Development Of Model Based Decoupler For Multi Input Multi Output Distillation Column
Distillation column is a complex multivariable system and exhibits nonlinear dynamic behaviour due to the complex processing configurations and high product purities. The strong coupling among control loops often invalidates conventional loop controllers. Coupling is a very common phenomenon in m...
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my.usm.eprints.59477 http://eprints.usm.my/59477/ Development Of Model Based Decoupler For Multi Input Multi Output Distillation Column Lee, Qiao Hui TP1-1185 Chemical technology Distillation column is a complex multivariable system and exhibits nonlinear dynamic behaviour due to the complex processing configurations and high product purities. The strong coupling among control loops often invalidates conventional loop controllers. Coupling is a very common phenomenon in multiple input multiple output (MIMO) systems. During processes, multiple control loops are designed for a process plant to control and guarantee the product quality. However, the control loops interact with other significantly. Due to the interaction between the loops, the stability and the product quality of the process may be compromised. Therefore, decoupling control was introduced to reduce the coupling problem in the nonlinear system. 2013-01 Thesis NonPeerReviewed application/pdf en http://eprints.usm.my/59477/1/24%20Pages%20from%2000001779527.pdf Lee, Qiao Hui (2013) Development Of Model Based Decoupler For Multi Input Multi Output Distillation Column. Masters thesis, Perpustakaan Hamzah Sendut. |
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TP1-1185 Chemical technology Lee, Qiao Hui Development Of Model Based Decoupler For Multi Input Multi Output Distillation Column |
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Distillation column is a complex multivariable system and exhibits nonlinear
dynamic behaviour due to the complex processing configurations and high product
purities. The strong coupling among control loops often invalidates conventional
loop controllers. Coupling is a very common phenomenon in multiple input multiple
output (MIMO) systems. During processes, multiple control loops are designed for a
process plant to control and guarantee the product quality. However, the control
loops interact with other significantly. Due to the interaction between the loops, the
stability and the product quality of the process may be compromised. Therefore,
decoupling control was introduced to reduce the coupling problem in the nonlinear
system. |
format |
Thesis |
author |
Lee, Qiao Hui |
author_facet |
Lee, Qiao Hui |
author_sort |
Lee, Qiao Hui |
title |
Development Of Model Based Decoupler For Multi Input Multi Output Distillation Column |
title_short |
Development Of Model Based Decoupler For Multi Input Multi Output Distillation Column |
title_full |
Development Of Model Based Decoupler For Multi Input Multi Output Distillation Column |
title_fullStr |
Development Of Model Based Decoupler For Multi Input Multi Output Distillation Column |
title_full_unstemmed |
Development Of Model Based Decoupler For Multi Input Multi Output Distillation Column |
title_sort |
development of model based decoupler for multi input multi output distillation column |
publishDate |
2013 |
url |
http://eprints.usm.my/59477/1/24%20Pages%20from%2000001779527.pdf http://eprints.usm.my/59477/ |
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1781705438262198272 |