1997
DOI: 10.1016/s1474-6670(17)43044-8
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Improvement of De-NOx Device Control Performance Using Software Sensor

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Cited by 9 publications
(11 citation statements)
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“…Software sensors have been described for diverse applications, such as chemical reactors (Régnier et al, 1996), analytical devices (Matsumura et al, 1998), environmental processes (Carstensen et al, 1996), and bioprocesses (Kiviharju et al, 2008). In addition, software sensors support the ambition of process analytical technology (PAT) to establish on-line monitoring methods for high quality manufacture of pharmaceutical products (FDA, 2004;Gnoth et al, 2007).…”
Section: Introductionmentioning
confidence: 99%
“…Software sensors have been described for diverse applications, such as chemical reactors (Régnier et al, 1996), analytical devices (Matsumura et al, 1998), environmental processes (Carstensen et al, 1996), and bioprocesses (Kiviharju et al, 2008). In addition, software sensors support the ambition of process analytical technology (PAT) to establish on-line monitoring methods for high quality manufacture of pharmaceutical products (FDA, 2004;Gnoth et al, 2007).…”
Section: Introductionmentioning
confidence: 99%
“…From (7), the output prediction may be also described as the following form: (14) where (15) Define the control move sequence and the desired output sequence as follows:…”
Section: B Nonlinear Mpc Strategymentioning
confidence: 99%
“…Now let us consider the following optimization problem, shown in equation (18) at the bottom of the page, where , represents the identity matrix, and are the positive definite diagonal weighting matrices, and both control levels and control moves are penalized. Introducing (15) into (18), after removing the constant terms, the quadratic form of the optimization problem (18) could be obtained as shown in (19)-(23) at the bottom of the page. The online optimization problem (19) or (20) may be solved by the quadratic programming (QP) routines.…”
Section: B Nonlinear Mpc Strategymentioning
confidence: 99%
“…1 shows the structure diagram of a de-NO x process in a thermal power plant. The dynamic behavior of this process is nonlinear and non-stationary, and depends on the timevarying load demand w(t) of the power plant (Matsumura et al, 1997). At different load levels, the process dynamics (between the de-NO x device outlet NO x y(t) and the total NH 3 flow-set u(t)+v 2 (t) in Fig.…”
Section: Simulation Studymentioning
confidence: 99%