1999
DOI: 10.1002/(sici)1099-1239(199909)9:11<799::aid-rnc441>3.3.co;2-l
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A novel analysis and design of a neural network assisted nonlinear controller for a bioreactor

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Cited by 6 publications
(12 citation statements)
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“…The process is valuable as its dynamics consists of coupled and nonlinear differential equations, which display a rich set of behaviors containing limit cycles, attractors and repellers [9,10]. The bioreactor is a tank containing a mixture of water, biological cells and nutrients.…”
Section: Data Sets 1-2: Bioreactor Benchmark Problemmentioning
confidence: 99%
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“…The process is valuable as its dynamics consists of coupled and nonlinear differential equations, which display a rich set of behaviors containing limit cycles, attractors and repellers [9,10]. The bioreactor is a tank containing a mixture of water, biological cells and nutrients.…”
Section: Data Sets 1-2: Bioreactor Benchmark Problemmentioning
confidence: 99%
“…The state of the process is the amount of cells denoted by c k 1 ∈[0,1] and the amount of nutrients denoted by c k 2 ∈ [0, 1]. The two difference equations obtained after the discretization of the continuous time process are given in (4)-(5), where γ = 0.48 and β = 0.02 are the nutrient inhibition parameter the growth rate parameter, respectively [9][10][11].…”
Section: Data Sets 1-2: Bioreactor Benchmark Problemmentioning
confidence: 99%
“…where c 1 ðtÞ is the cell concentration that is considered as the output of the process ðyðtÞ ¼ c 1 ðtÞÞ; c 2 ðtÞ is the amount of nutrients per unit volume and uðtÞ is the flow rate as the control signal [36]. In our simulations, gðtÞ is considered as the time-varying parameter of the process, where its nominal value is g nom ¼ 0:48: The aim of the control task is to keep the cell concentration c 1 ðtÞ as close as possible to the reference trajectory by manipulating the flow rate, magnitude of which is allowed to be between u min ¼ 0 and u max ¼ 2; and duration of which is kept constant at t min ¼ t max ¼ 0:5 s: The GPC parameters appeared in the performance index (2) are set to N 2 ¼ 10; N u ¼ 2 and l j ¼ 0:0001 for j ¼ 1; .…”
Section: Bioreactormentioning
confidence: 99%
“…Ungar [31] defines a Bioreactor Benchmark Problem that excellently fits in the context. The state of the process is described by two dimensionless variables named the cell mass denoted by c 1 (t) and the amount of nutrients denoted by c 2 (t) (see Ungar [31]; Puskorius and Feldkamp [23] and Efe et al [8]). The units for both variables are the normalized concentrations, i.e.…”
Section: Introductionmentioning
confidence: 99%
“…Efe et al [8] consider this problem for developing a nonlinear control law forcing the process states to those of a first order linear one. A MLP structure is used to build the nonlinear function in the control law and the plant is forced to follow a reference model.…”
Section: Introductionmentioning
confidence: 99%