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      A solar tower fuel plant for the thermochemical production of kerosene from H 2O and CO 2

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          Summary

          Developing solar technologies for producing carbon-neutral aviation fuels has become a global energy challenge, but their readiness level has largely been limited to laboratory-scale studies. Here, we report on the experimental demonstration of a fully integrated thermochemical production chain from H 2O and CO 2 to kerosene using concentrated solar energy in a solar tower configuration. The co-splitting of H 2O and CO 2 was performed via a ceria-based thermochemical redox cycle to produce a tailored mixture of H 2 and CO (syngas) with full selectivity, which was further processed to kerosene. The 50-kW solar reactor consisted of a cavity-receiver containing a reticulated porous structure directly exposed to a mean solar flux concentration of 2,500 suns. A solar-to-syngas energy conversion efficiency of 4.1% was achieved without applying heat recovery. This solar tower fuel plant was operated with a setup relevant to industrial implementation, setting a technological milestone toward the production of sustainable aviation fuels.

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          Highlights

          • Entire process chain from H 2O and CO 2 to solar kerosene realized in a solar tower

          • 50-kW solar reactor demonstrated for ceria-based thermochemical redox splitting

          • Consecutive redox cycling produced syngas suitable for FT synthesis

          • 4.1% solar-to-syngas energy efficiency achieved without implementing heat recovery

          Context & scale

          The aviation sector, which strongly relies on fossil-derived kerosene, is responsible for vast amounts of anthropogenic greenhouse gas emissions. To avoid these emissions, solar energy can be leveraged to efficiently produce sustainable drop-in fuels, e.g., solar--made synthetic kerosene, which is fully compatible with the existing global jet fuel infrastructures for its storage, distribution, and end-use in jet engines. This work advances the technological readiness level of solar fuels production by demonstrating the technical feasibility of the entire sun-to-liquid fuel process chain, from H 2O and CO 2 to kerosene, in a pilot-scale solar tower. We evaluate the performance of the solar reactor—the cornerstone technology—based on five primary metrics (namely, reaction selectivity, syngas quality, fuel purity, energy efficiency, and material stability) and experimentally validate its stable operation and full integration in the solar tower fuel plant.

          Abstract

          For the first time, the thermochemical production of kerosene using solar energy, water, and CO 2 is demonstrated in a fully integrated solar tower fuel plant. Solar-made kerosene can replace fossil-derived kerosene and further make use of the existing global jet fuel infrastructures and engines, which are particularly critical for the long-haul aviation sector. This pioneer technological demonstration, performed at a pilot scale relevant to industrial implementation, represents a critical milestone on the path toward the production of sustainable aviation fuels.

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          Most cited references38

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          High-flux solar-driven thermochemical dissociation of CO2 and H2O using nonstoichiometric ceria.

          Because solar energy is available in large excess relative to current rates of energy consumption, effective conversion of this renewable yet intermittent resource into a transportable and dispatchable chemical fuel may ensure the goal of a sustainable energy future. However, low conversion efficiencies, particularly with CO(2) reduction, as well as utilization of precious materials have limited the practical generation of solar fuels. By using a solar cavity-receiver reactor, we combined the oxygen uptake and release capacity of cerium oxide and facile catalysis at elevated temperatures to thermochemically dissociate CO(2) and H(2)O, yielding CO and H(2), respectively. Stable and rapid generation of fuel was demonstrated over 500 cycles. Solar-to-fuel efficiencies of 0.7 to 0.8% were achieved and shown to be largely limited by the system scale and design rather than by chemistry.
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            The Fischer–Tropsch process: 1950–2000

            Mark E Dry (2002)
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              Concentrating solar thermal power and thermochemical fuels

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                Author and article information

                Contributors
                Journal
                Joule
                Joule
                Joule
                Cell Press
                2542-4351
                20 July 2022
                20 July 2022
                : 6
                : 7
                : 1606-1616
                Affiliations
                [1 ]Department of Mechanical and Process Engineering, ETH Zurich, 8092 Zurich, Switzerland
                [2 ]Unit of High-Temperature Processes, IMDEA Energy, 28935 Móstoles, Spain
                [3 ]HyGear Technology and Services B.V., 6827 AV Arnhem, the Netherlands
                [4 ]Institute of Future Fuels, German Aerospace Center (DLR), 51147 Cologne, Germany
                [5 ]Bauhaus Luftfahrt e.V., 82024 Taufkirchen, Germany
                Author notes
                []Corresponding author erik.koepf@ 123456dupont.com
                [∗∗ ]Corresponding author aldo.steinfeld@ 123456ethz.ch
                [6]

                Lead contact

                Article
                S2542-4351(22)00286-0
                10.1016/j.joule.2022.06.012
                9332358
                35915707
                345a9363-612b-48b9-bb97-ffe4d56c2ba2
                © 2022 The Author(s)

                This is an open access article under the CC BY license (http://creativecommons.org/licenses/by/4.0/).

                History
                : 4 March 2022
                : 6 May 2022
                : 10 June 2022
                Categories
                Article

                concentrated solar energy,thermochemical,solar fuels,kerosene,solar reactor,redox cycle,water splitting,co2 splitting,ceria,sustainable aviation fuels.

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