Seeking synergistic effect - A key principle in process intensification

被引:30
作者
Huang, Kejin [1 ]
Wang, San-Jang
Shan, Lan
Zhu, Qunxiong
Qian, Jixin
机构
[1] Beijing Univ Chem Technol, Sch Informat Sci & Technol, Beijing 100029, Peoples R China
[2] Ta Hwa Inst Technol, Dept Chem & Mat Engn, Hsinchu 307, Taiwan
[3] Zhejiang Univ, Sch Informat Sci & Technol, Hangzhou 300027, Zhejiang, Peoples R China
关键词
process intensification; synergistic effect; process design; process operation; reactive distillation;
D O I
10.1016/j.seppur.2007.03.022
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Process intensification calls. for the combination of two or more conventional unit operations within one framework, thus giving rise to a challenging coordination problem in process synthesis and design. Seeking synergistic effect among all the conventional unit operations involved is found to be an important principle for process development. Three cases of process intensification are studied to evaluate the principle, including: (i) a hypothetical reactive distillation system; (ii) a reactive distillation column for the hydration of ethylene oxide; (iii) an ideal heat-integrated distillation column. It is demonstrated that simply combining two or more conventional unit operations together does not necessarily tap out the full potentials of capital investment reduction and energy saving. Only after the synergistic effect has been deliberately considered in process synthesis and design, can process intensification be carried out in the most effective manner. Furthermore, seeking synergistic effect appears frequently to yield improved process dynamics and provide additional redundancy to process operation because the underlying conflicts could be attenuated among all the conventional unit operations involved. (c) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:111 / 120
页数:10
相关论文
共 31 条
[11]   Towards further internal heat integration in design of reactive distillation columns - Part II. The process dynamics and operation [J].
Huang, Kejin ;
Nakaiwa, Masaru ;
Tsutsumi, Atsushi .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (16) :5377-5392
[12]   Reactive distillation design with considerations of heats of reaction [J].
Huang, Kejin ;
Nakaiwa, Masaru ;
Wang, San-Jang ;
Tsutsumi, Atsushi .
AICHE JOURNAL, 2006, 52 (07) :2518-2534
[13]   Interpreting design of an ideal heat-integrated distillation column through exergy analysis [J].
Huang, Kejin ;
Matsuda, Keigo ;
Iwakabe, Koichi ;
Takamatsu, Takeichiro ;
Nakaiwa, Masaru .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2006, 39 (09) :963-970
[14]   Towards further internal heat integration in design of reactive distillation columns - Part I: The design principle [J].
Huang, KJ ;
Iwakabe, K ;
Nakaiwa, M ;
Tsutsumb, A .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (17) :4901-4914
[15]   Dynamics of ideal heat integrated distillation columns [J].
Huang, KJ ;
Nakaiwa, M ;
Akiya, T ;
Owa, M ;
Aso, K ;
Takamatsu, T .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1996, 29 (04) :656-661
[16]  
Huang KJ, 1997, CHINESE J CHEM ENG, V5, P325
[17]  
Huang KJ, 1999, CHINESE J CHEM ENG, V7, P283
[18]   Modular synthesis framework for combined separation/reaction systems [J].
Ismail, SR ;
Proios, P ;
Pistikopoulos, EN .
AICHE JOURNAL, 2001, 47 (03) :629-649
[19]   Reactive separations: more ways to skin a cat [J].
Krishna, R .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (09) :1491-1504
[20]   Economic and dynamic impact of the use of excess reactant in reactive distillation systems [J].
Luyben, WL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (08) :2935-2946