Solar electricity via an Air Brayton cycle with an integrated two-step thermochemical cycle for heat storage based on Co3O4/CoO redox reactions III: Solar thermochemical reactor design and modeling

Solar Energy ◽  
2017 ◽  
Vol 150 ◽  
pp. 584-595 ◽  
Author(s):  
Andrew J. Schrader ◽  
Gianmarco De Dominicis ◽  
Garrett L. Schieber ◽  
Peter G. Loutzenhiser
Author(s):  
Evgeny Shafirovich ◽  
Allen Garcia

CO2 utilization for the production of valuable chemical products may help mitigate two global problems: increasing CO2 concentration in the atmosphere and depleting petroleum resources. Solar thermochemical cycles for CO2 splitting provide relatively high efficiencies of solar energy conversion while operating at realistic temperatures. In the present paper, the cycles proposed previously are reviewed and a novel cycle, based on SnO2/SnO redox reactions, is proposed. The results of thermodynamic calculations for the CO2 reduction step in this cycle are reported.


Materials ◽  
2010 ◽  
Vol 3 (11) ◽  
pp. 4922-4938 ◽  
Author(s):  
Peter G. Loutzenhiser ◽  
Anton Meier ◽  
Aldo Steinfeld

Solar Energy ◽  
2019 ◽  
Vol 179 ◽  
pp. 30-36 ◽  
Author(s):  
Mingkai Fu ◽  
Tianzeng Ma ◽  
Lei Wang ◽  
Shaomeng Dai ◽  
Zheshao Chang ◽  
...  

Solar Energy ◽  
2010 ◽  
Vol 84 (9) ◽  
pp. 1555-1566 ◽  
Author(s):  
S. Tescari ◽  
N. Mazet ◽  
P. Neveu

Author(s):  
Peter G. Loutzenhiser ◽  
M. Elena Ga´lvez ◽  
Illias Hischier ◽  
Anastasia Stamatiou ◽  
Aldo Steinfeld

Using concentrated solar energy as the source of high-temperature process heat, a two-step CO2 splitting thermochemical cycle based on Zn/ZnO redox reactions is applied to produce renewable carbon-neutral fuels. The solar thermochemical cycle consists of: 1) the solar endothermic dissociation of ZnO to Zn and O2; 2) the non-solar exothermic reduction of CO2 with Zn to CO and ZnO; the latter is the recycled to the 1st solar step. The net reaction is CO2 = CO + 1/2 O2, with products formed in different steps, thereby eliminating the need for their separation. A Second-Law thermodynamic analysis indicates a maximum solar-to-chemical energy conversion efficiency of 39% for a solar concentration ratio of 5000 suns. The technical feasibility of the first step of the cycle has been demonstrated in a high-flux solar furnace with a 10 kW solar reactor prototype. The second step of the cycle is experimentally investigated in a hot-wall quartz aerosol flow reactor, designed for in-situ quenching of Zn(g), formation of Zn nanoparticles, and oxidation with CO2. The effect of varying the molar flow ratios of the reactants was investigated. Chemical conversions were determined by gas chromatography and X-ray diffraction. Chemical conversions of Zn to ZnO of up to 88% were obtained for a residence time of ∼ 3.05 s. For all of the experiments, the reactions primarily occurred outside the aerosol jet flow on the surfaces of the reaction zone.


Author(s):  
Cedric Ophoff ◽  
Nesrin Ozalp ◽  
David Moens

Abstract Current state-of-the-art development of concentrated solar power (CSP) applications target cost-effective and highly efficient processes in order to establish commercialization of these technologies. The design of solar receivers/reactors and their respective flow configuration have a direct impact on the operational performance of the solar thermochemical processes. Thermal efficiencies, reaction kinetics and other key output metrics are the intrinsic result of the chosen configuration. Therefore, reactor design optimization plays a crucial role in the development of solar thermochemical applications. In this study a computational fluid dynamics (CFD) model of a directly-irradiated cavity receiver has been developed. The CFD-domain is coupled with incoming radiation that is obtained by using Monte Carlo Ray Tracing (MCRT). Experimental campaigns of the cavity receiver were carried out using a 7 kW High Flux Solar Simulator (HFSS) as radiative source. Temperature readings were obtained at different locations inside the cavity receiver for both wall and gas temperatures. In order to mimic naturally changing insolation conditions, the HFSS was run at different power levels. Heat flux at the aperture of the solar receiver was experimentally characterized. The acquired heat flux maps validated the intermediate results obtained with the MCRT method. The coupled computational model was validated against the measured temperatures at different locations inside the receiver. Computed temperature contours inside the receiver confirmed the experimentally observed non-uniformity of the axial temperature distribution. The validated analysis presented in this paper was then used as a baseline case for a parametric study. Design optimization efforts were undertaken towards obtaining temperature uniformity and achieving efficient heat transfer within the fluid domain. Enhanced flow circulation was achieved which yielded temperature uniformity of the receiver at steady state conditions. The outcome of this parametric analysis provided valuable insights in the development of thermal efficient solar cavity receivers. Hence, findings of this study will serve as a starting point for future solar reactor design. For example, it was found that reversing flow direction has an adverse effect on the temperature uniformity inside the receiver. Similarly, increasing the inlet angle does not positively affect the temperature distribution and hence should be chosen carefully when designing a solar reactor.


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