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Hybrid Fuel Cell Supercritical CO2 Brayton Cycle CO2 Storage

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Hybrid Fuel Cell Supercritical CO2 Brayton Cycle CO2 Storage ( hybrid-fuel-cell-supercritical-co2-brayton-cycle-co2-storage )

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Energies 2020, 13, 5043 2 of 20 Dual chambered solid oxide fuel cells (DC-SOFC) are highly efficient, but suffer from limited fuel flexibility due to carbon coking with hydrocarbon fuels [15]. Fuel reformers or catalysts address coking but increase complexity and cost. DC-SOFC also have low thermal endurance leading to sealant failure and performance reduction under cycling load [16,17], so they are not a good candidate for long-term practical applications. Flame-assisted fuel cells (FFC), and the related direct flame fuel cells (DFFCs) [18–22], were developed to overcome the limitations of DC-SOFC [23–29]. In the FFC setup, fuel-rich combustion (i.e., partial oxidation) generates syngas (i.e., H2 and CO), which generates power in the SOFC [28]. Lean combustion of the remaining fuel maximizes heat recovery [28,30]. Integration of FFC with NG fueled combustion subsystems can lead to improvements in thermal cycling and an increase in the overall system efficiency while reducing the complexity and cost compared to a DC-SOFC system [25,29,31]. Recently, a paper investigating the integration of FFC with an air Brayton cycle has shown a significant increase in net electrical efficiency due to the integration [32]. Along the same lines, the FFC with a sCO2 turbine, proposed in this paper, aims to achieve electrical efficiency gains at a lower cost compared to integration with a traditional SOFC system. Further decrease in CO2 emissions can be achieved by CO2 sequestration, which has been investigated recently [33–35]. Integrating CO2 sequestration with common power cycles leads to efficiency and cost penalties [36,37], which must be minimized. The approach we examine here relies on low temperature (323–473 K depending on the material) thermally-driven adsorption/desorption cycle for air separation [38,39] to provide pure oxygen to the power cycle. Using pure oxygen produces an exhaust stream containing only CO2 and water vapor, which after condensing the water vapor, is sequestration-ready. In the activation step of the sorption cycle, a high surface area solid sorbent with adsorbed oxygen is heated, leading to O2 desorption. In the pumping step, oxygen from air exothermically chemisorbs on the surface (either molecular or dissociative) [38]. Due to the low temperature requirement, the heat required for the activation step can make use of the heat rejected by the sCO2 cycle. With CO2 removal from the exhaust, the FFC-sCO2 turbine hybrid (FFCTH) can be a zero carbon emissions power and heat generation system. Here, we analyze the combined approach to emissions-free, CO2 sequestration-ready, NG power generation, via the integration of a FFC and sorption air separation, with a sCO2 Brayton cycle. The FCC and sCO2 turbine generates power; heat recovery makes this FFCTH a combined heat and power (CHP) system. This analysis investigates the benefits of the FFCTH integration showing a plausible path to zero emissions, high efficiency, combined heat, and power. 2. Theory This section establishes the theory of the overall concept and the individual components in the FFCTH. We first show a detailed analysis of the contribution from each component in the overall system. Following this component analysis, we provide a description of the experimental setup for testing the FFC along with the materials and methods used to conduct the experiment. Lastly, we use the results from the experiments in the theoretical analysis to evaluate the concept further. 2.1. Theoretical Basis: sCO2 Cycle, FFCs, Air Separation, and System Level 2.1.1. Standard sCO2 Brayton Cycle This section reviews the theory of a standard sCO2 Brayton cycle with recuperation and recompression, to provide a baseline for performance of a standalone sCO2 cycle. Figure 1 shows a schematic of a standard sCO2 cycle with recuperation and recompression [40]. At state 1, 53% of CO2 at a pressure of 7.5 MPa and a temperature of 300 K enters the system where it is compressed to a higher pressure and reaches state 2. Meanwhile, the secondary compressor compresses the rest of the CO2, which starts at the same pressure, but higher temperature and reaches state 2a.

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