| People | Locations | Statistics |
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| Naji, M. |
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| Motta, Antonella |
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| Aletan, Dirar |
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| Mohamed, Tarek |
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| Ertürk, Emre |
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| Taccardi, Nicola |
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| Kononenko, Denys |
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| Petrov, R. H. | Madrid |
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| Alshaaer, Mazen | Brussels |
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| Bih, L. |
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| Casati, R. |
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| Muller, Hermance |
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| Kočí, Jan | Prague |
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| Šuljagić, Marija |
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| Kalteremidou, Kalliopi-Artemi | Brussels |
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| Azam, Siraj |
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| Ospanova, Alyiya |
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| Blanpain, Bart |
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| Ali, M. A. |
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| Popa, V. |
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| Rančić, M. |
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| Ollier, Nadège |
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| Azevedo, Nuno Monteiro |
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| Landes, Michael |
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| Rignanese, Gian-Marco |
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Spallina, Vincenzo
in Cooperation with on an Cooperation-Score of 37%
Topics
Publications (10/10 displayed)
- 2022Techno-economic assessment of blast furnace gas pre-combustion decarbonisation integrated with the power generationcitations
- 2021A Ca-Cu chemical loop process for CO2 capture in steel mills: system performance analysis
- 2021A Ca-Cu chemical loop process for CO2 capture in steel mills
- 2020Advanced Packed-Bed Ca-Cu Looping Process for the CO2 Capture From Steel Mill Off-Gasescitations
- 2020Advanced Packed-Bed Ca-Cu Looping Process for the CO2 Capture From Steel Mill Off-Gasescitations
- 2020Advanced Packed-Bed Ca-Cu Looping Process for the CO 2 Capture From Steel Mill Off-Gasescitations
- 2016Pre-combustion packed bed chemical looping (PCCL) technology for efficient H2-rich gas production processescitations
- 2016Pre-combustion packed bed chemical looping (PCCL) technology for efficient H 2 -rich gas production processescitations
- 2016Development of highly permeable ultra-thin Pd-based supported membranescitations
- 2016Development of highly permeable ultra-thin Pd-based supported membranescitations
Places of action
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article
Pre-combustion packed bed chemical looping (PCCL) technology for efficient H2-rich gas production processes
Abstract
<p>A novel reactor system is presented and investigated for the production of a hydrogen rich gas stream for power or ammonia production, based on pre-combustion chemical looping (PCCL) technology using dynamically operated packed bed reactors. In this process, the oxygen carrier (OC) is alternately oxidized with a gas mixture of air and steam to produce a H<sub>2</sub>/N<sub>2</sub> product gas stream combining oxidation by air and water-splitting, and subsequently reduced with syngas producing a concentrated CO<sub>2</sub> stream. The process is carried out at elevated pressure, but at intermediate temperature (in the range of 600-900 °C), which allows circumventing the extremely high temperatures required in chemical-looping combustion. In addition, the N<sub>2</sub>/H<sub>2</sub> gas stream can be produced at the required composition for ammonia production, rendering this process also competitive with the conventional ammonia production. A preliminary experimental study has been carried out in a 2 kW<sub>th</sub> packed bed reactor using an iron-based oxygen carrier. The influence of the operating temperature and the initial solid composition during the oxidation cycle on the H<sub>2</sub>-rich gas yield has been investigated. The complete reduction to pure iron reduces the reactivity of the material due to sintering, whereas a controlled reduction to wüstite (FeO) allows to maintain a higher stability of the material, although the oxygen capacity is decreased.A preliminary thermodynamic assessment of the integrated PCCL plant for power production with natural gas has been carried out reaching an electrical efficiency of 49-51.5% (depending on the plant arrangement) with a carbon capture rate above 95%. The main parameter affecting the plant performance was found to be the steam requirement during the oxidation cycle. The comparison with benchmark technologies has confirmed the potential of the PCCL system.</p>