2024
DOI: 10.1016/j.applthermaleng.2024.123471
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Nonlinear state estimation of a power plant superheater by using the extended Kalman filter for differential algebraic equation systems

Vivek Saini,
Debangsu Bhattacharyya,
Daniel Purdy
et al.
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Cited by 4 publications
(3 citation statements)
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“…Obviously, a larger number of discretization grid points may be considered for higher spatial resolution, if needed. 46 The flow pattern as well as the input and output variables to the ECNN model remain the same for both flue gas and steam as compared to the lumped model. However, for both training and forward problems while developing ECNN for the distributed model, the enthalpy balance constraint eq (eq 13) has to be exactly satisfied for each of the individual control volumes in spatial directions, along with the boundaries of the system.…”
Section: Case Studies and Corresponding Mass−energy Balance Constraintsmentioning
confidence: 99%
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“…Obviously, a larger number of discretization grid points may be considered for higher spatial resolution, if needed. 46 The flow pattern as well as the input and output variables to the ECNN model remain the same for both flue gas and steam as compared to the lumped model. However, for both training and forward problems while developing ECNN for the distributed model, the enthalpy balance constraint eq (eq 13) has to be exactly satisfied for each of the individual control volumes in spatial directions, along with the boundaries of the system.…”
Section: Case Studies and Corresponding Mass−energy Balance Constraintsmentioning
confidence: 99%
“…Therefore, in this work, three nonlinear processes with different levels of complexity for mass and energy transfer within the system have been chosen for modeling. While the first case study considers the development of both lumped and distributed models of an adiabatic superheater/reheater system , involving no generation/loss/conversion of energy within the system, the second and third case studies, respectively, consider developing MECNNs to model the widely used nonisothermal lumped (i.e., CSTR) van de Vusse reactor system , involving an exothermic reaction (hence heat generation), as well as an electrically heated distributed tubular (plug-flow) reactor , involving vapor-phase cracking of acetone during the production of acetic anhydride, where electric energy gets transformed to heat to facilitate the endothermic reaction. Although, the mass balance constraints are trivially satisfied for the superheater/reheater system (Case Study 1), both mass and energy conservation laws have been simultaneously incorporated as equality constraints for the other two case studies considered in this work.…”
Section: Case Studies and Corresponding Mass–energy Balance Constraintsmentioning
confidence: 99%
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