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Chapter 3. Sustainable Hydrocarbon Fuels by Recycling CO2 with Renewable/Nuclear Energy 71 3.2.3. Catalytic Fuel Synthesis Some of the dissociation processes produce hydrocarbons directly, but in most cases it is simpler and often beneficial to produce one or both components (CO/H2) of syngas and catalyze fuel synthesis from these energy-rich precursors. Fischer-Tropsch synthesis (FTS) was developed in the 1920s and has been used economically as part of coal-to-liquids (CTL) and natural gas-to-liquids (GTL) projects [215]. The reaction can be represented by: 2 H2(g) + CO(g) –CH2–(l) + H2O(g) + 165 kJ (at 400K) [216] where –CH2– is part of a hydrocarbon chain. A variety of hydrocarbons can be produced; chain growth depends on the catalyst, syngas composition, and reactor temperature and pressure. High-temperature (300-350°C) yields gasoline and low molecular mass olefins over Fe-based catalysts while low-temperature reactors (200-240°C) yield diesel and high molecular mass linear waxes over Fe or Co-based catalysts. The water-gas shift reaction competes under certain conditions. Synthesis typically yields hydrocarbon chains with a distribution of chain lengths, up to gasoline- or diesel-like fuel distributions. Methanol can be produced in a Fischer-Tropsch-like reaction. Traditional methanol synthesis is carried out by reforming fossil-derived syngas over a Cu-ZnO/Al2O3 catalyst [26] according to CO(g) + 2 H2(g) CH3OH(l) + 128 kJ (at 298K) with up to 18% CO2 in the syngas. High methanol selectivity requires high pressures and low temperatures. The same catalyst can be used for methanol synthesis from CO2 and H2, according to CO2(g) + 3 H2(g) CH3OH(l) + H2O(g) + 87 kJ (at 298K) [26]. It has been stated that this type of methanol synthesis reactor (not necessarily with this particular catalyst) is commercially available with operating parameters of 50-100 bar and 200- 300 °C [18]. Modified catalysts, such as those with ZrO2-modified Al2O3 supports, show improvements by enhancing the dispersion of the copper particles [208, 217]. Zeolite membrane reactors also show promising results [218]. It has been shown that the carbon source in such methanol synthesis is exclusively CO2 and therefore the reaction mechanism involves hydrogenation of the adsorbed CO2, which proceed through an intermediate species of formate (HCOO-) [219]. Methanol synthesis by CO2 hydrogenation was demonstrated as early as 1927 [220]. Many proposed CO2-derived fuel cycles include methanol synthesis by CO2 hydrogenation (Table 3-1). Methanol-to-gasoline reactors that reform the methanol product to higher hydrocarbons have been investigated. They exhibit varying selectivity, over zeolite catalysts [26]PDF Image | Electrolysis of CO2 and H2O
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