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Solid-Acid Catalytic Conversion of Oil Shale: Effects of Sulfonic Acid Grafting on Oil Yield Enhancing and Quality Improvement

[Image: see text] Oil shale is a promising unconventional resource and in situ upgrading technology has been a practical approach for enhancing oil and gas recovery. Mineral-based clin/SBA-15 has been prepared and subsequently functionalized to get SO(3)H-SBA-15 catalysts. Compared with the noncatal...

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Detalles Bibliográficos
Autores principales: Meng, Xianglong, Qi, Zhilei, Yu, Cong, Bian, Junjie, Ma, Zhongliang, Long, Qiulian, Su, Jianzheng
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2021
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7931414/
https://www.ncbi.nlm.nih.gov/pubmed/33681622
http://dx.doi.org/10.1021/acsomega.0c06264
Descripción
Sumario:[Image: see text] Oil shale is a promising unconventional resource and in situ upgrading technology has been a practical approach for enhancing oil and gas recovery. Mineral-based clin/SBA-15 has been prepared and subsequently functionalized to get SO(3)H-SBA-15 catalysts. Compared with the noncatalytic conversion of oil shale under subcritical water, sulfonic acid grafted catalysts have played a predominant role in enhancing the oil yield by 3–16% and improving oil qualities. The O/C atomic ratio was declined to 0.10–0.11, while the hydrocarbon yield was sharply increased to 47–60% from 34%. The energy recovery has been elevated to 75–82%, and the produced oil had a heating value of 35–37 MJ/kg. Compared with that without catalyst, the energy recovery rate is 34.55%, and the heating value is 23.61 MJ/kg. The overall oil yield showed a linear trend with respect to the medium and strong acid amounts on SO(3)H-SBA-15 in the aqueous conversion of oil shale. It was indicated that the SO(3)H– group assisted in the depolymerization via the C–C and C–O bond breaking. Upon the addition of SO(3)H-SBA-15, the activation energies of the oil shale catalytic conversation are decreased dramatically to 78 kJ/mol. It provided a practical approach for the in situ upgrading of oil shale under milder reaction conditions.