Thermal conductivity measurements of copper-coated metal hydrides (LaNi5, Ca0.6Mm0.4Ni5, and LaNi4.75Al0.25) for use in metal hydride hydrogen compression systems
Introduction
A significant challenge in the practical use of hydrogen as an energy source is its low energy density. To make hydrogen gas a viable option, high storage pressures are required. Current methods in hydrogen compression typically comprises of mechanical compressors operated on electricity derived from fossils fuels, which poses higher energy costs. With the implementation of metal hydrides for hydrogen compression, energy density and efficiency can be increased while reducing costs. This investigation stems from the ability of metal hydrides to charge and discharge hydrogen at relatively fast rates. In a practical view, this aspect of metal hydrides will become increasingly important as the usage of hydrogen gas becomes more commercialized and the demand spreads to the consumer level. Therefore, improvements in heat and mass transfer are desirable and are highly dictated by the thermal conductivity and permeability of the hydride material [1], [2], [3], [4], [5], [6], [7], [8], [9], [10], [11]. In this experimentation, the metal hydride samples will be processed with a copper encapsulation method of different fractions in order to understand optimization methods.
One of the earliest studies conducted in analyzing the effective thermal conductivity of porous metal hydrides was done by Ron et al., in which LaNi5 powders were immersed in an aluminum matrix (0.075–0.3 mass fraction), activated, compacted into a cylindrical pellet, and subsequently sintered under high pressure (200–300 atm) hydrogen [1]. The thermal conductivity from this method was on the order of 8–23 W/m-K.
An alternative method to the aluminum matrix combined with metal hydride was introduced by Kim et al. [2], [3] where the metal hydride particles are copper-coated by chemical plating and then compacted into cylindrical pellets with varying amounts of Sn binder. In this work, the mass fraction of copper and compaction force was varied from 0.05 to 0.15 and 27.0 to 45.0 kpsi, respectively. The study reported thermal conductivity values of 3–6 W/m-K.
The goal of this study is to supplement the limited data on metal hydrides by experimentally determining the thermal conductivity of various metal hydrides powder beds treated in a similar manner accomplished by Kim et al. while varying the applied force in situ.
Section snippets
Experimental setup
In approaching the quantification of the thermal conductivity of porous metal hydride samples, an apparatus was constructed to make such experimental measurements possible. The apparatus implements the comparative method of thermal conductivity measurements. The test sample is placed between two reference materials (i.e., copper) with well-established thermal conductivities. Its strength allows for variances in compaction pressure of the sample. A constant cold temperature heat sink can be
Results
The resulting data for LaNi5 in a raw powder (virgin intermetallic) form and also coated in 40 and 50 s processes is shown in Fig. 7. The thermal conductivity data displays a strong correlation between the compaction pressure and the coating of copper. With greater pressure, the thermal conductivity increases, as expected, since the contact area between the particles increases and the void spaces decrease. It is also important to note that the length of the sample was adjusted with the
Discussion
Porous metal hydride powders were tested for their thermal conductivity, with variations in testing parameters. The three different metal hydrides used were LaNi5, Ca0.6Mm0.4Ni5, and LaNi4.75Al0.25 with copper coating process varying from 30, 40, 50, and 60 s. While the thermal conductivity data for Ca0.6Mm0.4Ni5 and LaNi4.75Al0.25 are limited for comparison purposes, they were found to have values ranging from 0.80 to 2.82 W/m-K and 1.78 to 4.29 W/m-K, respectively. On the other hand, the thermal
Acknowledgements
The authors extend sincere thanks for the financial support from the U.S. Department of Energy via National Renewable Energy Laboratory in connection with the NSWEP program (NDJ-6-66271-01).
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