4.5 Article

Effects of oxidation degree of support and phosphorus modification on the catalytic cracking of coal pyrolysis tar by char-supported nickel catalysts

Journal

JOURNAL OF THE ENERGY INSTITUTE
Volume 107, Issue -, Pages -

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.joei.2023.101178

Keywords

Tar cracking; Char-supported nickel catalyst; Oxidation degree of coal char; Ion exchange; Phosphorus additive

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The efficient conversion of low rank coal can be achieved through the pyrolysis process. Tar utilization and associated problems like pipeline blockage can be resolved through cracking and refining of heavy components in tar. This study explores the use of char-supported nickel catalysts to improve the cracking of coal pyrolysis tar, with catalysts prepared by ion exchange method exhibiting the best performance. The addition of phosphorus as a non-metallic additive further enhances the tar cracking activity of the catalysts.
The low rank coal can be converted efficiently when it undergoes the pyrolysis process. The utilization of tar is modified and the problems such as pipeline blockage are solved by cracking and lightning heavy components in tar. In this study, the char-supported nickel (Ni) catalysts were prepared by different Ni loading methods, and the cracking of coal pyrolysis tar was improved by the coal char support with different oxidation degrees. The catalysts prepared by ion exchange method showed better performance for the tar cracking than other methods, which is related to their smaller Ni crystallite size (NCS). The oxidation of H2O2 and HNO3 significantly increased the number of oxygen-containing groups. The intrinsic correlation between oxidation degree of support and catalytic property indicated that the XH2O2-Ni/C (ZD coal pretreated by H2O2) series catalysts had better tar cracking activity than XHNO3-Ni/C (ZD coal pretreated by HNO3) series catalysts, which did not only depend on the increase of Ni loading amounts but also related to the smaller NCS and higher dispersion. Moreover, the nonmetallic additive phosphorus (P) was added to modify the catalysts. It was found that the addition of P significantly improved the tar cracking performance of the 30%H2O2 P-Ni/C catalyst. The amounts of active components loaded and NCS contributed to the production of light tar.

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