW TOTAL TBUB TOTAL TDEW | atm | atm | atm C [c 1 0.1286767 0.1033407 74.2532061 77.5764061 Generic analysis results SRK模型 ysis PT-1 n Results immary Status ams mergence 统计结果 Results PRES TOTAL PBUB TOTAL PDEW TOTAL TBUB TOTAL TDEW ▼ ▼ |c3 EZ ， 1 0.143864 0.1381463 71.1546061 71.8554061 Generic analysis results NRTL SRK WILSON BOILING POINTS/C 74.317 71.154 74.253 Assign 6 Build EQ Model and Simulate the Reactive Distillation Process of Methyl Acetate ation