Applications of zeolites in catalysis are plagued by strong diffusion resistance,w hich results from limitations to molecular transport in micropores,a cross external crystal surfaces,b ut also across internal interfaces.T he first type of diffusion resistance is well understood, the second is receiving increasing attention, while the diffusion barriers at internal interfaces remain largely unclear.W et ake Pt/Beta catalyzed isomerization of n-heptane as the model system to explore the role of internal diffusion barriers in zeolite catalysis.T he two as-synthesized Pt/Beta catalysts have an identical Pt loading, similar Beta particle sizea nd acidity,b ut different internal structures.AP t/Beta crystal with no observable internal interfaces can be 180 %h igher in activity and 22 %h igher in selectivity than its counterpart with numerous internal interfaces.T his can only be attributed to the strong transport barriers across internal interfaces,a ss upported by directly comparing the apparent diffusivities of the two Beta samples.Microporous zeolite catalysts are widely applied in refinery and petrochemical industries,i ncluding fluid catalytic cracking, alkylation of aromatics,a nd isomerization of alkanes. [1,2] Thewell-defined microporous structure endows zeolites with superior shape selective catalytic properties,onthe one hand, but causes strong diffusion resistance,o nt he other hand. [3,4] Diffusion limitations are am ajor problem in improving the activity,s electivity,a nd stability of zeolitic catalysts.O ne efficient approach to reduce diffusion limitations is to synthesize zeolites with shortened diffusion path length, such as nano-sized zeolite crystals. [5] However,e ven when the diffusion path length is shortened to single-unit-cell thickness ( % 2nm), transport limitations could still persist, due to the presence of outer-surface and internal diffusion barriers. [6,7] Theo uter-surface diffusion barriers have been extensively probed by both experiments and simulations, [6][7][8][9][10][11][12][13][14][15][16] while the effects of internal diffusion barriers are much less well documented.Internal diffusion barriers were discovered when studying mass transfer in very large zeolite crystals (> 10 mm). [17][18][19][20][21] In these studies,abnormal mass transfer behavior was observed, e.g.,u nusual transient concentration profiles.T his behavior could only be explained when accounting for the presence of internal diffusion barriers.Such barriers exist on the internal interfaces between intergrowing components of zeolite crystals and originate from mismatches in structure and pore alignment. [22] Theaforementioned findings have advanced the understanding of internal diffusion barriers in micron-sized zeolite crystals.However,for submicron-sized (0.1-1 mm) and nano-sized (< 0.1 mm) zeolites that are of interest to industry,e ither by themselves or as part of hierarchically structured particles and pellets,k nowledge about internal diffusion barriers is very limited. Moreover,the possible influence of thes...