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A NEW METHOD FOR CO_2 CAPTURE: FROSTING CO_2 AT ATMOSPHERIC PRESSURE

机译:一种捕获CO_2的新方法:在大气压力下结霜CO_2

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摘要

CO_2 capture in the flue gas of energy production facilities shows a great advantage providing that it is performed at atmospheric pressure. Taking into account that the triple point of CO_2 is at 520 kPa and -56℃, the only possibility to capture CO_2 at atmospheric pressure is to freeze it on cold surface. This frosting is performed with a system consisting in an integrated cascade, which is a vapor compressor system using progressive distillation of a refrigerant blend in order to evaporate at low temperature (between -130 and -110℃) and at sufficient high pressure to keep an acceptable pressure ratio for a single stage compressor. The design and control of the frosting/defrosting on the heat exchanger surface permits the recovery of fusion heat when CO_2 changes from solid to liquid phase. This latent heat of fusion is used to cool down the liquid blend of refrigerants just prior to evaporation. The paper presents the global design of the system, the energy consumption and the coefficient of performance of this low temperature refrigerating system.
机译:如果在大气压力下进行,则在能源生产设施的烟气中捕获CO_2会显示出很大的优势。考虑到CO_2的三相点在520 kPa和-56℃,在大气压力下捕获CO_2的唯一可能性是将其冻结在冷的表面上。结霜是通过集成级联系统进行的,该系统是一种蒸汽压缩机系统,它使用制冷剂混合物的逐步蒸馏,以便在低温(-130至-110℃)和足够高的压力下蒸发,以保持单级压缩机可接受的压力比。热交换器表面结霜/除霜的设计和控制可在CO_2从固相变为液相时回收聚变热。熔化潜热仅在蒸发之前用于冷却制冷剂的液体混合物。本文介绍了该系统的总体设计,能耗和该低温制冷系统的性能系数。

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