2024 AIChE Annual Meeting
(116a) Handling Model Mismatch in Economic Model Predictive Control for Heat Pump Water Heaters
Authors
In the context of HPWHs, the MPC can utilize a tank thermal dynamic model to predict tank temperature evolution, facilitating the design of a preheating strategy aimed at maintaining the tank temperatures within the desired comfort range. Several works have developed and validated PDEs and multi-node ODEs for modeling tank thermal stratification (e.g., [5]-[7]). However, these models are often nonlinear to account for the buoyancy effect caused by temperature inversion. Moreover, HPWHs typically use a HP with a constant-speed compressor and resistance heating with constant resistance. Thus, the MPC decisions for HPWHs are binary. Utilizing a nonlinear predictive model alongside binary decisions in the MPC results in a mixed-integer nonlinear problem (MINLP) which is not suitable for real-time control. Alternatively, several studies use a one-node, linear model of a HPWH to convert the MPC problem into an MILP, predicting the average tank temperature while neglecting thermal stratification (e.g., [8]-[10]). In contrast, Jin et al. employs a 2-node model of a HPWH in the MPC, yielding higher HP utilization and lower resistance element use compared to a 12-node model. This is due to underestimation of the lower tank temperature and overestimation of the upper tank temperature in the 2-node model [11]. Despite the prevalent use of one-node, linear HPWH models in the MPC literature, there is a lack of understanding on the implications of this modeling simplification on MPC performance, particularly when considering the use of back-up resistive heating. For example, Buechler et al. use a one-node model for a two-element resistive water heater in the MPC, enabling only the activation of the lower resistance element despite the potential preference of using the upper element to heat water drawn from the top of the tank [12].
In this work, we examine the impact of model mismatch on MPC for HPWHs equipped with two backup resistive elements. Specifically, a 20-node nonlinear model is used to simulate the actual HPWH, while a one-node, linear HPWH model is used as the prediction model in the MPC. This study highlights adverse effects that can arise from such modeling discrepancies, such as overheating and unnecessary tank heating attributed to the use of resistance heating. To mitigate these issues, we introduce constraints on resistance heating elements within the MPC to reduce scalding risks and minimize additional energy costs. We then apply this MPC approach to the simulated HPWH to evaluate its effectiveness in alleviating the adverse effects stemming from model mismatch.
References
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