控制理论与控制工程研究生毕业论文

控制理论与控制工程研究生毕业论文内容摘要：

. 9 Chapter 3 Deepening Internal Mass Integration ........................... 11 The Method of Deepening Internal Mass Integration ............................................ 11 Four Strategies ....................................................................................................... 11 A Sequential Procedure .......................................................................................... 13 Conclusion ............................................................................................................. 14 Chapter 4 A Hypothetical Quaternary Reactive Distillation System (A+B↔C+D )..................................................................................... 15 Process Description................................................................................................ 15 Steady State Model Description ............................................................................. 15 Effect of Deepening Internal Mass Integration ...................................................... 18 Influences of Physical Propoties and Operation Condition ................................... 24 Influences of Thermal Conditions of FB ............................................................. 24 Influences of the Amount of Catalyst Employed ................................................ 25 Conclusion ............................................................................................................. 27 目 录 VIII Chapter 5 A Hypothetical Ternary Reactive Distillation System(A+B↔ C) .............................................................................. 28 Process Description................................................................................................ 28 Steady State Model Description ............................................................................. 28 Effect of Deepening Internal Mass Integration ...................................................... 31 Influences of Physical Propoties and Operation Condition ................................... 34 Influences of Thermal Conditions of FA ............................................................. 34 Influences of the Amount of Catalyst Employed ................................................ 36 Conclusion ............................................................................................................. 37 Chapter 6 A Hypothetical Ternary Reactive Distillaiton System with a Heavy Reactant A (HK)↔B(LK)+C(IK) ............................ 38 Process Description................................................................................................ 38 Steady State Model Description ............................................................................. 38 Effect of Deepening Internal Mass Integration ...................................................... 40 Influences of Physical Propoties and Operation Condition ................................... 46 Influences of Thermal Conditions of FA ............................................................. 46 Influences of the Amount of Catalyst Employed ................................................ 47 Conclusion ............................................................................................................. 47 Chapter 7 A Hypothetical Ternary Reactive Distillation System with a Intermediate Reactant A(IK)↔B(LK)+C(HK) ..................... 48 Process Description................................................................................................ 48 Steady State Model Description ............................................................................. 48 Effect of Deepening Internal Mass Integration ...................................................... 50 Influences of Physical Propoties and Operation Condition ................................... 55 Influences of Thermal Conditions of FA ............................................................. 56 Influences of the Amount of Catalyst Employed ................................................ 56 Conclusion ............................................................................................................. 57 Chapter 8 Discussion of Deepening Internal Mass Integration ..... 58 Other Methods of Deepening Internal Mass Integration ....................................... 58 Application Ranges of Deepening Internal Mass Integration ................................ 58 北京化工大学硕士学位论文 IX Chapter 9 Conclusion and prospect .............................................. 61 Conclusion ............................................................................................................. 61 Prospect .................................................................................................................. 61 Literature Cited ............................................................................... 63 Acknowledgements........................................................................... 69 Papers Published .............................................................................. 70 Introduction of Author and Tutor .................................................... 71 符号说明 1 符 号 说 明 A 组分 Avp 气相压力常数 ， Pa B 组分 Bvp 气相压力常数 ， Pa K C 组分 D 组分 E 反应 活化能 ， kJ/kmol F 反应物进料流速 ， kmol/s H 塔板滞液量 kmol ΔHR 反应热 ， kJ/kmol ΔHV 汽化潜热 ， kJ/kmol K 某温度点反应速率 ， kmol/(s kmol) L 液相流速 ， kmol/s N 塔板数 P 塔内气压 ， Pa R 理想气体常数 ， kJ/(kmol K) R 净反应速率 ， kmol/s T 温度 ， K V 汽相流速 ， kmol/s x 液相组成 y 汽相组成 z 进料组成 希腊字母 α 预指数因子 δ Kronecker 函数 ε 误差 ν 反应化学当量系数 目 录 2 下标 A 组分 b 逆向反应 B 组分 bot 塔釜产品 C 组分 d 精馏 D 组分 f 正向反应 i 组分 j 塔板 m 进料板 r 精馏段 re。