The dehydration of glycerol into acrolein was investigated over small-sized g-Al 2 O 3 prepared by am etal-organic framework (MOF) templated method. The particle size of alumina strongly affected the final physicochemical properties of g-Al 2 O 3 as well as its catalytic activity.T he MOF-derived, small-sized g-Al 2 O 3 (M-Al 2 O 3 )c atalyst exhibited highers tability and highera ctivity in the glycerol dehydration reaction than conventionalb ulk g-Al 2 O 3 andn anorod g-Al 2 O 3 owing to enriched intercrystal mesopores and an abundance of accessible acid sites. M-Al 2 O 3 retained its high glycerol conversion (over 80 %) for nearly 200 h, whereas high acrolein selectivity (74 %) was achieved.With growing concerns about the dwindlingp etroleum reserves and clean-energyt echnology,c onsiderable efforts have been made to replacet raditional petrochemical processing. In this regard, the catalytic processing of biomass to biodiesel has developed rapidly.M arket statisticsr eveal that biodiesel is considered as the major path for glycerolp roduction. [1] Glycerol is one of the top-12p latform chemicals, as it can be converted into value-added chemicals. [2] Acrolein is an important buildingb lock, and the dehydration of glycerolt oa crolein over solid acid catalysts is one of the most feasible alternatives because of its replaceability. [3] Ac onsiderable number of studies on the gas-phase dehydration of glycerol over solid acid catalysts have been undertaken. [4] Metal oxidesare the conventional choice for alcohol dehydration catalysts because of their rich surfacea cidic hydroxy groups. g-Al 2 O 3 is aw ell-known acidic metal oxide, and Kostestkyy et al. [5] suggested that g-Al 2 O 3 was more efficient in catalyzingd ehydration reactions than either titania or zirconia, as determined by theory and experiment. Extensive efforts have been dedicated to the use of g-Al 2 O 3 as ac atalysta nd ac atalysts upport in the glycerold ehydration reactiono wing to its high hydrothermal stability and the fact that it is rich in acid sites. [6] The main challenge in the design of alumina catalysts for the glycerold ehydration reaction lies in overcoming the low selectivity to acrolein and obtaining highers tability for industrial application. [6e] In the case of acrolein selectivity,A lhanash et al. [7] suggested that Brønsted acid sites promoted the generation of acrolein. In the case of catalystl ifetime, coke is closely relatedt oc atalyst stability. [8] Suprune tal. [6f] evaluated the effect of different transition-metal oxides loaded on phosphorus-modified g-Al 2 O 3 .M assa et al. [6e] prepared niobia-a nd tungsten-modified alumina and found that the highests electivity towardsacrolein (70 %) was obtained over an alumina-supported catalyst with equimolar amountso fN b 2 O 5 and WO 3 .H owever,u pt on ow,t he structure-activity relationship over the g-Al 2 O 3 catalyst for glyceroldehydration is still unclear.As mall-sized catalystc oulds ignificantly shorten the average diffusion path length of the particles, which ...