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Methane Post-Processor Development to Increase Oxygen Recovery beyond State-of-the-Art Carbon Dioxide Reduction Technology

机译:甲烷后处理技术的开发,将使氧气的回收率超过最先进的二氧化碳还原技术

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State-of-the-art life support carbon dioxide (CO_2) reduction technology, based on the Sabatier reaction, is theoretically capable of 50% recovery of oxygen from metabolic CO_2. This recovery is constrained by the limited availability of reactant hydrogen. Post-processing of the methane byproduct from the Sabatier reactor results in hydrogen recycle and a subsequent increase in oxygen recovery. For this purpose, a Methane Post-Processor Assembly containing three sub-systems has been developed and tested. The assembly includes a Methane Purification Assembly (MePA) to remove residual CO_2 and water vapor from the Sabatier product stream, a Plasma Pyrolysis Assembly (PPA) to partially pyrolyze methane into hydrogen and acetylene, and an Acetylene Separation Assembly (ASepA) to purify the hydrogen product for recycle. The results of partially integrated testing of these sub-systems are reported.
机译:基于Sabatier反应的最先进的生命支持二氧化碳(CO_2)还原技术理论上能够从代谢CO_2中回收50%的氧气。这种回收受到反应物氢有限供应的限制。 Sabatier反应器中甲烷副产物的后处理导致氢气再循环和随后氧气回收率的提高。为此,已经开发并测试了包含三个子系统的甲烷后处理装置。该组件包括:甲烷纯化组件(MePA),用于从Sabatier产品流中除去残留的CO_2和水蒸气;等离子体热解组件(PPA),用于将甲烷部分热解为氢气和乙炔;乙炔分离组件(ASepA),用于纯化回收氢气产品。报告了这些子系统的部分集成测试的结果。

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