All catalyzed propellants contained the same catalyst mass fraction.
The experimental runs were performed applying a wide range of catalyst mass to molar feed ratios.
No detectable Au was present in the water sample and the Cu concentration was 3.25 ppb (µg l 1), which is <1% of the Cu catalyst mass loading.
In contrast, the performance of methane TCD is relatively insensitive to the catalyst mass, regardless of which reaction stage is.
The effects of reaction (wall) temperature, catalyst mass, and reactant flow rate on the performance of methane TCD are evaluated.
The effect of reaction pressure, temperature, hydrogen peroxide concentration and catalyst mass were investigated.
Interestingly, the normalized catalyst mass loss is independent of the initial catalyst loading under identical conditions.
The effects of solvent, amine concentration, H2 partial pressure, catalyst mass, and reuse were studied.
The catalyst mass activity after feeding only 10%-MWNTs to CB increased by 1.5 and 2 times than those of the MWNTs-based- and CB-based catalysts, respectively.
Catalyst mass distribution, exothermic inlet temperature, operating pressures, number of tubes in the exothermic side and the total molar flow rates are the most important optimized parameters.
Reaction parameters (Copper content, nature of the solvent, hydrogen peroxide concentration, reaction time, catalyst mass and reaction temperature) were evaluated to reach the optimum reaction conditions.
