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  1. IEEE Industry Applications Society Dynamic Modeling Control Applications for Industry Workshop.
  2. IEEE Industry Applications Society Dynamic Modeling Control Applications for Industry Workshop
  3. Using first-principle models in control
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IEEE Industry Applications on Dynamic Modeling Control Applications for Industry Workshop
IEEE Industry Applications Society Dynamic Modeling Control Applications for Industry Workshop
Author index
Model-based Kamyr digester control
Modeling and control of a continuous digester
Using first-principle models in control
Monitoring and controlling of a real-time industrial process using dynamic model control technology
Real-time model-based fault detection and diagnosis for automated systems
Utilizing a neural network modeling process to create an inferred instrument
A survey of adaptive control applications
PID controller tuning for mixed continuous/discrete event processes using dynamic simulation
Lime kiln hybrid control system
Predictive-adaptive temperature control of molten glass
Multivariable identification of paper machine cross-direction process using an automated tool
Knowledgescaping: on-line, adaptive optimizing control methods
Sensor development in oil sand processing

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Using first-principle models in control

Content Provider IEEE Xplore Digital Library
Author Rhinehart, R.R.
Copyright Year 1997
Description Author affiliation: Dept. of Chem. Eng., Texas Tech. Univ., Lubbock, TX, USA (Rhinehart, R.R.)
Abstract Technical advances in computers make it feasible to use nonlinear process models for automatic control. One advantage over linear model-based controllers is that nonlinear controllers are functional over a wider operating range without retuning; and, where process nonlinearity is the major control problem, nonlinear controllers have demonstrated industrial success. Where designed with adaptive models, tracking phenomenologically meaningful model coefficients for process diagnosis, and using the model for supervisory optimization are other advantages. Disadvantages are the required case-by-case controller design and inability to mathematically guarantee such features as convergence, stability, etc.
Starting Page 10
Ending Page 19
File Size 495566
Page Count 10
File Format PDF
DOI 10.1109/DMCA.1997.603383
Language English
Publisher Institute of Electrical and Electronics Engineers, Inc. (IEEE)
Publisher Date 1997-05-26
Publisher Place Canada
Access Restriction Subscribed
Rights Holder Institute of Electrical and Electronics Engineers, Inc. (IEEE)
Subject Keyword Automatic control Fluid dynamics Inverse problems Transfer functions Process control Output feedback Predictive models Chemical engineering Design optimization Stability
Content Type Text
Resource Type Article
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