Shell and tube heat exchanger flexible design strategy for process operability

Traditionally, the shell and tube heat exchanger (STHE) design minimizes the total annual cost subject to allowable pressure drop. However, it is often insufficient when considering equipment limitations and uncertain disturbance factors. Design inefficiency or improper operation of overall process...

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Bibliographic Details
Published inCase studies in thermal engineering Vol. 37; p. 102163
Main Authors Chen, Liang-Yu, Adi, Vincentius Surya Kurnia, Laxmidewi, Rosalia
Format Journal Article
LanguageEnglish
Published Elsevier Ltd 01.09.2022
Elsevier
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ISSN2214-157X
2214-157X
DOI10.1016/j.csite.2022.102163

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Summary:Traditionally, the shell and tube heat exchanger (STHE) design minimizes the total annual cost subject to allowable pressure drop. However, it is often insufficient when considering equipment limitations and uncertain disturbance factors. Design inefficiency or improper operation of overall process systems could potentially occur. A rigorous design strategy of STHE based on the flexibility index analysis method is proposed to address the above issues. The genetic algorithm with rigorous constraints is considered for the STHE design optimization. Simultaneously, the flexibility index (FI) is incorporated to quantify the uncertain factors of the STHE operation. The STHE load capacity and the corresponding uncertain disturbance factors affecting the STHE operability are evaluated. In addition, design workflows incorporating flexibility index are also discussed. Simultaneous consideration of the flexibility index in the optimization procedure can improve the STHE design operability under the expected range of disturbance factors and lower the total cost. [Display omitted]
ISSN:2214-157X
2214-157X
DOI:10.1016/j.csite.2022.102163