Improved multi-model predictive control to reject very large disturbances on a distillation column
Abdul Wahid;
Arshad Ahmad
([Publisher not identified]
, 2016)
|
A multi modelpredictive control and proportional-integral controller switching (MMPCPIS)approach is proposed to control a nonlinear distillation column. The study wasimplemented on a multivariable nonlinear distillation column (Column A). Thesetpoint tracking and disturbance rejection performances of the proposedMMPCPIS were evaluated and compared to a proportional-integral(PI) controller and the hybrid controller (HC). MMPCPIS developed to overcome theHC?s limitation when dealing with very large disturbance changes (50%). MMPCPIS provided improvements by 27% and 31%of the ISE (integral of square error) for feed flow rate andfeed composition disturbance changes, respectively, comparedwith the PI controller, and 24% and 54% of the ISE for feed flow rate and feedcomposition disturbancechange, respectively, compared with HC. |
No. Panggil : | J-Pdf |
Entri utama-Nama orang : | |
Entri tambahan-Nama orang : | |
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Penerbitan : | [Place of publication not identified]: [Publisher not identified], 2016 |
Sumber Pengatalogan : | LibUI eng rda |
ISSN : | 20872100 |
Majalah/Jurnal : | International Journal of Technology (IJTECH) |
Volume : | Vol 7, No 6 (2016) 962-971 |
Tipe Konten : | text |
Tipe Media : | computer |
Tipe Carrier : | online resource |
Akses Elektronik : | http://www.ijtech.eng.ui.ac.id/index.php/journal/article/view/3524 |
Institusi Pemilik : | Universitas Indonesia |
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No. Panggil | No. Barkod | Ketersediaan |
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J-Pdf | 03-17-355520186 | TERSEDIA |
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