1989
DOI: 10.1002/cjce.5450670421
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Empirical strategies for open‐loop on‐line optimization

Abstract: Two empirical strategies for open‐loop on‐line optimization are developed as alternatives to the use of mechanistic process models. These strategies are based on on‐line identification of dynamic multi‐input single‐output (MISO) and multi‐input multi‐output (MIMO) models. The steady state gain of these models provides information for steady state optimization. Desirability functions, originally developed for multi‐objective optimization, are utilized as objective function modifiers for constrained on‐line opti… Show more

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Cited by 18 publications
(17 citation statements)
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References 15 publications
(13 reference statements)
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“…Perturbation-based methods for RTO system studied in this work include: (1) the Integrated System Optimization and Parameter Estimation (ISOPE) approach (Roberts, 1979); (2) a Linear Adaptive On-line Optimization (LAOO) approach (McFarlane and Bacon, 1989); and (3) a Quadratic Adaptive Online Optimization (QAOO) approach (Golden and Ydstie, 1989). A conventional RTO method, the Two-Phase approach (Chen and Joseph, 1987), which is widely used in current commercial RTO systems, is considered as a benchmark in this work.…”
Section: Perturbation-based Methods For Rto Systemmentioning
confidence: 99%
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“…Perturbation-based methods for RTO system studied in this work include: (1) the Integrated System Optimization and Parameter Estimation (ISOPE) approach (Roberts, 1979); (2) a Linear Adaptive On-line Optimization (LAOO) approach (McFarlane and Bacon, 1989); and (3) a Quadratic Adaptive Online Optimization (QAOO) approach (Golden and Ydstie, 1989). A conventional RTO method, the Two-Phase approach (Chen and Joseph, 1987), which is widely used in current commercial RTO systems, is considered as a benchmark in this work.…”
Section: Perturbation-based Methods For Rto Systemmentioning
confidence: 99%
“…One empirical strategy for determining the real plant inputoutput sensitivities ∇ x û during transitions between RTO cycles, proposed by McFarlane and Bacon (1989), is based on on-line identifi cation of a linear ARX model (Söderström and Stoica, 1989) and does not require any prior knowledge of process (i.e., fi rst-principles models are unnecessary). In this approach, Equation (5) is modifi ed to an unconstrained steady-state optimization problem by using a desirability function (McFarlane and Bacon, 1989).…”
Section: Linear Adaptive On-line Optimization Approachmentioning
confidence: 99%
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“…Indeed, the static gain of a transfer function represents the sensitivity (or gradient) of the output with respect to the input. McFarlane and Bacon [70] proposed to identify a linear ARX model and used the estimated static gradient for online optimizing control. A pseudo-random binary sequence (PRBS) was superimposed on each of the inputs to identify the ARX model.…”
Section: Dynamic Model Identificationmentioning
confidence: 99%
“…The same approach was also used by Golden and Ydstie [32] for estimating the first-and second-order derivatives of a SISO plant. Zhang and Forbes [60] compared the optimizing controllers proposed in [70] and [32] with ISOPE and the two-step approach.…”
Section: Dynamic Model Identificationmentioning
confidence: 99%