“…Although high glycerol conversion, high desired ether selectivity and low DIB selectivity were obtained with homogenous catalysts, difficulties in catalyst-product separation, corrosion and environmental issues reduced the interest on the commercialization of glycerol ether production. Subsequently, as well as improving the catalytic environment of ion exchange resins [27,29,31,34], different heterogeneous catalysts covering pure or modified wide pore zeolites [25,27,31,34,35,38,40,41,44], functionalized mesostructured materials [28,32,36,46] and other heterogeneous acid catalysts, such as montmorillonite K-10, amorphous microporous mixed oxide [24], sulfonated peanut shell [33], solid heteropolyacids [24,31,39], spherical silica supported Hyflon [37], sulfonated graphene [47], sulfonic acid functionalized aerogels [43], triflic acid supported on gamma alumina [46,48] were elaborated by comparing their performance with acidic ion exchange resins and attempting to understand effects of catalyst structures, such as porosity, surface area, pore size, pore volume, acid capacity, acid strength on catalytic activity, expressed by glycerol conversion, ether selectivity and side product formation.…”