A new approach to design heat-integrated reactive distillation process: Part 2. Role of additional variable in excess design

被引:0
|
作者
Teh, Irvy Ai Xia [1 ]
Lee, Hao-Yeh [2 ,3 ]
Kong, Zong Yang [1 ,4 ]
Putranto, Aditya [5 ]
Zheng, Jinchuan [6 ]
Sunarso, Jaka [1 ]
机构
[1] Swinburne Univ Technol, Res Ctr Sustainable Technol, Fac Engn Comp & Sci, Jalan Simpang Tiga, Kuching 93350, Sarawak, Malaysia
[2] Natl Taiwan Univ Sci & Technol, Dept Chem Engn, Taipei 10607, Taiwan
[3] Natl Taiwan Univ Sci & Technol, Proc Net Zero Res Ctr, Taipei 10607, Taiwan
[4] Sunway Univ, Sch Engn & Technol, 5 Jalan Univ, Bandar Sunway 47500, Selangor Darul, Malaysia
[5] Univ Surrey, Fac Engn & Phys Sci, Sch Chem & Chem Engn, Guildford GU2 7XH, Surrey, England
[6] Swinburne Univ Technol, Sch Sci Comp & Engn Technol, John St, Melbourne 3122, Australia
关键词
Process Intensification; Double effect; Energy savings; Hybrid configuration; Thermally coupled; THERMALLY COUPLED DISTILLATION; CONFIGURATION; ALTERNATIVES; SYSTEMS; COLUMN;
D O I
10.1016/j.seppur.2024.131330
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The purpose of this paper is to explore the possibility of extending a new perspective previously identified for neat design (DOI: 10.1016/j.seppur.2024.131201) to the excess design of reactive distillation (RD) configurations. In earlier research, we proposed to minimize the energy consumption of the RD column (RDC) prior to heat-integration (HI), instead of the conventional method of minimizing overall energy consumption, to achieve a more significant energy savings. This study extends the investigation to two specific configurations, i.e., excess design (1) RD and (2) thermally coupled reactive distillation (TCRD). The purpose of exploring such extension is because the excess design of RD is different from those of neat design due to the additional degree of freedom (DOF) available, such as the purity of recycled component. Our findings revealed that, minimizing the energy consumption of RDC results in higher energy savings for excess configurations. Post HI, the excess design RD and TCRD achieved energy savings of 27.65% and 27.55%, respectively, compared to the conventional RD base case. Furthermore, our study highlights the importance of considering XLLK-R as a design variable when performing process optimization for excess design.
引用
收藏
页数:16
相关论文
共 50 条
  • [21] Control structure design for parallel processes - Application to heat-integrated distillation
    Tsai, WH
    Huang, HP
    Yu, CC
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2005, 83 (A2): : 153 - 159
  • [22] Interaction between design and control of a heat-integrated distillation system with prefractionator
    Bildea, C.S.
    Dimian, A.C.
    Chemical Engineering Research and Design, 1999, 77 (07): : 597 - 608
  • [23] Reversibility Analysis for Design Optimization of an Internally Heat-Integrated Distillation Column
    Xu, Lianghua
    Yuan, Xigang
    Chen, Dawei
    Luo, Yiqing
    Yu, Kuotsung
    CHEMICAL ENGINEERING & TECHNOLOGY, 2013, 36 (07) : 1147 - 1156
  • [24] MODELING AND DESIGN METHOD FOR INTERNAL HEAT-INTEGRATED PACKED DISTILLATION COLUMN
    TAKAMATSU, T
    LUEPRASITSAKUL, V
    NAKAIWA, M
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1988, 21 (06) : 595 - 601
  • [25] Interaction between design and control of a heat-integrated distillation system with prefractionator
    Bildea, CS
    Dimian, AC
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 1999, 77 (A7): : 597 - 608
  • [26] Stability and multiplicity approach to the design of heat-integrated PFR
    Bildea, CS
    Dimian, AC
    AICHE JOURNAL, 1998, 44 (12) : 2703 - 2712
  • [27] Pinch analysis-based approach to conceptual design of internally heat-integrated distillation columns
    Gadalla, M
    Olujic, Z
    Sun, L
    De Rijke, A
    Jansens, PJ
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2005, 83 (A8): : 987 - 993
  • [28] Integrated Process Design and Control of Reactive Distillation Processes
    Mansouri, Seyed Soheil
    Sales-Cruz, Mauricio
    Huusom, Jakob Kjobsted
    Woodley, John M.
    Gani, Rafiqul
    IFAC PAPERSONLINE, 2015, 48 (08): : 1120 - 1125
  • [29] Interpreting design of an ideal heat-integrated distillation column through exergy analysis
    Huang, Kejin
    Matsuda, Keigo
    Iwakabe, Koichi
    Takamatsu, Takeichiro
    Nakaiwa, Masaru
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2006, 39 (09) : 963 - 970
  • [30] Approximate design and cost evaluation of internally heat-integrated distillation columns (HIDiCs)
    Young Han Kim
    Korean Journal of Chemical Engineering, 2012, 29 : 1004 - 1009