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| Hauptseite > Publikationsdatenbank > A Solid Oxide Fuel Cell Operating on Liquid Organic Hydrogen Carrier-Based Hydrogen - A Kinetic Model of the Hydrogen Release Unit and System Performance > print |
| Hauptseite > Publikationsdatenbank > A Solid Oxide Fuel Cell Operating on Liquid Organic Hydrogen Carrier-Based Hydrogen - A Kinetic Model of the Hydrogen Release Unit and System Performance > print |
| 001 | 859124 | ||
| 005 | 20240708133014.0 | ||
| 024 | 7 | _ | |a 10.1016/j.ijhydene.2019.03.220 |2 doi |
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| 100 | 1 | _ | |a Peters, Roland |0 P:(DE-Juel1)129901 |b 0 |e Corresponding author |
| 245 | _ | _ | |a A Solid Oxide Fuel Cell Operating on Liquid Organic Hydrogen Carrier-Based Hydrogen - A Kinetic Model of the Hydrogen Release Unit and System Performance |
| 260 | _ | _ | |a New York, NY [u.a.] |c 2019 |b Elsevier |
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| 520 | _ | _ | |a In this paper, a kinetic model for the catalytic dehydrogenation of perhydro dibenzyltoluene (H18-DBT), a well-established Liquid Organic Hydrogen Carrier (LOHC) compound, is presented. Kinetic parameters for hydrogen release at a Pt on alumina catalyst in a temperature range between 260 °C and 310 °C are presented. A Solid Oxide Fuel Cell (SOFC) system model was coupled to the hydrogen release from H18-DBT in order to validate the full sequence of LOHC-bound hydrogen-to-electric power. A system layout is described and investigated according to its transient operating behavior and its efficiency. We demonstrate that the maximum efficiency of LOHC-bound hydrogen-to-electricity is 45% at full load, avoiding any critical conditions for the system components. |
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| 773 | _ | _ | |a 10.1016/j.ijhydene.2019.03.220 |g p. S0360319919312790 |0 PERI:(DE-600)1484487-4 |n 26 |p 13794-13806 |t International journal of hydrogen energy |v 44 |y 2019 |x 0360-3199 |
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