In this work, the extractive distillation with heat integration process is extended to separate the pressure-insensitive benzene-cyclohexane azeotrope by using furfural as the entrainer. The optimal design of extractive distillation process is established to achieve minimum energy requirement using the multi-objective genetic algorithm, and the results show that energy saving for this heat integration process is 15.7%. Finally, the control design is performed to investigate the system’s dynamic ... 

【文章來源】：China Petroleum Processing & Petrochemical Technology. 2016,18(04)SCI

【文章頁數(shù)】：11 頁

【文章目錄】：
1 Introduction
2 Steady-State Design
    2.1 Process design
    2.2 Sensitivity analysis
    2.3 Optimization of extractive distillation process
3 Control System Design
    3.1 Basic control structure for the extractive distilla-tion(CS1)
    3.2 Improved control structure with the QR/F ratio and S/F ratio(CS2)
    3.3 Control structure with pressure-compensated temperature(CS3)
4 Conclusions
Nomenclature


【參考文獻(xiàn)】：
期刊論文
[1]Design and Control of Self-Heat Recuperative Distillation Process for Separation of Close-Boiling Mixtures: n-Butanol and iso-Butanol[J]. Li Lumin,Liu Yuliang,Zhai Jian,Sun Lanyi,Tian Yuanyu.  China Petroleum Processing & Petrochemical Technology. 2015(04)
[2]Considering Process Nonlinearity in Dual-Point Composition Control of a High-Purity Ideal Heat Integrated Distillation Column[J]. 黃克謹(jǐn),中巖勝,高松武一郎.  Chinese Journal of Chemical Engineering. 2001(01)



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