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The same production rate as in the slurry reactor is achieved using 62% less catalyst.
The second ethanolysis stage of the best RSM product required 50% less ethanol and 90% less catalyst consumption.
Among these are higher productivity and yield, smaller reactor volume, less catalyst, lower pressure drop, and improved sensitivity and control.
During the treatment, the molten salt redistributes to a configuration that has less catalyst available for accelerating the soot oxidation.
For the monolithic reactor a more than 3 times higher volumetric productivity is obtained with much less catalyst.
The useful lifetime can be nearly doubled at the pellet scale, and increased by 40% at the reactor scale, while using 29% less catalyst compared to a non-optimized purely mesoporous catalyst.
Similar(47)
For the same reforming-side gas hourly space velocity, the study has shown that the CPR designed with the segmented catalysts requires 66% less combustion-catalyst to achieve similar methane conversion and hydrogen yield in MSR compared to the conventional CPR design.
Alternate conditions with a less hydrophobic catalyst, CuBr2 with a 2,2′-bipyridine (bpy) ligand, result in a non-degradable polyHIPE.
Increasing the Cu loading to 10.1 wt% resulted in a less active catalyst (Cat-C) than for Cu loadings less than 10 wt%.
This effect was assigned to a better temperature control and less significant catalyst deactivation during the startup of the single channel milli-fixed bed reactor.
However, straight application of the hydrated molybdate precursor followed by in situ nitriding with 3/1 H2/N2 at 700 °C for 2 h produced a less active catalyst which, although containing some Co3Mo3N, comprised additional phases [38].
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