2012
DOI: 10.1016/j.compchemeng.2012.05.012
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Inferential monitoring and optimization of crude separation units via hybrid models

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Cited by 55 publications
(36 citation statements)
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“…The vapor-liquid equilibrium is in this approach described by a RBFN. Similar approaches are also pro-posed by Mahalec and Sanchez (2012), Hinchliffe et al (2003) and Arahal et al (2008), where Hinchliffe et al (2003) divides the polymerization reactor into several stages whereas Arahal et al (2008) uses discrete volume and wall segments. The difficulty in the just named approaches is that for the training of the nonparametric model, sufficient data must be available, and that a nonparametric model trained with global data might not perform well locally.…”
Section: Modelingmentioning
confidence: 90%
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“…The vapor-liquid equilibrium is in this approach described by a RBFN. Similar approaches are also pro-posed by Mahalec and Sanchez (2012), Hinchliffe et al (2003) and Arahal et al (2008), where Hinchliffe et al (2003) divides the polymerization reactor into several stages whereas Arahal et al (2008) uses discrete volume and wall segments. The difficulty in the just named approaches is that for the training of the nonparametric model, sufficient data must be available, and that a nonparametric model trained with global data might not perform well locally.…”
Section: Modelingmentioning
confidence: 90%
“…The focus in this section is on modeling applications that deal with experimental data rather than data from virtual, simulated experiments, because simulation cases are typically applied to validate a pro-posed methodology (methodologies have been discussed above), while experimental studies are much more practically oriented. It can be seen in (Bhutani et al, 2006;Feil et al, 2004;Fiedler & Schuppert, 2008;Hinchliffe, Montague, Willis, & Burke, 2003;Mogk et al, 2002;Tian et al, 2001;Tsen et al, 1996;Vega, Lima, & Pinto, 2000), crystallization (Georgieva & de Azevedo, 2009;Georgieva, Meireles, & Feyo de Azevedo, 2003;Lauret, Boyer, & Gatina, 2000), metallurgic processes (Hu et al, 2011;Jia, Mao, Chang, & Zhao, 2011;Reuter et al, 1993;Sohlberg, 2005), distilla-tion columns (Chen et al, 2004;Mahalec & Sanchez, 2012;Safavi, Nooraii, & Romagnoli, 1999), drying processes (Cubillos & Acuna, 2007), thermal devices (Arahal, Cirre, & Berenguel, 2008), mechan-ical reactors (Nascimento et al, 1999) or milling (Aguiar & Filho, 2001; Kumar Akkisetty, Lee, Reklaitis, & Venkatasubramanian, 2010), for more details and references see Table2 -supplementary material. Since the number of applications is relatively large and most of which either use the standard serial approach consisting of material and/or energy balances in which the kinetics are represented by a nonparametric model or a parallel approach, only some approaches are discussed here, namely those that present solutions of more complex problems.…”
Section: Modelingmentioning
confidence: 99%
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