MCM-68 zeolite with a multi-dimensional pore system, in which 12-ring and 10-ring micropores interconnect and only the 10-ring pores connect with supercages, is a promising catalyst for the propylene production processes. Although the MCM-68 calcined at 800°C after dealumination showed low catalytic activity due to loss of crystallinity, Ce-modification of dealuminated MCM-68 enhanced the stability. By successive calcination at 800°C, selective and long-lived catalyst for dimethyl ether-to-olefin conversion was obtained, and the propylene yield was as high as 46%.Keywords: MCM-68 zeolite | Ce-modification | Dimethyl ether-to-olefin reaction Propylene and its derivatives are important raw materials for chemicals, such as synthetic resins, synthetic rubbers, solvents, pharmaceuticals, surfactants, and perfumes.1 There is concern about supply shortage due to rapid increase in demand of propylene.2 The worldwide production of propylene currently depends on thermal cracking or fluid catalytic cracking (FCC) of naphtha.3,4 The depletion of petroleum resources has recently driven worldwide researchers to utilize non-petroleum fuels such as methane or coal as an alternative. The shale gas revolution has provided tremendous recoverable reserves, which give rise to further demand in methane as a raw material of chemical production as well as an energy source.Methanol (MeOH)-to-olefin (MTO) and dimethyl ether (DME)-to-olefin (DTO) processes have attracted attention due to the increasing availability of MeOH obtained from steam reforming of methane. 5,6 In the 1980s, Mobil applied molecular sieve catalysts for catalytic conversion of MeOH to hydrocarbons for the first time.7 A series of zeolites had been tested during the past decades, which revealed the excellent catalytic performances of SAPO-34 and ZSM-5 in the MTO/ DTO reaction. However, these two catalysts have some limitations in the selective production of propylene. SAPO-34 with chabazite cages connected through 8-ring (8R) windows (CHA topology) 811 suffers from coke deposition, which causes rapid deactivation due to the small pore entrances.
11Although ZSM-5 with 10-10R channel system (MFI topology) 1215 has a high resistance to coke deposition, the selectivity to propylene is relatively low because of its acidic characteristics. 15 Recently, we have reported that MCM-68 zeolite with threedimensional 12-10-10R channel system (MSE topology) 16,17 shows excellent catalytic performance in DTO reaction. 18,19 The relatively large 12R micropores make the MCM-68 highly resistant to coke formation, and its tunable acidity upon dealumination during acid treatments is convenient for realizing high selectivity to propylene. 18,19 Hence, MCM-68 zeolite is a useful catalyst for enhancing production of propylene in the MTO/DTO process.Stability is one of the most important factors that influence catalytic activities of zeolite. To enhance the thermal and hydrothermal stabilities of zeolites, in general, various approaches like steaming treatment, 2022 rare-earth ion-exchange...