Multi-objective Bonobo optimisers of industrial low-density polyethylene reactor

被引:0
|
作者
Rohman, Fakhrony Sholahudin [1 ]
Alwi, Sharifah Rafidah Wan [1 ,2 ]
Muhammad, Dinie [2 ]
Zahan, Khairul Azly [3 ]
Murat, Muhamad Nazri [4 ]
Azmi, Ashraf [5 ]
机构
[1] Univ Teknol Malaysia, Res Inst Sustainable Environm RISE, Proc Syst Engn Ctr UTM PROSPECT, Johor Baharu 81310, Malaysia
[2] Univ Teknol Malaysia, Fac Engn, Sch Chem & Energy Engn, UTM, Johor Baharu 81310, Johor, Malaysia
[3] Univ Tun Hussein Onn Malaysia, Fac Engn Technol, Batu Pahat 86400, Johor, Malaysia
[4] Univ Sains Malaysia, Sch Chem Engn, Engn Campus, Nibong Tebal 14700, Penang, Malaysia
[5] Univ Teknol MARA, Coll Engn, Sch Chem Engn, Shah Alam 40450, Selangor, Malaysia
来源
CHEMICAL PRODUCT AND PROCESS MODELING | 2024年 / 19卷 / 04期
关键词
low-density polyethylene; multi-objective optimization; tubular reactor; Bonobo optimizer; POLYMERIZATION; OPTIMIZATION; ETHYLENE;
D O I
10.1515/cppm-2024-0023
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A multi-objective optimization (MOO) technique to produce a low-density polyethylene (LDPE) is applied to address these two problems: increasing conversion and reducing operating cost (as the first optimization problem, P1) and increasing productivity and reducing operating cost (as the second optimization problem, P2). ASPEN Plus software was utilized for the model-based optimization by executing the MOO algorithm using the tubular reactor model. The multi-objective optimization of multi-objective Bonobo optimisers (MOBO-I, MOBO-II and MOBO-III) are utilised to solve the optimization problem. The performance matrices, including hypervolume, pure diversity, and distance, are used to decide on the best MOO method. An inequality constraint was introduced on the temperature of the reactor to prevent run-away. According to the findings of the study, the MOBO-II for Problems 1 and 2 was the most effective MOO strategy. The reason is that the solution set found represents the most accurate, diversified, and acceptable distribution points alongside the Pareto Front (PF) in terms of homogeneity. The minimum operating cost, the maximum conversion and productivity obtained by MOBO-II are Mil. RM/year 114.3, 31.45 %, Mil. RM/year 545.3, respectively.
引用
收藏
页码:631 / 652
页数:22
相关论文
共 50 条
  • [41] Low-density polyethylene homopolymer
    Townsend, P
    MODERN PLASTICS, 1996, 73 (02): : 66 - 66
  • [42] LOW-DENSITY POLYETHYLENE (LDPE)
    GLASER, R
    KUNSTSTOFFE-GERMAN PLASTICS, 1980, 70 (10): : 600 - 602
  • [43] Pyrolysis of Low-Density Polyethylene
    Zattini, Giorgio
    Leonardi, Chiara
    Mazzocchetti, Laura
    Cavazzoni, Massimo
    Montanari, Ivan
    Tosi, Cristian
    Benelli, Tiziana
    Giorgini, Loris
    SUSTAINABLE DESIGN AND MANUFACTURING 2017, 2017, 68 : 480 - 490
  • [44] LOW-DENSITY POLYETHYLENE PROCESSING
    FALKIEWICZ, S
    BEK, T
    PRZEMYSL CHEMICZNY, 1987, 66 (04): : 190 - 193
  • [45] A NEW LOW-DENSITY POLYETHYLENE
    LEVETT, CT
    PRITCHAR.JE
    MARTINOV.RJ
    SPE JOURNAL, 1970, 26 (06): : 40 - &
  • [46] BIODEGRADATION OF LOW-DENSITY POLYETHYLENE
    NYKVIST, NB
    PLASTICS & POLYMERS, 1974, 42 (161): : 195 - 199
  • [47] Linear low-density polyethylene
    Czaja, K
    Bialek, M
    POLIMERY, 2002, 47 (10) : 685 - 693
  • [48] Crystallization of low-density polyethylene- and linear low-density polyethylene-rich blends
    Drummond, KM
    Hopewell, JL
    Shanks, RA
    JOURNAL OF APPLIED POLYMER SCIENCE, 2000, 78 (05) : 1009 - 1016
  • [49] Physical properties, reactor modeling, and polymerization kinetics in the low-density polyethylene tubular reactor process
    Bokis, CP
    Ramanathan, S
    Franjione, J
    Buchelli, A
    Call, ML
    Brown, AL
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (05) : 1017 - 1030
  • [50] Multi-objective reactor network synthesis for industrial mass transfer limited processes
    Neves, Filipe
    Silva, Dulce
    Oliveira, Nuno
    Mendes, Fernando
    16TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING AND 9TH INTERNATIONAL SYMPOSIUM ON PROCESS SYSTEMS ENGINEERING, 2006, 21 : 1027 - 1032