Simultaneous synthesis of work exchange networks with heat integration

被引:54
|
作者
Onishi, Viviani C. [1 ,2 ,3 ]
Ravagnani, Mauro A. S. S. [1 ]
Caballero, Jose A. [2 ]
机构
[1] Univ Estadual Maringa, Dept Chem Engn, BR-87020900 Maringa, Parana, Brazil
[2] Univ Alicante, Dept Chem Engn, E-03080 Alicante, Spain
[3] Minist Educ Brazil, CAPES Fdn, BR-7004020 Brasilia, DF, Brazil
关键词
Optimization; Mixed integer nonlinear programming (MINLP); Work exchange network (WEN); Heat exchanger network (HEN); Heat integration; Pressure recovery; OF-THE-ART; SIMULTANEOUS-OPTIMIZATION; ENTROPY GENERATION; RETROFIT DESIGN; MINLP SYNTHESIS; STATE; GRASSROOT;
D O I
10.1016/j.ces.2014.03.018
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The optimal integration of work and its interaction with heat can represent large energy savings in industrial plants. This paper introduces a new optimization model for the simultaneous synthesis of work exchange networks (WENs), with heat integration for the optimal pressure recovery of process gaseous streams. The proposed approach for the WEN synthesis is analogous to the well-known problem of synthesis of heat exchanger networks (HENs). Thus, there is work exchange between high-pressure (HP) and low-pressure (LP) streams, achieved by pressure manipulation equipment running on common axes. The model allows the use of several units of single-shaft-turbine-compressor (SSTC), as well as stand-alone compressors, turbines and valves. Helper motors and generators are used to respond to any demand and excess of energy. Moreover, between the WEN stages the streams are sent to the HEN to promote thermal recovery, aiming to enhance the work integration. A multi-stage superstructure is proposed to represent the process. The WEN superstructure is optimized in a mixed-integer nonlinear programming (MINLP) formulation and solved with the GAMS software, with the goal of minimizing the total annualized cost. Three examples are conducted to verify the accuracy of the proposed method. In all case studies, the heat integration between WEN stages is essential to improve the pressure recovery, and to reduce the total costs involved in the process. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:87 / 107
页数:21
相关论文
共 50 条
  • [31] Synthesis of optimal chemical reactor networks with simultaneous mass integration
    Lakshmanan, A
    Biegler, LT
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (12) : 4523 - 4536
  • [32] An MILP model for simultaneous mass allocation and heat exchange networks design
    Ghazouani, Sami
    Zoughaib, Assaad
    Le Bourdiec, Solene
    CHEMICAL ENGINEERING SCIENCE, 2017, 158 : 411 - 428
  • [33] Simultaneous synthesis of flexible heat-exchange networks with uncertain source-stream temperatures and flow rates
    Chen, CL
    Hung, PS
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (18) : 5916 - 5928
  • [34] Simultaneous Utility and Heat Exchanger Area Targeting for Integrated Process Synthesis and Heat Integration
    Kong, Lingxun
    Wu, Yaqing
    Maravelias, Christos T.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2017, 56 (41) : 11847 - 11859
  • [35] A new framework for work and heat exchange network synthesis and optimization
    Pavao, Leandro V.
    Costa, Caliane B. B.
    Ravagnani, Mauro A. S. S.
    ENERGY CONVERSION AND MANAGEMENT, 2019, 183 : 617 - 632
  • [36] Framework for work-heat exchange network synthesis (WHENS)
    Nair, Sajitha K.
    Rao, Harsha Nagesh
    Karimi, Iftekhar A.
    AICHE JOURNAL, 2018, 64 (07) : 2472 - 2485
  • [37] Simultaneous heat integration and the synthesis of biogas processes from animal waste
    Drobez, Rozalija
    Pintaric, Zorka Novak
    Pahor, Bojan
    Kravanja, Zdravko
    ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, 2011, 6 (05) : 734 - 749
  • [38] Simultaneous Process Synthesis, Heat and Power Integration in a Sustainable Integrated Biorefinery
    Ng, Rex T. L.
    Tay, Douglas H. S.
    Ng, Denny K. S.
    ENERGY & FUELS, 2012, 26 (12) : 7316 - 7330
  • [39] Synthesis of new distillation systems by simultaneous thermal coupling and heat integration
    Rong, BG
    Turunen, I
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (11) : 3830 - 3842
  • [40] An Optimisation-based Framework for Simultaneous Process Synthesis and Heat Integration
    Kong, Qingyuan
    Shah, Nilay
    27TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, PT A, 2017, 40A : 619 - 624