Article ID Journal Published Year Pages File Type
10262442 Chemical Engineering Science 2012 12 Pages PDF
Abstract
► We introduce a reduced order rate based model for distillation in packed columns. ► It is shown that despite the large-scale model, structure can be efficiently exploited. ► The high differentiation index problem is studied. ► A procedure based on structural analysis of model Jacobian is proposed for index reduction. ► Model dynamic simulation and parameter sensitivity analysis for the proposed model is presented.
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
Authors
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