Perfect-Foresight Flow-Rate Control of a Photovoltaic–Thermal Collector for Thermochemical Storage: An Exergy Upper Bound

设定值 上下界 控制理论(社会学) 控制器(灌溉) 火用 水准点(测量) 间歇性 机械 流入 热力学 可用能 环境科学 数学 计算机科学 瓶颈 性能系数 温度控制 带宽遏流 流量(数学) 再沸器 质量流量 非绝热的 储能 化学 上临界溶液温度 工程类 工艺工程
作者
Suratsavadee Koonlaboon Korkua,Krit Funsian,Choosak Rittiphet,Mohammad Faridun Naim Tajuddin,Santanu Kumar Dash,Kamon Thinsurat
出处
期刊:Energies [Multidisciplinary Digital Publishing Institute]
卷期号:19 (17): 3949-3949
标识
DOI:10.3390/en19173949
摘要

Photovoltaic–thermal (PVT) collectors coupled to thermochemical energy storage (TCES) can turn intermittent low-grade solar heat into a dispatchable service, but solar intermittency poses a closed-loop control problem. A companion study established the feedback-only lower bound: a 937 kJ accumulated exergy-delivery-deficit benchmark under optimally tuned proportional–integral–derivative (PID) flow control. The corresponding upper bound is quantified here by means of a deliberately idealised search-based predictive controller that, at each 10 s step, enumerates 51 candidate pump rates, predicts the reactor-inlet temperature by a single forward-Euler step, and is granted perfect future irradiance. On the experimentally validated shared plant (matched to the companion baseline), against an optimally tuned PID, the perfect-foresight advantage is marginal: +0.96% daily exergy on synthetic days and +0.07–0.24% on two measured Walailak University monsoon days, all controllers tracking within 6–13 K on the measured days. Under tropical-monsoon irradiance, the 95 °C desorption setpoint is rarely sustained, so the delivered exergy is nearly controller-independent: the perfect-foresight upper bound lies just above the feedback-only lower bound, and together the two results bracket the exergy envelope available to any flow-rate controller of this system. A horizon sweep localises the bottleneck to internal-model fidelity, not anticipation depth. The eight-node plant is validated against measured module temperature (root-mean-square error 3.5 °C, coefficient of determination R2 = 0.89) and a copper-tube PVT prototype (1.5 °C; peak hot water up to 79 °C). The central contribution is therefore a rigorously defined, experimentally grounded upper bound showing that, at this scale and latitude, deployability rather than anticipation is the effective design lever.
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