用于碳捕获和合成气生产的双相碳酸酯膜的研究进展

Liza Melia Terry , Melvin Xin Jie Wee , Claudia Li , Guoqiang Song , Jiuan Jing Chew , Jian Song , M. Hanif B.M. Halim , Farahdila B. Kadirkhan , Shaomin Liu , Sibudjing Kawi , Jaka Sunarso
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引用次数: 0

摘要

在全球范围内,随着人们对减少温室气体排放的环保意识的提高,推动了包括膜分离在内的碳捕集与利用(CCU)技术的发展。在膜分离技术中,双相碳酸酯膜在高温下具有较高的热稳定性和化学稳定性,可用于燃烧后碳捕集。在催化双相碳酸酯膜反应器中整合碳捕集和甲烷干重整(DRM),使其作为单一装置用于合成气生产,是一个新兴的研究领域。本文旨在全面综述双相碳酸酯膜和膜反应器在碳捕集和合成气生产方面的研究进展。本文从多方面(即材料选择、膜配置、材料改性和操作条件)深入研究了三种碳酸酯膜在二氧化碳分离中的工作机理和性能。此外,还概述了所涉及的反应(即 DRM、甲烷蒸汽重整(SRM)和甲烷部分氧化(POM))和催化剂设计(即以金属氧化物和沸石为支撑的镍基)。报告还详细比较了使用不同类型催化剂生产合成气的催化双相陶瓷-碳酸盐膜反应器的性能。最后,对双相碳酸酯膜和膜反应器开发方面的挑战、建议和未来见解进行了讨论,从而结束了本综述。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Advancements in dual-phase carbonate membranes for carbon capture and syngas production

Advancements in dual-phase carbonate membranes for carbon capture and syngas production

Globally, the rise in the environmental awareness on the reduction of greenhouse gas emissions has spurred the development of carbon capture and utilization (CCU) technologies, including membrane separation. Among the membrane separation technologies, dual-phase carbonate membrane is feasible for post-combustion carbon capture given its high thermal and chemical stabilities at high temperatures. The integration of carbon capture and dry reforming of methane (DRM) in a catalytic dual-phase carbonate membrane reactor to function as a single device for syngas production is an emerging area of research. This paper aims to provide a comprehensive review on the progress of the dual-phase carbonate membranes and membrane reactors in carbon capture and syngas production. The working mechanism and performance of three types of carbonate membranes in CO2 separation from various aspects (i.e., material selection, membrane configuration, modifications on the materials, and operating conditions) are thoroughly examined. Additionally, an overview of the reactions involved (i.e., DRM, steam reforming of methane (SRM), and partial oxidation of methane (POM)) and catalyst design (i.e., nickel-based supported with metal oxides and zeolites) is provided. A detailed comparison of the performance of the catalytic dual-phase ceramic-carbonate membrane reactor using different types of catalysts for syngas production is presented. Finally, the review is concluded with a discussion of the challenges, recommendations, and future insights on the development of dual-phase carbonate membranes and membrane reactors.

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