“…control volume c p heat capacity, J kg À1 K À1 C sg hydride capacity, kg H 2 /kg hydride, e b C volumetric hydrogen storage capacity, kg H2 m À3 d average hydride particle size, m DH mass enthalpy of reaction, J kg À1 DH n molar enthalpy of reaction, J mol À1 DS n molar entropy of reaction, J mol À1 K À1 e total energy of control surface/volume, J kg À1 E Abs activation energy, J mol À1 E rea enthalpy of reaction per unit volume, J m À3 ε hydride porosity, e f FC constant proportional to fill criteria, e F heat conductive material fraction, e F volumetric flow, m 3 [41,42] [43e45] [46]*, [47] *Propose some sort of optimization.…”