Abstract
There is a large worldwide demand for light olefins (C2=–C4=), which are needed for the production of high value-added chemicals and plastics. Light olefins can be produced by petroleum processing, direct/indirect conversion of synthesis gas (CO + H2) and hydrogenation of CO2. Among these methods, catalytic hydrogenation of CO2 is the most recently studied because it could contribute to alleviating CO2 emissions into the atmosphere. However, due to thermodynamic reasons, the design of catalysts for the selective production of light olefins from CO2 presents different challenges. In this regard, the recent progress in the synthesis of nanomaterials with well-controlled morphologies and active phase dispersion has opened new perspectives for the production of light olefins. In this review, recent advances in catalyst design are presented, with emphasis on catalysts operating through the modified Fischer–Tropsch pathway. The advantages and disadvantages of olefin production from CO2 via CO or methanol-mediated reaction routes were analyzed, as well as the prospects for the design of a single catalyst for direct olefin production. Conclusions were drawn on the prospect of a new catalyst design for the production of light olefins from CO2.
Highlights
Light olefins (C2 = –C4 = ) can be produced by steam cracking, fluid catalytic cracking of naphtha, direct/indirect conversion of synthesis gas (CO + H2 ) [1] or by hydrogenation of CO2 using H2 from renewable energy sources [2,3,4]
The main reason is that the catalyst has to be able to simultaneously catalyze the reverse water-gas shift (RWGS) and modified Fischer-Tropsch to olefins (FTO) reactions working under the same operating conditions, and its final behavior depends on several
For the effective olefin formation via FTO or methanol todifficult olefins (MTO) routes, the promising strategy should be the design of tandem catalysts [3]
Summary
The addition of promoters alone cannot increase selectivity to levels of interest for the industry In this regard, multifunctional metal–zeolite catalysts showing enhanced CO2 activation and inhibition of secondary olefin hydrogenation were intensively investigated [3]. The selection of metals is limited to Fe, Co, Pd, Ni and Ru, which are the only ones that show combined factors, such as the type of metals, the selection of supports, the co-catalyst and high activity in the CO2 hydrogenation upon moderate reaction conditions.
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