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A computer-aided tool for the simulation and optimization of the combined HDS-FCC processes

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dc.contributor.author Bollas, GM en
dc.contributor.author Papadokonstantakis, S en
dc.contributor.author Michalopoulos, J en
dc.contributor.author Arampatzis, G en
dc.contributor.author Lappas, AA en
dc.contributor.author Vasalos, IA en
dc.contributor.author Lygeros, A en
dc.date.accessioned 2014-03-01T01:19:44Z
dc.date.available 2014-03-01T01:19:44Z
dc.date.issued 2004 en
dc.identifier.issn 0263-8762 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/15681
dc.subject Computer-aided tools en
dc.subject Fluid catalytic cracking en
dc.subject Hydrodesulphurization en
dc.subject Optimization en
dc.subject Process modelling en
dc.subject Simulation en
dc.subject.classification Engineering, Chemical en
dc.subject.other Algorithms en
dc.subject.other Computer simulation en
dc.subject.other Computer software en
dc.subject.other Oil shale refining en
dc.subject.other Optimization en
dc.subject.other Sensitivity analysis en
dc.subject.other Computer software - Visual Basic en
dc.subject.other Dehydrosulfurization (HDS) en
dc.subject.other Fluid catalytic cracking en
dc.subject.other computer aided process planning en
dc.title A computer-aided tool for the simulation and optimization of the combined HDS-FCC processes en
heal.type journalArticle en
heal.identifier.primary 10.1205/0263876041596706 en
heal.identifier.secondary http://dx.doi.org/10.1205/0263876041596706 en
heal.language English en
heal.publicationDate 2004 en
heal.abstract A computer-aided tool for the simulation, optimization and analysis of the combined operation of the hydrodesulphurization (HDS) and fluid catalytic cracking (FCC) processes in an oil refinery is presented. The optimization of these processes is an important yet difficult engineering task, because of the complexity in the integration of the two units, the large number of interacting variables, the product quality specifications and the financial benefits associated. The proposed tool is developed in a user-friendly Visual Basic environment and operates in two different modes: the modelling-prediction mode and the optimization-sensitivity analysis mode. The modelling of the processes is based on 'short form' models, which were created following statistical and neural network approaches. This kind of model usually has short computing time requirements, which is critical for the optimization mode. The optimization algorithm is based on a financial objective function with a flexible form, which gives the user the option to explore a variety of scenarios. Industrial runs have verified the modelling accuracy of the tool. The optimization scenarios examined include the contemporary needs of modern refineries for LPG and gasoline maximization, subject to strict quality specifications. The demonstration of this tool aims to give an insight into the system dependencies and add knowledge on the possibility of a more profitable operation of such a complex process. © 2004 Institution of Chemical Engineers. en
heal.publisher INST CHEMICAL ENGINEERS en
heal.journalName Chemical Engineering Research and Design en
dc.identifier.doi 10.1205/0263876041596706 en
dc.identifier.isi ISI:000222552800008 en
dc.identifier.volume 82 en
dc.identifier.issue 7 en
dc.identifier.spage 881 en
dc.identifier.epage 894 en


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