期刊
ACCOUNTS OF CHEMICAL RESEARCH
卷 54, 期 8, 页码 1961-1971出版社
AMER CHEMICAL SOC
DOI: 10.1021/acs.accounts.0c00883
关键词
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资金
- Natural Science Foundation of China [91945301, 22072177, 21776296]
- National Key R&D Program of China [2017YFB0602202]
- Program of Shanghai Academic/Technology Research Leader [20XD1404000]
- Key Research Program of Frontier Sciences, CAS [QYZDB-SSW-SLH035]
- Transformational Technologies for Clean Energy and Demonstration, Strategic Priority Research Program of the Chinese Academy of Sciences [XDA21020600]
- Youth Innovation Promotion Association of CAS
- Xin Rui Excellent Young Talents Program of SARI [E054881ZZ1]
Syngas conversion to olefins using Co2C nanoprisms as catalysts shows promising potential for industrial applications by significantly increasing olefins selectivity while decreasing methane production under mild reaction conditions. The unique catalytic behavior of Co2C nanoprisms deviates from traditional FT process and presents a critical step towards efficient production of chemicals. Extensive exploration of the underlying mechanism and the use of various spectroscopic and microscopic investigations contribute to the advancements in Co2C nanocatalyst development.
CONSPECTUS: Syngas conversion is a key platform for efficient utilization of various carbon-containing resources including coal, natural gas, biomass, organic wastes, and even CO2. One of the most classic routes for syngas conversion is Fischer-Tropsch synthesis (FTS), which is already available for commercial application. However, it still remains a grand challenge to tune the product distribution from paraffins to value-added chemicals such as olefins and higher alcohols. Breaking the selectivity limitation of the Anderson-Schulz-Flory (ASF) distribution has been one of the hottest topics in syngas chemistry. Metallic Co-0 is a well-known active phase for Co-catalyzed FTS, and the products are dominated by paraffins with a small amount of chemicals (i.e., olefins or alcohols). Specifically, a cobalt carbide (Co2C) phase is typically viewed as an undesirable compound that could lead to deactivation with low activity and high methane selectivity. Although iron carbide (FexC) can produce olefins with selectivity up to similar to 60%, the fraction of methane is still rather high, and the required high reaction temperature (300-350 degrees C) typically causes coke deposition and fast deactivation. Recently, we discovered that Co2C nanoprisms with preferentially exposed facets of (020) and (101) can effectively produce olefins from syngas conversion under mild reaction conditions with high selectivity. The methane fraction was limited within 5%, and the product distribution deviated greatly from ASF statistic law. The catalytic performances of Co2C nanoprisms are completely different from that reported for the traditional FT process, exhibiting promising potential industrial application. This Account summarizes our progress in the development of Co2C nanoprisms for Fischer-Tropsch synthesis to olefins (FTO) with remarkable efficiencies and stability. The underlying mechanism for the observed unique catalytic behaviors was extensively explored by combining DFT calculation, kinetic measurements, and various spectroscopic and microscopic investigation. We also emphasize the following issues: particle size effect of Co2C, the promotional effect of alkali and Mn promoters, and the role of metal-support interaction (SMI) in fabricating supported Co2C nanoprisms. Specially, we briefly review the synthetic methods for different Co2C nanostructures. In addition, Co2C can also be applied as a nondissociative adsorption center for higher alcohol synthesis (HAS) via syngas conversion. We also discuss the construction of a Co-0/Co2C interfacial catalyst for HAS and demonstrate how to tune the reaction network and strengthen CO nondissociative adsorption ability for efficient production of higher alcohols. We believe that the advances in the development of Co2C nanocatalysts described here present a critic step to produce chemicals through the FTS process.
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