Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
10262442 | Chemical Engineering Science | 2012 | 12 Pages |
Abstract
⺠We introduce a reduced order rate based model for distillation in packed columns. ⺠It is shown that despite the large-scale model, structure can be efficiently exploited. ⺠The high differentiation index problem is studied. ⺠A procedure based on structural analysis of model Jacobian is proposed for index reduction. ⺠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
J. Bonilla, F. Logist, J. Degrève, B. De Moor, J. Van Impe,