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Figure 2: Dual UEGO Fore-Aft Controller  A review of electrochemical sensor technology may be found in [33]. Control and diagnosis of catalysts using UEGO sensors are described by [84, 35]. In [36, 37], Fiengo and co-authors use the catalyst model described above along with pre- and post-catalyst UEGO sensors to develop a controller with two objectives: to simultaneously maximize the conversion efficiencies of HC, CO and NO,, and to obtain steady-state air- fuel control that is robust with respect to disturbances. A series controller topology is adopted as illustrated in Figure 2. The objective of the first block, the Fore Controller, is to respond relatively quickly to A/F disturbances on the basis of measured feedgas oxygen level. The objective of the second block, the Aft Controller, is to adjust the setpoint of the fore controller, on the basis of both A/F measurements, so that the TWC achieves simultaneously high conversion efficiencies for HC’ and NO,. The aft controller is composed of a bias estimator and a proportional term. The bias estimator uses the upstream and downstream A/F measurements to correct the error in the upstream oxygen sensor. The proportional controller feeds back the post-catalyst UEGO sensor measurement and establishes the reference for the fore controller.

Figure 2 Dual UEGO Fore-Aft Controller A review of electrochemical sensor technology may be found in [33]. Control and diagnosis of catalysts using UEGO sensors are described by [84, 35]. In [36, 37], Fiengo and co-authors use the catalyst model described above along with pre- and post-catalyst UEGO sensors to develop a controller with two objectives: to simultaneously maximize the conversion efficiencies of HC, CO and NO,, and to obtain steady-state air- fuel control that is robust with respect to disturbances. A series controller topology is adopted as illustrated in Figure 2. The objective of the first block, the Fore Controller, is to respond relatively quickly to A/F disturbances on the basis of measured feedgas oxygen level. The objective of the second block, the Aft Controller, is to adjust the setpoint of the fore controller, on the basis of both A/F measurements, so that the TWC achieves simultaneously high conversion efficiencies for HC’ and NO,. The aft controller is composed of a bias estimator and a proportional term. The bias estimator uses the upstream and downstream A/F measurements to correct the error in the upstream oxygen sensor. The proportional controller feeds back the post-catalyst UEGO sensor measurement and establishes the reference for the fore controller.