Current Catalysis

Shaobin Wang  
Curtin University
Perth, WA 6845 U1987


Effect of Pyrite Ore in Direct Coal Liquefaction Process

Author(s): Felipe G. Santos, Humberto G. Riella, Maria Ana P. M. Martins and Ricardo Vieira

Affiliation: Combustion and Propulsion Laboratory, Brazilian Institute for Space Research (INPE), Rodovia Presidente Dutra km 40, 12630-000 Cachoeira Paulista, SP, Brazil.

Graphical Abstract:


The catalytic activity of pyrite ore from coal mining was studied in the direct liquefaction process of high volatile bituminous coal from the south of Brazil. The process consisted of mixing pulverized coal with tetralin in the presence of catalyst. It was possible to obtain fractions of preasphaltenes, asphaltenes, and oils. Pressure had little influence on the direct coal liquefaction process, while temperature had a strong effect on liquefaction yields. The results of total conversions obtained were nearly 16 % at 300 °C, 26.5 % at 350 °C and 38.5 % at 380 °C, in spite of high inertinite-group maceral content (34 vol.%). The pyrite ore catalyst had a fundamental role in this reaction, leading to thermal cracking of the coal structure and hydrogenation of the fragments. However, the most significant result related to catalyst presence was the increase in selectivity of the oil fraction.

Keywords: Conversion, direct coal liquefaction, pyrite, selectivity.

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Article Details

Page: [255 - 259]
Pages: 5
DOI: 10.2174/2211544703666140221004610