This paper presents the results of experimental and analytical study of the
thermal cycling absorption process (TCAP); which is a metal-hydride-based
hydrogen separation system configured as a helical shell-and-tube heat exch
anger. The column (tube side) is packed with Palladium deposited on kieselg
uhr (Pd/k). This packed column is thermally cycled by a hot and cold nitrog
en gas on its exterior surface (shell side), while a stream of hydrogen mix
ed with other inert gases are passed through the packed column. Hydrogen ga
s is absorbed and desorbed from the Palladium, causing a separation from th
e gas stream. The rate at which the hydrogen is separated depends only on h
ow quickly the Pd/k can be thermally cycled. In this paper we present a tra
nsient heat transfer analysis to model the heat transfer in the Pd/k packed
column. To improve the efficiency of the TPAC, metallic foam was added in
the Pd/k packed column. It was observed that adding metallic foam significa
ntly improved the separation rate of hydrogen. Thermal cycling times for va
rying packed column diameters, materials, and compositions are also determi
ned. Comparison of performance is made between an existing 1.25 in (31.75 m
m) column versus a 2 in (50.8 mm) column tube. A parametric argument is pre
sented to optimize the material selection and geometric design of a TCAP he
at exchanger. (C) 2001 Published by Elsevier Science Ltd. on behalf of the
International Association for Hydrogen Energy.