2005
DOI: 10.1016/j.jprocont.2005.03.007
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Analysis and control of a nonlinear boiler-turbine unit

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Cited by 148 publications
(74 citation statements)
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“…In our experiments we used a normal operating point for the BWPP in which the pressure equals 108 kg/cm 2 , that was achieved by keeping the three valves in the following normal valve positions (NVP): u 1 = 0.34, u 2 = 0.69 and u 3 = 0.433 [14]. As a consequence, TCCs, that implement the control logic code, must maintain constant the position of the three valves in order to provide a constant steam pressure of 108 kg/cm 2 .…”
Section: Boiling Water Power Plantmentioning
confidence: 99%
“…In our experiments we used a normal operating point for the BWPP in which the pressure equals 108 kg/cm 2 , that was achieved by keeping the three valves in the following normal valve positions (NVP): u 1 = 0.34, u 2 = 0.69 and u 3 = 0.433 [14]. As a consequence, TCCs, that implement the control logic code, must maintain constant the position of the three valves in order to provide a constant steam pressure of 108 kg/cm 2 .…”
Section: Boiling Water Power Plantmentioning
confidence: 99%
“…Recently, a nonlinearity measure via gap metric is proposed to assess the nonlinearity of the nonlinear system [20], [21]. Grid the operating space of the forcedcirculation byNoperating points, and the nonlinearity measure is defined as [21] (27) where L i N L, L j N L are linearization systems of the nonlinear plant at the i -th and the j -th operating point, respectively.…”
Section: ) Gap-metric-based Nonlinearity Measure For the Forcedcircumentioning
confidence: 99%
“…The boiler-turbine dynamics can be described by a nonlinear model of the 3 rd order, [1,8]. For individual subsystems we use the linearized model derived in [1], respective to one of operating points.…”
Section: Boiler-turbine Modelmentioning
confidence: 99%