Experimental investigation of the applicability of a 250 kW ceria receiver/reactor for solar thermochemical hydrogen generation
Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiati...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Thanda, V.K. [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2022transfer abstract |
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| Schlagwörter: |
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| Umfang: |
10 |
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| Übergeordnetes Werk: |
Enthalten in: Technologies and practice of CO - HU, Yongle ELSEVIER, 2019, an international journal : the official journal of WREN, The World Renewable Energy Network, Amsterdam [u.a.] |
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| Übergeordnetes Werk: |
volume:198 ; year:2022 ; pages:389-398 ; extent:10 |
| Links: |
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| DOI / URN: |
10.1016/j.renene.2022.08.010 |
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| Katalog-ID: |
ELV058971343 |
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| 245 | 1 | 0 | |a Experimental investigation of the applicability of a 250 kW ceria receiver/reactor for solar thermochemical hydrogen generation |
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| 520 | |a Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. | ||
| 520 | |a Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. | ||
| 650 | 7 | |a Solar hydrogen production |2 Elsevier | |
| 650 | 7 | |a Thermochemical cycle |2 Elsevier | |
| 650 | 7 | |a Solar fuel |2 Elsevier | |
| 650 | 7 | |a Ceria |2 Elsevier | |
| 650 | 7 | |a Solar hydrogen reactor |2 Elsevier | |
| 650 | 7 | |a Redox reaction |2 Elsevier | |
| 700 | 1 | |a Fend, Th. |4 oth | |
| 700 | 1 | |a Laaber, D. |4 oth | |
| 700 | 1 | |a Lidor, A. |4 oth | |
| 700 | 1 | |a von Storch, H. |4 oth | |
| 700 | 1 | |a Säck, J.P. |4 oth | |
| 700 | 1 | |a Hertel, J. |4 oth | |
| 700 | 1 | |a Lampe, J. |4 oth | |
| 700 | 1 | |a Menz, S. |4 oth | |
| 700 | 1 | |a Piesche, G. |4 oth | |
| 700 | 1 | |a Berger, S. |4 oth | |
| 700 | 1 | |a Lorentzou, S. |4 oth | |
| 700 | 1 | |a Syrigou, M. |4 oth | |
| 700 | 1 | |a Denk, Th. |4 oth | |
| 700 | 1 | |a Gonzales-Pardo, A. |4 oth | |
| 700 | 1 | |a Vidal, A. |4 oth | |
| 700 | 1 | |a Roeb, M. |4 oth | |
| 700 | 1 | |a Sattler, Ch. |4 oth | |
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10.1016/j.renene.2022.08.010 doi /cbs_pica/cbs_olc/import_discovery/elsevier/einzuspielen/GBV00000000001929.pica (DE-627)ELV058971343 (ELSEVIER)S0960-1481(22)01176-4 DE-627 ger DE-627 rakwb eng Thanda, V.K. verfasserin aut Experimental investigation of the applicability of a 250 kW ceria receiver/reactor for solar thermochemical hydrogen generation 2022transfer abstract 10 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. Solar hydrogen production Elsevier Thermochemical cycle Elsevier Solar fuel Elsevier Ceria Elsevier Solar hydrogen reactor Elsevier Redox reaction Elsevier Fend, Th. oth Laaber, D. oth Lidor, A. oth von Storch, H. oth Säck, J.P. oth Hertel, J. oth Lampe, J. oth Menz, S. oth Piesche, G. oth Berger, S. oth Lorentzou, S. oth Syrigou, M. oth Denk, Th. oth Gonzales-Pardo, A. oth Vidal, A. oth Roeb, M. oth Sattler, Ch. oth Enthalten in Elsevier Science HU, Yongle ELSEVIER Technologies and practice of CO 2019 an international journal : the official journal of WREN, The World Renewable Energy Network Amsterdam [u.a.] (DE-627)ELV002723662 volume:198 year:2022 pages:389-398 extent:10 https://doi.org/10.1016/j.renene.2022.08.010 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U AR 198 2022 389-398 10 |
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10.1016/j.renene.2022.08.010 doi /cbs_pica/cbs_olc/import_discovery/elsevier/einzuspielen/GBV00000000001929.pica (DE-627)ELV058971343 (ELSEVIER)S0960-1481(22)01176-4 DE-627 ger DE-627 rakwb eng Thanda, V.K. verfasserin aut Experimental investigation of the applicability of a 250 kW ceria receiver/reactor for solar thermochemical hydrogen generation 2022transfer abstract 10 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. Solar hydrogen production Elsevier Thermochemical cycle Elsevier Solar fuel Elsevier Ceria Elsevier Solar hydrogen reactor Elsevier Redox reaction Elsevier Fend, Th. oth Laaber, D. oth Lidor, A. oth von Storch, H. oth Säck, J.P. oth Hertel, J. oth Lampe, J. oth Menz, S. oth Piesche, G. oth Berger, S. oth Lorentzou, S. oth Syrigou, M. oth Denk, Th. oth Gonzales-Pardo, A. oth Vidal, A. oth Roeb, M. oth Sattler, Ch. oth Enthalten in Elsevier Science HU, Yongle ELSEVIER Technologies and practice of CO 2019 an international journal : the official journal of WREN, The World Renewable Energy Network Amsterdam [u.a.] (DE-627)ELV002723662 volume:198 year:2022 pages:389-398 extent:10 https://doi.org/10.1016/j.renene.2022.08.010 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U AR 198 2022 389-398 10 |
