Energy-Saving Optimal Design and Effective Control of Heat Integration-Extractive Dividing Wall Column for Separating Heterogeneous Mixture Methanol/Toluene/Water with Multiazeotropes

被引:76
作者
Yang, Ao [1 ]
Wei, Renxing [1 ]
Sun, Shirui [1 ]
Wei, Shun'an [1 ]
Shen, Weifeng [1 ]
Chien, I-Lung [2 ]
机构
[1] Chongqing Univ, Sch Chem & Chem Engn, Chongqing 400044, Peoples R China
[2] Natl Taiwan Univ, Dept Chem Engn, Taipei 10617, Taiwan
基金
中国国家自然科学基金;
关键词
DISTILLATION PROCESS; AZEOTROPIC DISTILLATION; THERMODYNAMIC INSIGHTS; DIMETHYL-SULFOXIDE; ENTRAINER; SYSTEM; OPTIMIZATION; METHANOL; WATER; DEHYDRATION;
D O I
10.1021/acs.iecr.8b00668
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
To the best of our knowledge, very few efforts have been investigated for separating heterogeneous mixtures methanol/toluene/water with multiazeotropes using extractive dividing-wall column (EDWC). In this work, we propose a systematic approach for the energy-efficient EDWC to achieve less capital cost and operating cost in separating heterogeneous multiazeotropes mixtures, which involves thermodynamic feasible insights via residue curve maps to find separation constraints, global optimization based on a proposed CPOM model, and a dynamic control through Aspen Dynamics simulator to better maintain product purities. An energy-saving EDWC with heat integration (HI-EDWC) flowsheet is then proposed to achieve the minimum total annualized cost (TAC). The computational results show that the TAC of the proposed HI-EDWC is significantly reduced by 15.14% compared with the optimal double-column extractive distillation with an additional decanter. Furthermore, an effective control strategy CS3 with a fixed reboiler duty-to-feed ratio and temperature/(S/F) cascade is proposed to better handle the methanol, toluene, and water product purities than basic control structures CSI and CS2 while feed flow rate and composition disturbances are introduced in the proposed HI-EDWC process.
引用
收藏
页码:8036 / 8056
页数:21
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