The H2 refueling infrastructure's capital and operating expenses are mostly driven by the cost of hydrogen compression. To effectively address this issue, thermally driven H2 compression using metal hydrides (MH) may be used. For industrial customers who have the required infrastructure, such as H2 pipelines, low-grade heat sources, etc., metal hydride hydrogen compressors (MHHC) are particularly promising. However, the H2 compression cycle time issue is brought on by the poor thermal conductivity of the MH's powder. In the present study, a novel MHHC operating procedure is examined numerically. This procedure offers two possible options: The first is referred to as a “Multiple-Cycle Simultaneous Procedure’ (MCSiP for short), as the MH beds' sensible cooling (or sensible heating) and hydrogen's absorption (or desorption) processes start simultaneously and the final pressure is reached after a number of sub-cycles of compression. The second one, dubbed the ”Multiple-Cycle Sequential Procedure“ (MCSeP for short), is similar to the MCSiP mode except that the MH beds' sensible cooling (or sensible heating) as well as the hydrogen's absorption (or desorption) start out sequentially. To evaluate the impact of this procedure on the compressor’s performance, a theoretical model was established and effectively validated by comparison with experimental results reported in the literature. The simulation findings show that the suggested procedure compresses more hydrogen mass at high pressure and is faster than the other operating methods. For instance, 140 NL H2 at a pressure of 110 bar can be obtained with a 70% reduction in compression time compared to the commonly used operating mode utilizing 1.0 kg of MmNi4.6Al0.4 as low pressure MH and 0.832 kg of Ti0.99Zr0.01V0.43Fe0.099Cr0.05Mn1.5 as high pressure MH and operating conditions of 20 bar supply pressure, 293 K absorption temperature, and 373 K desorption temperature.
Read full abstract