Catalytic cracking of fat by hierarchical zeolite containing mesoporous silica-aluminas using a Curie point pyrolyzer were performed. Most of prepared catalysts showed the higher catalytic activity and selectivity for gasoline than single zeolite. The ratio of multi/single branch in the gasoline fraction reached more than 0.40, which was much larger than that of single zeolite. Catalysts prepared using a larger amount of malic acid developed the mesoporous structure and showed the higher olefin/paraffin ratio and RON compared with single zeolite and a catalyst with microporous structure.