Dehydrogenation kinetics of MgH2-based hydrogen storage tank at different operating temperatures and mass flow rates |
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Affiliation: | 1. School of Chemistry, Institute of Science, Suranaree University of Technology, Nakhon Ratchasima, 30000, Thailand;2. National Nanotechnology Center (NANOTEC), National Science and Technology Development Agency (NSTDA), Pathum Thani 12120, Thailand;3. Synchrotron Light Research Institute (Public Organization), Nakhon Ratchasima, 30000, Thailand;4. Research Network NANOTEC-SUT on Advanced Nanomaterials and Characterization, School of Chemistry, Suranaree University, Nakhon Ratchasima, 30000, Thailand |
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Abstract: | The most efficient electrical production from fuel cells integrated with hydride-based hydrogen storage tanks is obtained from suitable dehydrogenation kinetics, facilitating constant flow rate of hydrogen supply for a long period of time. Dehydrogenation kinetics of hydride-based tanks depends strongly on operating temperatures and system pressures, relating to hydrogen mass flow rate (H2-FR) released from the tank. Since a cylindrical tank (96.2 mL) mounted with central heat exchanger containing TiF4-MWCNT-MgH2 (~45 g) shows excellent de/rehydrogenation and reversibility (5.4 wt % H2 upon 20 cycles), the effects of different operating conditions (T = 300–340 °C and H2-FR = 0.6–1.0 standard L/min) on kinetic properties of this MgH2-based tank are of significant interest. Kinetic properties either rapid or steady-state desorption can be optimized by tuning the operating temperature and H2-FR simultaneously. Moreover, the performances in the axial and radial directions of the tank as well as kinetic behaviors and rate-limiting step during dehydrogenation at different temperatures and H2-FR of MgH2-based tank are investigated. |
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Keywords: | Hydrides Transition metals Carbon Kinetic models Rate-limiting step |
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