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ADAPTIVE CONTROL OF TEMPERATURE FOR MINIMIZATION OPERATING COSTS OF INDUSTRIAL METHANE TANK PROCESS

机译:工业甲烷池工艺最小化运行温度的温度自适应控制

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An algorithm for adaptive control of temperature in methane tank is developed in order to minimize operating costs under variation of the methane tank process conditions. The adaptation is based on process model and on-line minimization of objective function that relates operating costs to the process variables. Mathematical model for prediction of biogas production and simulation of the temperature control process is identified using experimental data from the waste water treatment plant. The temperature adaptive control system is investigated via computer simulation of the control system performance under operating conditions of real methane tank process during one year period. The process operating costs by optimal control of temperature are compared to those of temperature control at constant set-point. The model identification and the control system simulation results are presented and discussed.
机译:为了在甲烷罐工艺条件变化的情况下最小化运行成本,开发了一种用于甲烷罐温度自适应控制的算法。调整基于过程模型和目标函数的在线最小化,目标函数将运营成本与过程变量相关联。利用废水处理厂的实验数据,确定了预测沼气产量和模拟温度控制过程的数学模型。通过在真实甲烷罐工艺的运行条件下一年内对控制系统性能进行计算机模拟,研究了温度自适应控制系统。将通过最佳控制温度的过程运行成本与恒定设定点的温度控制成本进行比较。给出并讨论了模型辨识和控制系统仿真结果。

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