The parameter estimation and refinement of a steam methane reformer model.

dc.contributor.authorSeverinsen, Isaac
dc.date.accessioned2020-07-27T01:11:51Z
dc.date.available2020-07-27T01:11:51Z
dc.date.issued2020en
dc.description.abstractThis work comprises of incremental enrichment of a steam methane reformer model to enable its use as a prediction tool for process changes. Using a variety of compounding improvements a model was developed that accurately predicts relevant outlet reformed gas parameters. This model reflects a real reformer including: physical and chemical catalyst degradation effects, geometry of real reformer design, real gas physical properties estimation, modern reaction kinetics and coking prediction. This model is validated and regressed against industrial data from the steam reformer of an operating methanol plant. Using this industrial data relevant key models of: reaction kinetics, heat transfer, pressure drop and higher hydrocarbon reaction kinetics from literature are evaluated for their accuracy and effectiveness in an industrial setting.en
dc.identifier.urihttps://hdl.handle.net/10092/100758
dc.identifier.urihttp://dx.doi.org/10.26021/958
dc.languageEnglish
dc.language.isoen
dc.publisherUniversity of Canterburyen
dc.rightsAll Right Reserveden
dc.rights.urihttps://canterbury.libguides.com/rights/thesesen
dc.titleThe parameter estimation and refinement of a steam methane reformer model.en
dc.typeTheses / Dissertationsen
thesis.degree.disciplineChemical Engineeringen
thesis.degree.grantorUniversity of Canterburyen
thesis.degree.levelMastersen
thesis.degree.nameMaster of Engineeringen
uc.bibnumber2940650en
uc.collegeFaculty of Engineeringen
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