首页> 外文会议>Power and Energy Engineering Conference (APPEEC), 2010 >Optimization Model and PID Temperature Control System Design for CO2 Capture Process by CaO Carbonation-CaCO3 Calcination Cycles
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Optimization Model and PID Temperature Control System Design for CO2 Capture Process by CaO Carbonation-CaCO3 Calcination Cycles

机译:CaO碳化-CaCO3煅烧循环CO2捕集工艺优化模型及PID温度控制系统设计

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CO2 capture processes by carbonation-calcination cycles of CaO/CaCO3 were limited by the carbonation conversion and sorbents reutilization with the number of carbonation/calcinations cycles. In order to optimizing the CaO/CaCO3 cycles, BP neural network model and PID temperature control system were established based on the simulation of the process parameters and dynamic characteristics. The carbonization/calcination temperature, the mass fraction of additives for sorbents and calcination time were selected for the input conditions, while the output conditions were capture capacity and the reutilization of sorbents. Genetic algorithm(GA) model is established to optimize the PID controller's proportional coefficient kp, integral coefficient k1, and differential coefficient kD. The results indicated that BPNN coupled with PID model could form a complete optimization strategy for CO2 capture process by CaO/CaCO3 cycles.
机译:CaO / CaCO 3 的碳化-煅烧循环捕获CO 2 过程受碳酸化转化率和吸附剂再利用次数的限制。为了优化CaO / CaCO 3 循环,在模拟工艺参数和动态特性的基础上,建立了BP神经网络模型和PID温度控制系统。输入条件选择碳化/煅烧温度,吸附剂添加剂的质量分数和煅烧时间,而输出条件为捕获能力和吸附剂的再利用。建立遗传算法模型,优化PID控制器的比例系数k p ,积分系数k 1 和微分系数kD。结果表明,BP神经网络结合PID模型可以通过CaO / CaCO 3 循环形成一个完整的CO 2 捕获过程优化策略。

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