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The experimental results show that the CO2 conversion could be enhanced with higher catalyst inlet temperatures.
Higher catalyst to ionomer ratio decreases the cell performance at low and medium current densities.
This feature can be attributed to an enhanced electrode|membrane interface in the anode side and significantly higher catalyst efficiency.
It is proved that the use of a higher catalyst loading mostly promotes a higher methanol conversion rate.
Higher catalyst utilization due to easier fuel access and ionomer coverage led to higher fuel cell performance.
A thicker catalyst layer will result in a larger ohmic voltage loss and higher catalyst cost.
Furthermore, higher catalyst loads per reactor volume can be achieved with the monolith.
For fully-passive operation, a higher catalyst loading at the cathode helps retain stable performance when a WBD enhancement layer is used.
Therefore, higher inlet temperatures, longer residence times or higher catalyst dispersions respectively (high amount of active surface sites) favor POX and reforming, which both increase the syngas selectivity.
Higher catalyst to biomass ratios increased the gas yield, at the expense of liquid and solid products, while enhancing aromatic selectivity.
Seeking to reduce the cost due to high process temperatures, the impact of using higher catalyst content (25%) with a lower temperature (500 °C) was investigated.
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