The conversion of propanal on large (2-5 mu m) and small (0.2-0.5 mu m) crystallite HZSM-5 at 400 degrees C and atmospheric pressure has been studied. Improved catalyst stability was observed on small crystallites due to faster removal of products with the shorter diffusion path length, reducing the formation of coke precursors. As previously shown, C-9 aromatics are the initial aromatics produced from propanal via aldol condensation followed by cyclization and these have less opportunity to crack to lighter aromatics on the small crystallites. Thus, a higher ratio of C-9/(C-8+C-7) aromatics was observed on the small crystallites. The main isomer of the C-8 aromatic products observed on small crystallites was the initial cracking product of the C-9 aromatics, and thermodynamically preferred, meta-xylene, while the shape-selective preferred para-xylene was the predominant product on large crystallites. The higher internal diffusion rate of the para isomer results in greater shape selectivity with the longer path of the large crystallite zeolite. It is concluded that the use of smaller crystallite HZSM-5 improves results for production of alkyl aromatics from light oxygenates at mild conditions that may prove useful for bio-oil upgrading. (C) 2010 Elsevier B.V. All rights reserved.