Please use this identifier to cite or link to this item: https://doi.org/10.1002/aic.11682
Title: Operational modeling of multistream heat exchangers with phase changes
Authors: Hasan, M.M.F. 
Karimi, I.A. 
Alfadala, H.E.
Grootjans, H.
Keywords: Cryogenics
LNG
Main cryogenic-heat exchanger
MINLP
Multi-stream heat exchangers
Phase change
Superstructure
Issue Date: Jan-2009
Source: Hasan, M.M.F., Karimi, I.A., Alfadala, H.E., Grootjans, H. (2009-01). Operational modeling of multistream heat exchangers with phase changes. AIChE Journal 55 (1) : 150-171. ScholarBank@NUS Repository. https://doi.org/10.1002/aic.11682
Abstract: Multistream heat exchangers (MSHE) enable the simultaneous exchange of heat among multiple streams, and are preferred in cryogenic processes such as air separation and LNG. Most MSHEs are complex; proprietary and involve phase changes of mixtures. Although modeling MSHE is crucial for process optimization, no such work exists to our knowledge. We present a novel approach for deriving an approximate operational (vs. design) model from, historic data for an MSHE. Using a superstructure of simple 2-stream exchangers, we propose a mixed-integer nonlinear programming (MINLP) formulation to obtain a HE network that best represents the MSHE operation. We also develop an iterative algorithm to solve the large and nonconvex MINLP model in reasonable time, as existing commercial solvers fail to do so. Finally, we demonstrate the application of our work on an MSHE from an existing LNG plant, and successfully predict its performance over a variety of seasons and feed conditions. © 2008 American Institute of Chemical Engineers.
Source Title: AIChE Journal
URI: http://scholarbank.nus.edu.sg/handle/10635/64337
ISSN: 00011541
DOI: 10.1002/aic.11682
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