Abstract
The wave reformer, developed by New Wave Hydrogen, Inc. (NWH2), harnesses shock waves resulting from the pressure exchange between two gases to initiate thermal decomposition reactions in a hydrocarbon gas to generate hydrogen. This article investigates the influence of various operating parameters, including driver gas mixtures and operating pressure on the overall hydrogen conversion within an 8-ports wave reformer. The objective is to start with a peak pressure region and reaction zone away from the end-wall toward the center of the wave reformer, allowing for more time for high-temperature initiation.
The main intention of the work is to consider the role of the gas composition of the driver gas (energy input) on the pyrolysis of methane using shock-wave heating. This study provides a comprehensive comparative analysis of the effects of driver gas properties on the flow rate, velocity, temperature, and pressure distribution within the wave reformer. Utilizing a Quasi-2D (Q2D) model, simulations yield valuable insights into how these parameters impact the performance of the technology.
Key findings include the critical role of driven outlet back pressure in driving mass flow within the cycle and its subsequent influence on maximum temperature. Most interestingly, the choice of driver gases was found to profoundly influence the temperature and density fields and plays a significant role in the mass flow ratio of the two gases.
This research enhances our understanding of wave reformer technology and its sensitivity to various operational parameters. The insights gained are instrumental in optimizing wave reformer performance for efficient hydrogen conversion.
