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Process control of the advanced flash stripper for CO2 solvent regeneration

机译:用于二氧化碳溶剂再生的高级闪蒸器的过程控制

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The advanced flash stripper (AFS) is an intensified process design for CO2 solvent regeneration in amine scrubbing. This work identified self-optimizing controlled variables for the energy recovery bypass flowrates of the AFS, as well as a controller configuration for the steam extraction flowrate. Two self optimizing variables were selected using a high-fidelity steady state process model: the temperature difference at the top of the stripper packing and the temperature difference on the hot end of the stripper overhead heat exchanger. Ranges of possible off-design conditions for the rich loading, absorber temperature, rich flowrate, and flash tank operating temperature were evaluated, and the worst case heat duty for CO2 stripping of the self-optimizing control scheme was within 1% of the true system optimum. A low-order dynamic model was used to test the proposed self-optimizing control strategy and showed no significant control loop interactions in the closed-loop response. Cascade control, where the inner loop controlled the steam heater effluent temperature and the outer loop controlled the flash tank temperature, was found to have favorable dynamic performance compared to a non-cascaded structure with uncontrolled flash tank temperature. (C) 2016 Elsevier B.V. All rights reserved.
机译:先进的闪蒸器(AFS)是用于胺洗涤中CO2溶剂再生的强化工艺设计。这项工作确定了AFS能量回收旁路流量的自优化控制变量,以及蒸汽提取流量的控制器配置。使用高保真稳态过程模型选择了两个自我优化变量:汽提塔填料顶部的温度差和汽提塔顶置热交换器热端的温度差。评估了浓负载,吸收塔温度,浓流量和闪蒸罐工作温度可能超出设计的条件范围,并且自优化控制方案的CO2汽提的最坏情况热负荷在真实系统的1%以内最佳。一个低阶动态模型被用来测试所提出的自优化控制策略,并且在闭环响应中没有显着的控制环相互作用。与不受控的闪蒸罐温度的非级联结构相比,级联控制(内环控制蒸汽加热器的出水温度,外环控制闪蒸室的温度)具有良好的动态性能。 (C)2016 Elsevier B.V.保留所有权利。

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