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Modelling and Multi-stage Design of Membrane Processes Applied to Carbon Capture in Coal-fired Power Plants

机译:燃煤电厂碳捕集膜过程的建模与多级设计

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摘要

According to recent predictions, energy generation from coal will continue to play a key role in the next decades. The UK 2008 Climate Change Act requires a reduction of 80% of greenhouse gases emissions by 2050, and carbon capture and storage will have a key role in order to meet this target.This work focuses on post-combustion capture from coal-fired power plants based on membrane separation. Adetailed multi-stage design is presented: the developed flowsheet includes cross-flow and countercurrent-sweep stages. The cross-flow stages are based on a 2D model implemented by our research group able to predict the separation through spiral-wound permeators. Different process configurations are analysed, with the aim of reducing both energy consumption and membrane area.An economic analysis is also included: both capture and avoidance costs are evaluated. The estimated values are compared with data available in the literature for processes based on amine capture technology.
机译:根据最近的预测,在未来几十年中,煤炭发电将继续发挥关键作用。英国《 2008年气候变化法案》要求到2050年减少80%的温室气体排放,碳捕集与封存将为实现这一目标发挥关键作用。这项工作的重点是燃煤电厂的燃烧后捕集。基于膜分离。介绍了详细的多阶段设计:开发的流程图包括错流和逆流扫描阶段。错流阶段基于我们研究小组实施的2D模型,该模型能够预测通过螺旋缠绕渗透器的分离。为了减少能耗和减少膜面积,分析了不同的工艺配置,还进行了经济分析:评估了捕获成本和避免成本。将估计值与文献中基于胺捕获技术的过程中可获得的数据进行比较。

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