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1999
DOI: 10.1002/aic.690450914
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Scoping and screening complex reaction networks using stochastic optimization

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Cited by 56 publications
(27 citation statements)
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“…The respective evolution of the superstructure, the selected clusters and their maximum objective values are illustrated in Table 8. The results obtained in this work compare well to those obtained in the literature (Marcoulaki, E. C. and Kokossis 1999) and with those obtained by conventional Tabu Search (Table 9). It is apparent that results from Simulated Annealing optimisation offer a small CSTR as the final reactor, which is equivalent to having an extra sub-CSTR at the end of the previous PFR, hence performing the same as a single PFR.…”
Section: Denbigh Reaction Resultssupporting
confidence: 81%
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“…The respective evolution of the superstructure, the selected clusters and their maximum objective values are illustrated in Table 8. The results obtained in this work compare well to those obtained in the literature (Marcoulaki, E. C. and Kokossis 1999) and with those obtained by conventional Tabu Search (Table 9). It is apparent that results from Simulated Annealing optimisation offer a small CSTR as the final reactor, which is equivalent to having an extra sub-CSTR at the end of the previous PFR, hence performing the same as a single PFR.…”
Section: Denbigh Reaction Resultssupporting
confidence: 81%
“…The1 Van de Vusse reaction consists of a combination of parallel and serial reactions (Kokossis, A. and Floudas 1990;Marcoulaki, E. C. and Kokossis 1999). In this reaction scheme, A is the reactant, B is desired product, and C and D are by-products ( The feed flows at 100 / and contains pure A with the feed concentration of 5.8 / .…”
Section: Appendix 1: the Van De Vusse Reactionmentioning
confidence: 99%
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“…Using alternative reactors and better integration, and in reference to a base case stirred-tank reactor, NREL reported a two-fold increase in the concentration of sugars, a ballpark figure for the expected benefits in the yields. Instead of case-by-case analysis, systems tools are able to, systematically target efficiencies (Mehta & Kokossis, 1997Marcoulaki & Kokossis, 1999), setting the scope for integration El-Halwagi, 1997Linke & Kokossis, 2007, El-Halwagi, et al, 2008 and enabling the evaluation of fractionation, enzyme technologies and reactive-separation schemes (Linke & Kokossis, 2003a). …”
Section: Process Level Analysis and Researchmentioning
confidence: 99%
“…Such methods are plentiful on energy targeting (Gundersen, 1988;Briones and Kokossis, 1999a,b), water targeting (Wang and Smith, 1994a,b;Smith, 2005;Hallale and Fraser, 1998;Alva-Argaez et al, 1999;2007a,b;Gunaratnam et al, 2005), and mass-exchange networks (Halwagi, 1997(Halwagi, , 1990a(Halwagi, ,b, 2006(Halwagi, , 2008, but also in reactor and reaction engineering targeting (Halwagi and Srinivas, 1992;Marcoulaki and Kokossis, 1999;Kokossis, 1997, 1998;Kokossis and Floudas, 1990), simple and complex distillation Kokossis, 2001, 2002), solvent design (Papadopoulos and Linke, 2006a, b;Kazantzi et al, 2007, Kazantzi andHalwagi, 2005;Kokossis, 2000, 2001) and reaction-separation systems (Linke and Kokossis, 2003a,b, 2004Kokossis and Floudas, 1991). Instead, literature evidence indicates a predominant use of general flowsheeting technology for techno-economic and case-by-case analysis, using Aspen Plus for instance, as in the work of NREL on bioethanol production (Wooley et al, 1999) and that of Haas et al (2006) for biodiesel.…”
mentioning
confidence: 99%