[a] Increasingly,m ethanol is considered as an important chemical intermediate between coal and natural gas feedstocks and olefinic building blocks used extensively in the chemical industry.Currently,t he methanol-to-olefins (MTO) reaction is the most important in terms of the installed capacity of all methanol-tohydrocarbon reactions. [1][2][3][4] Am icroporous silicoaluminophosphate materialw ith the chabazite (CHA) framework topology (H-SAPO-34)i st he preferred catalystc ommercially.[5] One concern is the predicted scarcity of phosphorus,w hich is contained in typical silicoaluminophosphates up to 20 wt %. [6,7] The higher acidity of SSZ-13, the isostructural phosphorous-free aluminosilicate analogue of H-SAPO-34, presentsa no pportunity to operate the MTO reactiona talower temperature and, in this way,t oi mprove process economics.[8] However,t he stronger acidityr esults in more rapid catalystd eactivation caused by multiring aromaticst hat block the pore system of the zeolite.[9] These multiring aromatics derive from the fusion of aromatic hydrocarbon pool species, which are key reactioni ntermediates of the MTOr eactioni ns mall-pore zeolites.[10] Catalyst stability is impeded by the fact that these deposits form in the outer regions of the zeolite crystalsa nd, accordingly,p reventt he accesso fm ethanolt oi nternal regions.T he introduction of mesopores within zeolite crystals is an elegant way to reduce these negative effects of diffusionl imitations and improve the catalytic performance. [11][12][13] Common and scalable approaches such as steaming and alkaline leaching have an egative effect on MTO performance if applied to SSZ-13 zeolite. [14,15] An understanding of the role of the hierarchical pore architecture of SSZ-13z eoliteso nt he catalytic performance in the methanol-to-olefins (MTO) reactioni sc rucial to guide the design of better catalysts. We investigated the influence of the space velocity on the performance of am icroporous SSZ-13 zeolite and severalh ierarchically structured SSZ-13 zeolites. Single catalytic turnovers, as recorded by nanometera ccuracy by using stochastic chemical reactions (NASCA) fluorescence microscopy verified that the hierarchical zeolitesc ontain pores larger than the 0.38 nm apertures native to SSZ-13z eolite.T he amount of fluorescent events correlated well with the additional pore volume availableb ecause of the hierarchical structuring of the zeolite. Positron emission tomography (PET) using 11 C-labeled methanolw as used to map the 2D spatial distribution of the deposits formed during the MTO reaction in the catalystb ed. We used PET imaging to demonstrate that hierarchical structuring not only improves the utilization of the availablem icroporous cages of SSZ-13 but also that the aromatic hydrocarbon pool species are involved in more turnovers beforet hey condense into larger multirings tructures that deactivate the catalyst.