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Chapter 3. Sustainable Hydrocarbon Fuels by Recycling CO2 with Renewable/Nuclear Energy 73 fuel production process, but at present the energy demand and need for moving a lot of materials render these methods less economical. Electrolytic regeneration with byproduct H2 production may become feasible with further developments of the electrolytic cell. We choose the humidity swing method for this study. Of the dissociation technologies reviewed, high temperature electrolysis using solid oxide cells appears to be one of the most promising (section 3.2.2.3.2). Recent developments and performance improvements have brought solid oxide electrolysis cells close to practical implementation. Efficient co-electrolysis of H2O and CO2 has been demonstrated with low cell degradation rates [37, 38] (and see Chapter 4). By supplying the proper ratio of H2O and CO2, syngas can be produced with a composition tailored for catalytic fuel synthesis. Despite the potential heat management complexity and the as yet unproven durability at very high current densities discussed at the end of section 3.2.2.3.2, we choose the solid oxide electrolyzer over other means of dissociation. This is not to say that other means of dissociation are not worthwhile. However, critical aspects of the feasibility of heat and light driven processes have not been sufficiently demonstrated (sections 3.2.2.1, 3.2.2.2, and 3.2.2.4), and because of the inherently more limited current densities of alkaline electrolyzers their capital cost is at present too expensive for intermittent operation (section 3.2.2.3.1). A pathway based on capture of CO2 from the atmosphere, high-temperature co-electrolysis of H2O and CO2, and Fischer-Tropsch synthesis is therefore chosen for the following analysis. Weimer et al first proposed the use of solid oxide cells for a CO2-recycled synthetic fuel cycle [18, 19]. The proposed process used a KOH absorbent to capture CO2 from the air, regenerated the resulting K2CO3 to KOH (releasing CO2) by reacting with CaO and H2O, and calcining the resulting CaCO3 in a thermal absorbent regeneration process. Steam and the captured CO2 are supplied together to a solid oxide cell stack for co-electrolysis, yielding syngas. The syngas is sent to a catalytic methanol synthesis reactor for methanol production. The fuel synthesis is exothermic and the authors note that the waste heat can be used to heat water to produce steam. Here is proposed a similar process along with the energy balance, economic estimate, and discussion about implementing the process, using published experimental data when possible. The differences are the use of a new type of CO2 air capture process which uses far less energy and costs less [2], the use of today’s state-of-the-art solid oxide cells for co- electrolysis, and the use of conventional Fischer-Tropsch synthesis. Isothermal operation of the cells can be attained just above the thermoneutral voltage, taking into account small heat exchange losses as the hot outlet gasses are used to preheat the inlet gasses. Therefore the cells would operate at slightly lower than the 100% operating efficiency of an electrolysis cell that was mentioned in section 3.2.2.3. The initial internal resistance of the cell stack is assumed to be 0.3 Ω cm2 at 850 °C based on single-cell results [37, 38] and assuming some additional ohmic losses from the stackPDF Image | Electrolysis of CO2 and H2O
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