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Optimal operating strategies for semi-batch reactor used for chromium sludge regeneration process

机译:铬污泥再生过程中半间歇式反应器的最佳运行策略

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This paper deals with controlling of a semi-batch nonlinear reactor used for chromium sludge regeneration process. The aim is to process the largest amount of chromium filter cake (chromium sludge) in the shortest possible time. The reactor has to be cooled because of strongly exothermic process. For safety reasons the temperature should not exceed 100 °C. In this study the reactor is controlled by two manipulating inputs: filter cake feeding flow rate and cooling water temperature. The speed of the whole process depends on the filter cake feeding flow rate - in case of a large amount filter cake addition a sharp temperature rise follows. The controller must be able to find optimal strategy between the filter cake dosing and the cooling temperature to reach the shortest possible process time. In order to deal with process nonlinearities here an online identification must be used. Results obtained using the proposed control method are then compared with our previous research, especially with control method using only one manipulating input - filter cake feeding flow rate.
机译:本文研究了用于铬污泥再生过程的半间歇式非线性反应器的控制。目的是在尽可能短的时间内处理最大数量的铬滤饼(铬泥渣)。由于强烈的放热过程,必须将反应器冷却。出于安全原因,温度不得超过100°C。在这项研究中,反应堆由两个操纵输入控制:滤饼进料流速和冷却水温度。整个过程的速度取决于滤饼的进料流速-如果大量添加滤饼,则温度会急剧上升。控制器必须能够在滤饼计量和冷却温度之间找到最佳策略,以达到最短的处理时间。为了处理过程非线性,必须使用在线标识。然后将使用建议的控制方法获得的结果与我们以前的研究进行比较,尤其是仅使用一个操纵输入-滤饼进料流速的控制方法。

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