2003
DOI: 10.1021/ie020965m
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Mathematical Programming Model for Heat-Exchanger Network Synthesis Including Detailed Heat-Exchanger Designs. 2. Network Synthesis

Abstract: This work proposes an optimization model for heat-exchanger network synthesis that includes a heat-exchanger design model. This model takes into account several detailed design variables: number of tubes, number of tube passes, internal and external tube diameters, tube arrangement pattern, number of baffles, head type, and fluid allocation (i.e., to the shell or tubes). The network superstructure with individual heat-exchanger designs is solved using the logic-based outer approximation method (Turkay, M.; Gro… Show more

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Cited by 63 publications
(71 citation statements)
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“…Depending on the flow regime and the operating conditions, the heat transfer coefficient on tube side can be calculated from the following correlations [22,23].…”
Section: Shell and Tube Side Heat Transfer Coefficientmentioning
confidence: 99%
“…Depending on the flow regime and the operating conditions, the heat transfer coefficient on tube side can be calculated from the following correlations [22,23].…”
Section: Shell and Tube Side Heat Transfer Coefficientmentioning
confidence: 99%
“…Case 1: 1.44(MW) duty, kerosene-crude oil exchanger [19] Case 2: 0.46(MW) duty, distilled water-raw water exchanger [16] Case 3: 4.34(MW) duty, Process fluid-water exchanger [20].…”
Section: Case Studiesmentioning
confidence: 99%
“…The third case studies were analyzed by Ponce-Ortega et al [17] using GA approach and taken from literature [20].…”
Section: Case Studiesmentioning
confidence: 99%
“…These curves demonstrate in separate diagrams the impact on heat transfer area of variations in decision variables such as tube length, tube diameter and tube arrangement. Using Delaware's approach, Ponce et al [15] described shell side flow and used a genetic algorithm with a few decision variables to minimize their objective function (total cost), and observed a decrease in pressure drop and total cost compared with a similar analysis in another reference [16]. Munawar and Babu [17] used differential completion for optimizing a shell and tube heat exchanger.…”
Section: Introductionmentioning
confidence: 99%