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多组分体系中基于镍基催化剂的发酵气低温甲烷化

Low-temperature methanation of fermentation gas with Ni-based catalysts in a multicomponent system.

作者信息

Yin Jie, Yao Zihui, Zhao Qizhi, Cheng Shikun, Wang Xuemei, Li Zifu

机构信息

School of Energy and Environmental Engineering, Beijing Key Laboratory of Resource-Oriented Treatment of Industrial Pollutants, University of Science and Technology Beijing, Xueyuan Road No.30, Haidian District, Beijing, 100083, People's Republic of China.

出版信息

Biotechnol Biofuels Bioprod. 2024 Jan 28;17(1):12. doi: 10.1186/s13068-023-02455-4.

Abstract

A large amount of greenhouse gases, such as carbon dioxide and methane, are released during the production process of bioethanol and biogas. Converting CO into methane is a promising way of capturing CO and generating high-value gas. At present, CO methanation technology is still in the early stage. It requires high temperature (300-400 ℃) and pressure (> 1 MPa), leading to high cost and energy consumption. In this study, a new catalyst, Ni-Fe/Al-Ti, was developed. Compared with the activity of the common Ni/AlO catalyst, that of the new catalyst was increased by 1/3, and its activation temperature was reduced by 100℃. The selectivity of methane was increased to 99%. In the experiment using simulated fermentation gas, the catalyst showed good catalytic activity and durability at a low temperature and atmospheric pressure. Based on the characterization of catalysts and the study of reaction mechanisms, this article innovatively proposed a Ni-Fe/Al-Ti quaternary catalytic system. Catalytic process was realized through the synergism of Al-Ti composite support and Ni-Fe promotion. The oxygen vacancies on the surface of the composite carrier and the higher activity metals and alloys promoted by Fe accelerate the capture and reduction of CO. Compared with the existing catalysts, the new Ni-Fe/Al-Ti catalyst can significantly improve the methanation efficiency and has great practical application potential.

摘要

在生物乙醇和沼气的生产过程中会释放大量温室气体,如二氧化碳和甲烷。将一氧化碳转化为甲烷是捕获一氧化碳并生成高价值气体的一种有前景的方法。目前,一氧化碳甲烷化技术仍处于早期阶段。它需要高温(300 - 400℃)和高压(>1兆帕),导致成本高和能耗大。在本研究中,开发了一种新型催化剂Ni-Fe/Al-Ti。与普通Ni/AlO催化剂的活性相比,新型催化剂的活性提高了1/3,其活化温度降低了100℃。甲烷的选择性提高到了99%。在使用模拟发酵气的实验中,该催化剂在低温和常压下表现出良好的催化活性和耐久性。基于催化剂的表征和反应机理研究,本文创新性地提出了Ni-Fe/Al-Ti四元催化体系。催化过程通过Al-Ti复合载体与Ni-Fe促进作用的协同实现。复合载体表面的氧空位以及由Fe促进的高活性金属和合金加速了一氧化碳的捕获和还原。与现有催化剂相比,新型Ni-Fe/Al-Ti催化剂可显著提高甲烷化效率,具有很大的实际应用潜力。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/6a71/10823717/8df2aef6e61f/13068_2023_2455_Fig1_HTML.jpg

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