A heuristic approach to design a cost-effective and low-CO2 emission synthesis in a heat exchanger network with crude oil distillation units

被引:9
作者
Xu, Yue [1 ]
Zhang, Lu [1 ]
Cui, Guomin [1 ]
Yang, Qiguo [1 ]
机构
[1] Univ Shanghai Sci & Technol, Sch Energy & Power Engn, 516 Jungong Rd, Shanghai 200093, Peoples R China
基金
中国国家自然科学基金;
关键词
Crude oil distillation units; Heat exchanger network synthesis; Compulsive evolution; RWCE; Carbon emissions; Multi-objective optimization; MULTIOBJECTIVE OPTIMIZATION; CO2; EMISSIONS; ENERGY; ALGORITHM; PINCH; FORMULATION; GENERATION;
D O I
10.1016/j.energy.2023.126972
中图分类号
O414.1 [热力学];
学科分类号
摘要
This paper presents a tradeoff grassroots design of cost-effective and low-CO2 emissions heat exchanger networks for crude oil distillation units (CDUs) to address high energy consumption in CDUs. To reduce the impact of the objective's magnitude on the optimization searching direction, a normalization process handling the objectives to the dimensionless indexes to assess the performance of CDU is presented. An originally designed random walk algorithm with compulsive evolution (RWCE) and a special superstructure nodes-based non-structural model (NNM) is adopted for the multi-objective optimization problem. The comparison analysis shows that the pro-posed model and the heuristic algorithm are robust in solving the global optimization problem. In addition, aiming to investigate the evolution mode of utilities in RWCE, an active evolution strategy of utilities (RWCE-AU) is proposed to promote structural evolution by altering the heat loads of utilities by a certain probability. Finally, several industrial CDU cases are optimized by RWCE and RWCE-AU in this work. The continuous improvement solutions have highlighted that the RWCE could yield a better optimal total annual cost (TAC) compared to the reported initial case. Moreover, the RWCE-AU enhances the searching ability of RWCE and provides a better tradeoff between the economic benefits and the environmental impacts.
引用
收藏
页数:16
相关论文
共 54 条
[1]   Multiobjective optimal design of heat exchanger networks using new adaptations of the elitist nondominated sorting genetic algorithm, NSGA-II [J].
Agarwal, Aaditya ;
Gupta, Santosh K. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (10) :3489-3501
[2]  
Ahmad S, 1987, AICHE ANN M
[3]   Investigating the trade-off between operating revenue and CO2 emissions from crude oil distillation using a blend of two crudes [J].
Al-Mayyahi, Mohmmad A. ;
Hoadley, Andrew F. A. ;
Smith, Nicholas E. ;
Rangaiah, G. P. .
FUEL, 2011, 90 (12) :3577-3585
[4]   Retrofit of heat exchanger networks by graphical Pinch Analysis - A case study of a crude oil refinery in Kuwait [J].
Alhajri, Ibrahim H. ;
Gadalla, Mamdouh A. ;
Abdelaziz, Omar Y. ;
Ashour, Fatma H. .
CASE STUDIES IN THERMAL ENGINEERING, 2021, 26
[5]  
Alhammadi HY, 2008, COMPUT-AIDED CHEM EN, V25, P169
[6]   AN MILP FORMULATION FOR HEAT-INTEGRATED DISTILLATION SEQUENCE SYNTHESIS [J].
ANDRECOVICH, MJ ;
WESTERBERG, AW .
AICHE JOURNAL, 1985, 31 (09) :1461-1474
[7]   Exceeding Pinch limits by process configuration of an existing modern crude oil distillation unit - A case study from refining industry [J].
Bayomie, Omar S. ;
Abdelaziz, Omar Y. ;
Gadalla, Mamdouh A. .
JOURNAL OF CLEANER PRODUCTION, 2019, 231 :1050-1058
[8]  
Biswarup Mondal, 2020, CHEM ENG PROCESS, V176
[9]  
Chen L, 2008, THESIS U MACHESTER M
[10]   Coupling design of interunit heat integration in an industrial crude distillation plant using pinch analysis [J].
Cui, Chengtian ;
Sun, Jinsheng .
APPLIED THERMAL ENGINEERING, 2017, 117 :145-154