Experimental data were collected for n-hexane cracking on acidic ultrastable Y (H-USY) zeolite at 673 K which clearly document a change from monomolecular cracking to bimolecular/oligomeric cracking as the reactant partial pressure and contact time (or conversion) increased. Under conditions of low pressure (<0.1 kPa) and low conversion (ca. 0%), the characteristic product distribution of monomolecular cracking, which contained relatively high amounts of methane and ethane, was observed. The rates of methane and ethane production depended only on the hexane partial pressure and remained unaffected by alkene partial pressure over the entire range of conditions studied (0.1-6.2 kPa, 0.3-35% conversion). However, the presence of alkenes, either as product or added in the feed, resulted in bimolecular and oligomeric cracking becoming more important contributors to hexane conversion. Corresponding to this transition, the product distribution showed increased amounts of propane, propene, and higher branched products. Using a new methodology to account for varying adsorption properties with hydrocarbon chain length, the observed reaction rates conformed to a simple kinetic rate expression that incorporated both monomolecular and bimolecular/oligomeric cracking. The results showed that, for H-USY zeolite, the observed rate constant for bimolecular/oligomeric cracking was about 75 times greater per kPa of equivalent propene partial pressure in the gas phase than that for monomolecular cracking at 673 K. This observation emphasizes the importance of making comparisons between solid acids under conditions where the same mechanism dominates.