“…21,22,[26][27][28][29][30] Stronger solid acids such as NaY (Si/Al = 1.3-4.5 molar ratio), ZSM-5 (Si/Al = 14-25 molar ratio) and zeolite beta (Si/Al = 20 molar ratio) were utilized as components of catalyst systems. 26,28,[34][35][36][37]42,[45][46][47][48]52,53,55,59 Moreover, acid-base bifunctional catalyst systems arose, which have both acid and base sites. 27,29,30,[35][36][37][38][41][42][43][44][46][47][48][50][51][52][53][54]56,57 As a result of the presence of stronger solid acid sites which easily induce LA decarbonylation and LA polymerization (which eases coke formation), catalytic stability for the production of AA declined and catalysts deactivated faster than expected, although initial catalytic activity and selectivity were prominent.…”