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evaluation of CO2 utilisation for fuel production

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evaluation of CO2 utilisation for fuel production ( evaluation-co2-utilisation-fuel-production )

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3.3 Synthesis of methanol using captured CO2 There exist two catalytic routes to synthesise MeOH from CO2: direct hydrogenation of CO2 with H2 or CO2 conversion into CO and further hydrogenation of CO [100]. MeOH can be also produced electrochemically by CO2 reduction and H2O oxidation [101]. Methanol can be a product of CO2 reduction and water oxidation in a fuel cell, producing oxygen as by-product [102]. There is also a line of research considering solar energy as the source of CO2 reduction with H2O in a compacted photo-electrochemical cell [103]. Methanol synthesis from captured CO2 is moving forward: Iceland and Japan have different plants that combine CO2 and renewable H2 [17]. Carbon Recycling International (CRI) started the operation of its first commercial demonstration plant in Iceland, in 2011, with the aim of improving plant economics for larger plants and of gaining operational expertise [104]. This plant has the particular advantage that its location gives it access to very low-cost electricity from geothermal energy sources and CO2 from the geothermal source [1]. Its capacity is about 5 Mt MeOH/yr. Moreover, CRI has had a pilot plant operating since 2007. The company is involved in a Horizon 2020 project aiming to use surplus and intermittent renewable energy sources to produce chemicals and fuels from CO2 from coal power plants. The study will focus on the deployment of fast response electrolysers [104]. Mitsui Chemicals Inc., in 2008, built a pilot plant to synthesise MeOH from CO2 and H2 in Osaka, with a capacity of around 100 t MeOH/yr. The installation uses CO2 emitted from factories and H2 obtained from water photolysis. The purpose of the MeOH produced is to synthesise olefins and aromatics [105]. Methanex, a leading MeOH company, expressed its interest in MeOH produced from CO2, becoming a shareholder of CRI in July 2013 [106], [107]. Moreover, CRI has also attracted attention from the northern European oil company Argos, which started to sell gasoline blended with MeOH from CRI in the Netherlands, in February 2013 [108]. The existence of the CRI and Mitsui Chemicals Inc. plants allows us to conclude a TRL of 6-7 for MeOH synthesis from CO2. As such, R & D is crucial to move towards a competitive CDU process, from the most fundamental research level (e.g. [109], research on catalysts) to integrated studies at conceptual design level (e.g. [110], complete plants). 3.4 Methanol CDU process simulation in CHEMCAD The MeOH synthesis process can be separated into three different stages [67]. In the first stage of the process, the feed gases are compressed up to the reactor feed pressure, using several compression stages with intercooling. In the second stage, the pressurised feed is heated up and fed to the reactor. In the third stage, MeOH is separated from water in a distillation column. Before entering the distillation column, which is operated at ambient pressure, the process stream coming from the reaction section is depressurised. While the main stream is condensed, the unreacted H2 and CO2 are purged from a flash vessel. The process is governed by the two main reactions that occur in the reactor, Eq. (9) and Eq. (10). CO 3H CHOHHO Eq.(9) 2232 CO2  H2 CO  H2O Eq. (10) While Eq. (9) is the one that produces MeOH, Eq. (10) is less desirable as it consumes the feed meant for MeOH formation. The selectivity is pushed towards the MeOH formation by recycling the formed CO together with unreacted H2 after a flash separation of MeOH and water. The heat of reaction can be partially used to heat feed streams. 32

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