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10.1016/j.renene.2022.08.010 doi /cbs_pica/cbs_olc/import_discovery/elsevier/einzuspielen/GBV00000000001929.pica (DE-627)ELV058971343 (ELSEVIER)S0960-1481(22)01176-4 DE-627 ger DE-627 rakwb eng Thanda, V.K. verfasserin aut Experimental investigation of the applicability of a 250 kW ceria receiver/reactor for solar thermochemical hydrogen generation 2022transfer abstract 10 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. Solar hydrogen production Elsevier Thermochemical cycle Elsevier Solar fuel Elsevier Ceria Elsevier Solar hydrogen reactor Elsevier Redox reaction Elsevier Fend, Th. oth Laaber, D. oth Lidor, A. oth von Storch, H. oth Säck, J.P. oth Hertel, J. oth Lampe, J. oth Menz, S. oth Piesche, G. oth Berger, S. oth Lorentzou, S. oth Syrigou, M. oth Denk, Th. oth Gonzales-Pardo, A. oth Vidal, A. oth Roeb, M. oth Sattler, Ch. oth Enthalten in Elsevier Science HU, Yongle ELSEVIER Technologies and practice of CO 2019 an international journal : the official journal of WREN, The World Renewable Energy Network Amsterdam [u.a.] (DE-627)ELV002723662 volume:198 year:2022 pages:389-398 extent:10 https://doi.org/10.1016/j.renene.2022.08.010 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U AR 198 2022 389-398 10 |
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10.1016/j.renene.2022.08.010 doi /cbs_pica/cbs_olc/import_discovery/elsevier/einzuspielen/GBV00000000001929.pica (DE-627)ELV058971343 (ELSEVIER)S0960-1481(22)01176-4 DE-627 ger DE-627 rakwb eng Thanda, V.K. verfasserin aut Experimental investigation of the applicability of a 250 kW ceria receiver/reactor for solar thermochemical hydrogen generation 2022transfer abstract 10 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. Solar hydrogen production Elsevier Thermochemical cycle Elsevier Solar fuel Elsevier Ceria Elsevier Solar hydrogen reactor Elsevier Redox reaction Elsevier Fend, Th. oth Laaber, D. oth Lidor, A. oth von Storch, H. oth Säck, J.P. oth Hertel, J. oth Lampe, J. oth Menz, S. oth Piesche, G. oth Berger, S. oth Lorentzou, S. oth Syrigou, M. oth Denk, Th. oth Gonzales-Pardo, A. oth Vidal, A. oth Roeb, M. oth Sattler, Ch. oth Enthalten in Elsevier Science HU, Yongle ELSEVIER Technologies and practice of CO 2019 an international journal : the official journal of WREN, The World Renewable Energy Network Amsterdam [u.a.] (DE-627)ELV002723662 volume:198 year:2022 pages:389-398 extent:10 https://doi.org/10.1016/j.renene.2022.08.010 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U AR 198 2022 389-398 10 |
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10.1016/j.renene.2022.08.010 doi /cbs_pica/cbs_olc/import_discovery/elsevier/einzuspielen/GBV00000000001929.pica (DE-627)ELV058971343 (ELSEVIER)S0960-1481(22)01176-4 DE-627 ger DE-627 rakwb eng Thanda, V.K. verfasserin aut Experimental investigation of the applicability of a 250 kW ceria receiver/reactor for solar thermochemical hydrogen generation 2022transfer abstract 10 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. Solar hydrogen production Elsevier Thermochemical cycle Elsevier Solar fuel Elsevier Ceria Elsevier Solar hydrogen reactor Elsevier Redox reaction Elsevier Fend, Th. oth Laaber, D. oth Lidor, A. oth von Storch, H. oth Säck, J.P. oth Hertel, J. oth Lampe, J. oth Menz, S. oth Piesche, G. oth Berger, S. oth Lorentzou, S. oth Syrigou, M. oth Denk, Th. oth Gonzales-Pardo, A. oth Vidal, A. oth Roeb, M. oth Sattler, Ch. oth Enthalten in Elsevier Science HU, Yongle ELSEVIER Technologies and practice of CO 2019 an international journal : the official journal of WREN, The World Renewable Energy Network Amsterdam [u.a.] (DE-627)ELV002723662 volume:198 year:2022 pages:389-398 extent:10 https://doi.org/10.1016/j.renene.2022.08.010 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U AR 198 2022 389-398 10 |
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experimental investigation of the applicability of a 250 kw ceria receiver/reactor for solar thermochemical hydrogen generation |
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Experimental investigation of the applicability of a 250 kW ceria receiver/reactor for solar thermochemical hydrogen generation |
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Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. |
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Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. |
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Solar thermochemical water splitting via a two-stage redox cycle has been subjected to numerous theoretical and experimental studies since a couple of decades. It has been considered as a promising technology to generate green hydrogen as it is feasible to directly convert concentrated solar radiation into storable chemical energy. The present article describes the results of an experimental campaign, which has been carried out to further demonstrate the feasibility of this technology. Based on the prior experience from solar gas turbine projects, a combined receiver/reactor has been designed and built up operating at temperatures between 1400 °C and 1000 °C using radiative power of up to 150 kW generated by a large-scale solar simulator (Synlight). The reactor has a total volume of 90 L with open porous ceramic foam structure. Additionally, high-performance heat exchangers have been used to recover the heat content of the product gases. Typical necessary durations for the sub-cycles, reduction and oxidation as well as durations for the corresponding necessary heating and cooling phases have been determined. By producing up to 8,8 g of hydrogen per cycle it could be shown that the production of hydrogen in a medium scale structured reactor is possible. |
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