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Conversion of n- octane over ZSM-5 zeolites are greatly enhanced by incorporation of 0.35 wt. % Fe, Zn, Zr metals. Hydroconversion rates were conducted at temperature range of 350-500 C, W/F of 14.8 g of catalyst / g. mole of feed / h, and hydrogen / feed = 5:1 (mole : mole). The product selectivity with total conversion was examined at the temperature range under study. The catalyst Zr / H25 M-5 gave the highest selectivity towards aromatization and production of xylenes.
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