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An Advanced CO2 Removal System Using Regenerable Solid Amines

机译:使用可再生固体胺的高级CO2去除系统

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United Technologies Aerospace Systems has drawn on over 30 years of experience with solid amine-based CO2 removal systems to develop a thermally desorbed system for the collection and concentration of CO2. Our approach incorporates a passive means of water vapor recovery, using desiccant materials in thermally linked sorbent beds, upstream of the solid amine CO2 sorbent beds, to achieve an approximate 90% nominal water vapor recovery with minimal power input. The residual water vapor and CO2 are subsequently removed by SA9T amine sorbent in a second set of sorbent beds. The dry, CO2 free effluent is then used to regenerate the desiccant beds using a simple sweep gas desorption. When the amine beds are loaded with CO2 to their design capacity, they are isolated, evacuated and heated to approximately 60°C, while simultaneously pumping the evolved CO2 and residual water vapor. The residual water vapor is removed from the CO2 product stream via sorbent beds, or a condensing heat exchanger, depending on the subsequent downstream processing requirements of the CO2. The concentrated CO2 can then be discharged overboard or sent to a CO2 reduction system such as Sabatier. A significant advantage to utilizing solid amines is that they are relatively insensitive to incoming water vapor and therefore large desiccant beds are not required upstream of the CO2 sorbent beds. Additionally, the passive nature of the water recovery and moderate regeneration temperature of the amine, may result in reduced power requirements compared to the state of the art CO2 removal systems. This paper presents results of our testing of our TRL 4 system, and current status of a TRL 5 design.
机译:United Technologies Aerospace Systems在30多年的经验中绘制了固体胺类的二氧化碳除去系统,为CO 2的收集和浓度开发热解吸系统。我们的方法包括水蒸气回收的被动装置,使用热链接的吸附剂床中的干燥剂材料,固体胺CO2吸附剂床的上游,以实现具有最小功率输入的近似90%的标称水蒸气回收。随后通过SA9T胺吸附剂在第二组吸附剂床中除去残留的水蒸气和CO 2。然后使用干燥的CO 2自由流出物使用简单的扫描气体解吸来再生干燥剂床。当胺床加载到它们的设计能力上时,将它们被隔离,抽空并加热至约60℃,同时泵送进化的二氧化碳和残留的水蒸气。根据CO 2的随后的下游加工要求,通过吸附剂床或冷凝热交换器从CO 2产物流中除去残留的水蒸气。然后可以将浓缩的CO 2排出落后或送到CO2还原系统,例如塔巴德。利用固体胺的显着优点是它们对进入的水蒸气相对不敏感,因此在CO 2吸附剂床的上游不需要大的干燥剂床。另外,与最先进的CO2去除系统相比,胺的水回收和中等再生温度的被动性能可能导致功率要求降低。本文提出了我们对TRL 4系统的测试的结果,以及TRL 5设计的当前状态。

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