Yayın: Catalytic semi-continuous operation modes for hydrogen generation from carbon derivatives of ammonia boranes
| dc.contributor.author | Coskuner, Ozge | |
| dc.contributor.author | Figen, Aysel Kanturk | |
| dc.date.accessioned | 2026-06-27T14:47:35Z | |
| dc.date.issued | 2022 | |
| dc.description.abstract | In the present study, the semi-continuous regime is evaluated for generating hydrogen (H-2) from carbon derivatives of ammonia borane (AB) via hydrolysis in presence of cobalt-doped activated carbon catalyst (Co-AC). Methylamine borane (MeAB) and ethane 1,2 diamine borane (EDAB) is used as an H-2 storage medium. At first, catalytic activity tests are performed between 20 degrees C and 80 degrees C. 0.2 M MeAB, EDAB, and also AB are hydrolyzed with - Co-AC catalyst, and the results are compared in two temperature regions. EDAB shows the lowest hydrogen generation rate at 64.38 mLH(2)/min.g(Co-AC) of all carbon derivatives of AB due to its higher thermal stability. The power-law model is used to describe the kinetic rate and activation energy (E-a) for all the reactants in the catalytic hydrolysis reaction and the reaction kinetics studied in two temperature regions as the low-temperature region (20-50 degrees C) and the high-temperature region (60-80 degrees C). The zero-order kinetic model describes each temperature region for each reactant. The E-a values of AB, MeAB, and EDAB are calculated as in the range of 48-65 kJ mol(-1) for the low-temperature region and in the range of 33-51 kJ mol(-1) for the high temperature region. The semi-continuous regimes were performed at 60 degrees C with the same amount of AB, MeAB, EDAB, and Co-AC catalyst used for catalytic activity tests. The hydrogen generation rates for the semi-continuous regime are calculated to be 2.46 L/h, 0.86 L/h, and 0.17 L/h for AB, MeAB, and EDAB, respectively. The used catalysts and the exhaust solutions are also characterized. After the semicontinuous regime, the characterization results show that Co-AC is stable and Co species does not leach into the exhaust solution. Also, boron is accumulated on the catalyst observed due to by-product formation during the hydrolyses. (c) 2022 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved. | en |
| dc.description.sponsorship | Yildiz Technical University [FBA-2019-3476] | |
| dc.description.uri | https://doi.org/10.1016/j.ijhydene.2022.02.134 | |
| dc.identifier.doi | 10.1016/j.ijhydene.2022.02.134 | |
| dc.identifier.eissn | 1879-3487 | |
| dc.identifier.endpage | 40316 | |
| dc.identifier.issn | 0360-3199 | |
| dc.identifier.issue | 95 | |
| dc.identifier.startpage | 40304 | |
| dc.identifier.uri | https://hdl.handle.net/20.500.14981/64837 | |
| dc.identifier.volume | 47 | |
| dc.identifier.wos | 000907643300003 | |
| dc.language.iso | eng | |
| dc.publisher | PERGAMON-ELSEVIER SCIENCE LTD | |
| dc.relation.ispartof | INTERNATIONAL JOURNAL OF HYDROGEN ENERGY | |
| dc.subject | Activated carbon | |
| dc.subject | Catalyst | |
| dc.subject | Hydrogen | |
| dc.subject | Ammonia borane | |
| dc.subject | Carbon derivatives | |
| dc.subject | CORE-SHELL NANOPARTICLES | |
| dc.subject | HYDROLYTIC DEHYDROGENATION | |
| dc.subject | THERMAL DEHYDROGENATION | |
| dc.subject | METHYLAMINE-BORANE | |
| dc.subject | ETHYLENEDIAMINE BISBORANE | |
| dc.subject | EXPERIMENTAL INSIGHTS | |
| dc.subject | EFFICIENT CATALYSTS | |
| dc.subject | INFRARED-SPECTRA | |
| dc.subject | STORAGE | |
| dc.subject | FTIR | |
| dc.subject | Chemistry | |
| dc.subject | Electrochemistry | |
| dc.subject | Energy & Fuels | |
| dc.title | Catalytic semi-continuous operation modes for hydrogen generation from carbon derivatives of ammonia boranes | |
| dc.type | Article | |
| dspace.entity.type | Publication | |
| local.import.source | WOS |