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Application of response surface methodology as a new PID tuning method in an electrocoagulation process control case

机译:响应面方法在电凝过程控制箱中的新PID调谐方法中的应用

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In this work the application of response surface methodology (RSM) to proportional-integral-derivative (PID) controller parameter tuning for electrocoagulation (EC) treatment of pulp and paper mill wastewater was researched. Dynamic data for two controlled variables (pH and electrical conductivity) were obtained under pseudo random binary sequence (PRBS) input signals applied to manipulated variables (acid and supporting electrolyte flow rates). Third order plus time delay model parameters were evaluated through System Identification Toolbox (TM) in MATLAB (R). Four level full factorial design was applied to form a design matrix for three controller tuning parameters as factors and to evaluate statistical analysis of the system in terms of integral of square error (ISE), integral of absolute error (IAE), integral of time square error (ITSE) and integral of time absolute error (ITAE) performance criteria as response. Numerical values of the responses for the runs in the design matrices were determined using closed-loop PID control system simulations designed in Simulink (R). Optimum proportional gain, integral action and derivative action values for electrical conductivity control were found to be 1,500 s, 0 s and 16.4636 s respectively. Accordingly, the same optimization scheme was followed for pH control and optimum controller parameters were found to be -8.6970 s, 0.0211 s and 50 s, respectively. Theoretically optimized controller parameters were applied to batch experimental studies. Chemical oxygen demand (COD) removal efficiency and energy consumption of pulp and paper mill wastewater treatment by EC under controlled action of pH at 5.5 and electrical conductivity at 2.72 mS/cm was found to be 85% and 3.87 kWh/m(3) respectively. Results showed that multi input-multi output (MIMO) control action increased removal efficiency of COD by 15.41% and reduced energy consumption by 6.52% in comparison with treatment under uncontrolled conditions.
机译:在这项工作中,研究了响应表面方法(RSM)对比例 - 积分 - 衍生物(PID)控制器参数调整用于电凝固纸浆和造纸厂废水的电凝(EC)处理。在伪随机二进制序列(PRBS)输入信号下获得两个受控变量(pH和电导率)的动态数据,其施加到操纵变量(酸和支撑电解质流速)。第三阶加上时间延迟模型参数通过Matlab(R)中的系统识别工具箱(TM)进行评估。使用四级全面设计,形成三个控制器调整参数的设计矩阵作为因素,并根据方误差(ISE)的整体,绝对误差(IAE)积分的统计分析,绝对误差(IAE)的积分,时间广场错误(ITSE)和时间绝对错误(ITAE)性能条件作为响应。使用在Simulink(R)中设计的闭环PID控制系统模拟确定设计矩阵中运行响应的数值。发现导电性控制的最佳比例增益,积分动作和衍生作用值分别为1,500秒,0 s和16.4636秒。因此,遵循相同的优化方案进行pH控制,发现最佳控制器参数分别为-8.6970 s,0.0211s和50 s。从理论上优化的控制器参数应用于批量实验研究。 EC在PH值下的PH值下的纸浆和纸体造纸废水的去除效率和能量消耗在5.5和2.72ms / cm的电导率下,分别为85%和3.87kWh / m(3) 。结果表明,与不受控制条件下的治疗相比,多输入多输出(MIMO)控制动作增加了15.41%,减少了活力,减少了6.52%。

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