Dynamic simulation and operational optimization of dividing wall batch distillation columns based on rigorous models

IF 4.9 2区 工程技术 Q2 COMPUTER SCIENCE, INTERDISCIPLINARY APPLICATIONS
Computers & Chemical Engineering Pub Date : 2026-03-01 Epub Date: 2025-12-24 DOI:10.1016/j.compchemeng.2025.109542
Xing Qian , Jiayi Du , Gonghan Guo , Shengkun Jia , Chao Zhang
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引用次数: 0

Abstract

Batch distillation, as a widely applied separation technology, demonstrates significant advantages in small-scale, multi-component, and composition-variable separation tasks. Current research primarily focuses on two directions to enhance its overall performance, reduce energy consumption, and shorten separation time: development of novel process configurations and operational optimization. Among these, the dividing wall batch distillation column (DWBDC) remarkably improves separation efficiency of conventional batch distillation through its innovative batch dividing wall process intensification structure. However, as a highly nonlinear dynamic system, DWBDC presents considerable challenges in rigorous simulation and optimization, which is well worth further investigation. Bayesian optimization algorithms have gained extensive application in chemical engineering due to their efficient global search capability in recent years. This study innovatively applies Bayesian optimization to batch distillation processes, establishing an operational optimization framework based on this algorithm and implementing it in the optimal design of various batch distillation configurations. To systematically evaluate DWBDC's superiority, rigorous dynamic simulations were conducted on three configurations: conventional batch distillation column (BDC), middle vessel batch distillation column (MVBDC), and DWBDC, with corresponding concentration control systems developed. The research examined separation performances of these configurations for industrial waste solvents with different feed compositions (light-component-dominant, intermediate-component-dominant, and balanced light/intermediate-component feeds). Bayesian optimization was employed to optimize operational parameters for all three configurations, followed by comparative performance analysis under optimal conditions. Results demonstrate the superior performance of DWBDC in both operating time and economic efficiency, providing crucial theoretical foundations and practical guidance for industrial application of dividing wall batch distillation technology.
基于严格模型的分壁间歇精馏塔动态仿真及操作优化
间歇精馏作为一种广泛应用的分离技术,在小规模、多组分、多组分的分离任务中具有显著的优势。目前的研究主要集中在两个方向,以提高其整体性能,降低能耗,缩短分离时间:开发新的工艺配置和操作优化。其中,分壁间歇精馏塔(DWBDC)通过其创新的间歇分壁过程强化结构,显著提高了常规间歇精馏的分离效率。然而,作为一个高度非线性的动态系统,DWBDC在严格的仿真和优化方面面临着相当大的挑战,值得进一步研究。近年来,贝叶斯优化算法以其高效的全局搜索能力在化工领域得到了广泛的应用。本研究创新性地将贝叶斯优化应用于间歇精馏过程,建立了基于该算法的操作优化框架,并将其应用于间歇精馏的各种配置优化设计中。为了系统地评价DWBDC的优越性,对常规间歇精馏塔(BDC)、中间容器间歇精馏塔(MVBDC)和DWBDC三种配置进行了严格的动态仿真,并开发了相应的浓度控制系统。研究考察了这些构型对不同原料组成(轻组分为主、中间组分为主、轻/中间组分平衡)的工业废溶剂的分离性能。采用贝叶斯优化方法对三种构型的运行参数进行优化,并在最优条件下进行性能对比分析。结果表明,DWBDC在操作时间和经济效率方面均具有优越的性能,为分壁间歇精馏技术的工业应用提供了重要的理论基础和实践指导。
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来源期刊
Computers & Chemical Engineering
Computers & Chemical Engineering 工程技术-工程:化工
CiteScore
8.70
自引率
14.00%
发文量
374
审稿时长
70 days
期刊介绍: Computers & Chemical Engineering is primarily a journal of record for new developments in the application of computing and systems technology to chemical engineering problems.
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