2025 AIChE Annual Meeting

(193b) Numerical Modeling of Hydrogen Generation from Metal Hydride in a Millimeter-Scale Reactor

Authors

Anthony Dixon - Presenter, Worcester Polytechnic Institute
Andrew Teixeira, Worcester Polytechnic Institute
Maliha A. Marium, Worcester Polytechnic Institute
Matthew J. Kale, University of California, Riverside
William Knaeble, University of California at Berkeley
Hydrogen is an attractive alternative to conventional fuels as it is environmentally friendly, is abundant and has high energy density. Difficulties with storage and transport have hindered its use, especially in remote settings or for transport applications. Metal hydride storage can be effective due to high storage capacity and practical operating conditions, especially using steam hydrolysis for rapid hydrogen generation.1 Many candidate hydride materials have been studied, and lithium aluminum hydride (LAH) has been identified as having high reaction yield and practical energy density.2 However the accompanying high heat release and changes in properties of the material and its solid products present engineering challenges.

To address the practical use of LAH for hydrogen generation, we developed an unsteady 1D heterogeneous model of a millimeter-scale fixed bed reactor, using kinetics derived from literature experiments in a batch reactor for LAH hydrolysis2 along with a simplified lumped particle sub-model, justified by the small size of the particles (< 50 μm). The model has species balances for H2O and H2 and energy balances, in the fluid and particle phases, LAH in the particle phase, and equations for pressure drop and change in total molar flow. The equations were solved in conservation form by the finite element method. The reactor tube dimensions were approximately 0.08 m long, 0.023 m in diameter with wall cooling at 293.15 K. The base case from literature was 5 μm particles and void fraction ε = 0.86.

The resulting species profiles show the progression of the reaction front along the tube. Figure 1 shows the development of the temperature profile with time, for base case conditions. Parametric studies will be presented to show the effect of particle-scale configurations (size, void fraction) and tube-scale configurations (flow velocity, tube diameter) on the hydrogen production rate and the temperature rise.

References

  1. Aiello R, Sharp JH, Matthews MA. Production of hydrogen from chemical hydrides via hydrolysis with steam. J. Hydrogen Energy. 24 (1999) 1123-30.
  2. Eickhoff S. The effects of hydride chemistry, particle size, and void fraction on micro fuel cell performance. Power Sources. 243 (2023) 562-8.