2011 19th Mediterranean Conference on Control &Amp; Automation (MED) 2011
DOI: 10.1109/med.2011.5983157
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A general distillation modeling framework applied to an isotopic distillation column

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Cited by 3 publications
(2 citation statements)
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“…• Polymer production processes are composed of two stages, namely the primary process for bulk polymer generation and the secondary process for obtaining the polymer in spun form; • The principal tasks in acrylic fiber production are polymerization reaction, polymer separation, washing and filtration, polymer repulping, filtering, spun generation, second washing, and separation of solvent and washing (Grau et al, 1996, Capón-García et al, 2011a, EPA, 1995; • Two methods are used to synthesize acrylic fiber in industry, namely suspension and solution copolymerization technologies; either batch or continuous operation may be employed (EPA, 1995); • There is the possibility of avoiding solvent separation after the solution copolymerization reaction, provided that high conversion rates are achieved (Gol'dfein & Zyubin, 1990, Bajaj et al, 1996); • The operational information and dynamic models of copolymerization reaction is provided by Butala et al (1988) and of separation systems by Haggblom (1991), Luyben (1992), Oldenburg et al (2003), Muntean et al (2011); • Washing water of final product can be recovered and reused (EPA, 1995).…”
Section: Acrylic Fiber Productionmentioning
confidence: 99%
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“…• Polymer production processes are composed of two stages, namely the primary process for bulk polymer generation and the secondary process for obtaining the polymer in spun form; • The principal tasks in acrylic fiber production are polymerization reaction, polymer separation, washing and filtration, polymer repulping, filtering, spun generation, second washing, and separation of solvent and washing (Grau et al, 1996, Capón-García et al, 2011a, EPA, 1995; • Two methods are used to synthesize acrylic fiber in industry, namely suspension and solution copolymerization technologies; either batch or continuous operation may be employed (EPA, 1995); • There is the possibility of avoiding solvent separation after the solution copolymerization reaction, provided that high conversion rates are achieved (Gol'dfein & Zyubin, 1990, Bajaj et al, 1996); • The operational information and dynamic models of copolymerization reaction is provided by Butala et al (1988) and of separation systems by Haggblom (1991), Luyben (1992), Oldenburg et al (2003), Muntean et al (2011); • Washing water of final product can be recovered and reused (EPA, 1995).…”
Section: Acrylic Fiber Productionmentioning
confidence: 99%
“…The separation stage is lead using a energy separation system composed of an evaporator and a condenser. The dynamic equations system is defined according to Haggblom (1991), Luyben (1992), Oldenburg et al (2003), andMuntean et al (2011).…”
Section: Separation Stagementioning
confidence: 99%