“…Fischer–Tropsch synthesis (FTS) is a traditional strategy to convert syngas into hydrocarbons over Fe and Co catalysts; however, the Anderson–Schulz–Flory (ASF) model in FTS limits the selectivity of C 2–4 hydrocarbons (including olefins and paraffins), which is no more than 58%. , Recently, an elegant oxide–zeolite (OX-ZEO) route was proposed to selectively convert syngas into olefins (STO), liquid fuels and aromatics depending on the topologies of the zeolites, , which breaks the ASF distribution in FTS. A number of metal oxides, such as ZnCrO x , , Zn–ZrO 2 , , ZnAlO x ,, and MnGaO x , − and several kinds of zeolites, including SAPO-34, − SAPO-18, , AlPO-18, and SSZ-13, , have been intensively studied. In such an OX-ZEO catalyst system, the metal oxide is responsible for the syngas activation to generate intermediates like methanol and ketene, while the zeolite plays the role in tandem conversion of intermediates to target products .…”