2004
DOI: 10.1021/ie049978l
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Approximation Algorithms for the Minimum Number of Matches Problem in Heat Exchanger Network Synthesis

Abstract: Although the use of heuristics has been prevalent in the process synthesis literature, their justification has been exclusively based on empirical evidence obtained through computational testing. As a result, heuristics currently in use offer no guarantee of optimality. Optimization algorithms, on the other hand, offer rigor but suffer from the combinatorial explosion of computational requirements necessary to produce an optimal solution. Recognizing this gap between heuristic and optimization approaches in pr… Show more

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Cited by 23 publications
(49 citation statements)
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“…However, the author refers the interested reader to a selected subset of excellent reviews and perspective papers on: reactor and reactor-separator network synthesis focusing on attainable region construction (Feinberg, 2002), synthesis of heat integration networks (Furman and Sahinidis, 2004;Morar and Agachi, 2010), water network synthesis (Jez˙ owski, 2010), distillation-based separation sequence synthesis (Skiborowski et al, 2013), and general process synthesis approaches focusing on their substantial potential for synthesis of sustainable and environmentally-friendly processes for energy and chemicals production (Grossmann and Guillén-Gosálbez, 2010;Yuan and Chen, 2012;Yuan et al, 2013).…”
Section: Introductionmentioning
confidence: 99%
“…However, the author refers the interested reader to a selected subset of excellent reviews and perspective papers on: reactor and reactor-separator network synthesis focusing on attainable region construction (Feinberg, 2002), synthesis of heat integration networks (Furman and Sahinidis, 2004;Morar and Agachi, 2010), water network synthesis (Jez˙ owski, 2010), distillation-based separation sequence synthesis (Skiborowski et al, 2013), and general process synthesis approaches focusing on their substantial potential for synthesis of sustainable and environmentally-friendly processes for energy and chemicals production (Grossmann and Guillén-Gosálbez, 2010;Yuan and Chen, 2012;Yuan et al, 2013).…”
Section: Introductionmentioning
confidence: 99%
“…Such definition almost always leads to a total number of units that is larger than N min (as defined above), and consequently these structures are rarely MSTR structures. Similarly, structures with nonisothermal mixing and with bypasses that cannot be represented by the staged superstructure have been studied and rendered values given by N min that are virtually impossible using other limited superstructures.Remark There have been several studies in the literature regarding the a‐priori calculation of the minimum number of units, sometimes referred to as minimum number of matches . Letsios et al presented a proof that the minimum number is N min = NH + NC + NHU + NCU‐L , where NHU and NCU are the number of hot and cold utilities types respectively and L ∈ [1, Min { NH + NHU , NC + NCU }].…”
Section: Hen Propertiesmentioning
confidence: 99%
“…Continuous variables t H i,j,k and t C i,j,k express the exiting temperature of hot stream Figure 5: In the transportation model (Cerda and Westerburg, 1983), each hot stream i supplies σ i,t units of heat in temperature interval t which can be received, in the same or a lower temperature interval, by a cold stream j which demands δ j,t units of heat in t. In the transshipment model (Papoulias and Grossmann, 1983), there are also intermediate nodes transferring residual heat to a lower temperature interval. This figure is adapted from Furman and Sahinidis (2004).…”
Section: Multistage Minimum Utility Cost Problemmentioning
confidence: 99%