Adaptive superstructure for multiple-interconnection process synthesis: Eliminate unnecessary flowsheet predetermination to reduce complexity

被引:10
作者
Lyu, Hao [1 ]
Zhang, Xiaodong [1 ]
Cui, Chengtian [2 ]
Sun, Jinsheng [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300072, Peoples R China
[2] Nanjing Tech Univ, Inst Intelligent Mfg, Nanjing 211816, Peoples R China
关键词
Adaptive superstructure; Process synthesis; Side-stream distillation column; Hybrid double-effect distillation; THERMALLY COUPLED DISTILLATION; EXTRACTIVE DISTILLATION; DIFFERENTIAL EVOLUTION; HEAT INTEGRATION; OPTIMIZATION; SEPARATION; DESIGN; SEQUENCES; FRAMEWORK; SYSTEM;
D O I
10.1016/j.cep.2021.108731
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The integrated distillation configurations have an enormous number of alternative flowsheets leading to great challenges for process synthesis. The superstructure-based approach can be the countermeasure but it is difficult to solve the complex networks using rigorous models due to the nonconvexity and nonlinearity. Although stochastic algorithms can robustly find high-quality solutions for a single predefined flowsheet, the performance will still degrade when dealing with complex superstructure models. This paper introduces an adaptive strategy to determine the substructure branches of the superstructure, which can reduce the complexity of the superstructure models optimized by stochastic algorithms. The improved method selects the downstream flowsheet based on the calculation results of the upstream modules, instead of predefining the branches before the simulation. Thereby, stochastic algorithms could optimize the simplified superstructure model with fewer sequence variables more robustly and efficiently. A multiple-effect distillation system and a double side-stream distillation system separating aromatics are optimized as case studies. The results show that the improved method, compared with the conventional approach, could find the optimized side-stream design with 17.8% lower cost more robustly, and find the optimized multi-effect distillation design with 2.4% lower cost within the same iterations.
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页数:15
相关论文
共 48 条
  • [1] SYNTHESIS OF HEAT INTEGRATED NONSHARP DISTILLATION SEQUENCES
    AGGARWAL, A
    FLOUDAS, CA
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 1992, 16 (02) : 89 - 108
  • [2] Thermally coupled distillation with reduced number of intercolumn vapor transfers
    Agrawal, R
    [J]. AICHE JOURNAL, 2000, 46 (11) : 2198 - 2210
  • [3] More operable arrangements of fully thermally coupled distillation columns
    Agrawal, R
    Fidkowski, ZT
    [J]. AICHE JOURNAL, 1998, 44 (11) : 2565 - 2568
  • [4] A simulated annealing-based approach to the optimal synthesis of heat-integrated distillation sequences
    An Wei-zhong
    Yuan Xi-Gang
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2009, 33 (01) : 199 - 212
  • [5] Boonstra S., 2016, 23 INT WORKSH EUR GR
  • [6] Self-adapting control parameters in differential evolution: A comparative study on numerical benchmark problems
    Brest, Janez
    Greiner, Saso
    Boskovic, Borko
    Mernik, Marjan
    Zumer, Vijern
    [J]. IEEE TRANSACTIONS ON EVOLUTIONARY COMPUTATION, 2006, 10 (06) : 646 - 657
  • [7] Structural considerations and modeling in the synthesis of heat-integrated-thermally coupled distillation sequences
    Caballero, Jose A.
    Grossmann, Ignacio E.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (25) : 8454 - 8474
  • [8] Synthesis of Complex Thermally Coupled Distillation Systems Including Divided Wall Columns
    Caballero, Jose A.
    Grossmann, Ignacio E.
    [J]. AICHE JOURNAL, 2013, 59 (04) : 1139 - 1159
  • [9] COMPARISON OF ENERGY-CONSUMPTION IN 5 HEAT-INTEGRATED DISTILLATION CONFIGURATIONS
    CHIANG, TP
    LUYBEN, WL
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1983, 22 (02): : 175 - 179
  • [10] Process intensification in ternary distillation via comparative grassroots and retrofit designs: A case study of distilling an industrial multicomponent C6 alkane mixture in caprolactam processing
    Cui, Chengtian
    Zhang, Xiaodong
    Lyu, Hao
    Wang, Shaojing
    Sun, Jinsheng
    Qu, Yaping
    Wu, Wangcheng
    Bo, Cuimei
    Wong, David Shan-Hill
    Zhang, Quanling
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2021, 164