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Furthermore, higher catalyst loads per reactor volume can be achieved with the monolith.
They are comparable to conventional methods or better on the base of mass transfer per reactor volume.
A critical aspect is represented by the restrictions on the specific load of catalyst per reactor volume resulting from the poor adhesion of very thick catalyst layers onto metallic surfaces.
The GSVR exhibited the ability to intensify the biomass pyrolysis process with respect to both production per reactor volume and selectivity toward the desired products, indicating that further investigations with more detailed kinetics and/or experimental reactors is warranted.
Structured packings with catalyst coating typically exhibit low pressure drop compared to the conventional randomly dumped packed bed, as well as excellent heat transfer characteristics, but also have considerably less catalyst inventory per reactor volume.
Productivity comparisons calculated as amount of refolded protein per reactor volume and process time showed that an optimal refolding concentration to achieve highest productivity value is a balance between a rational reactor volume and a reasonable refolding time.
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By definition yield is the amount of H2 produced per amount of substrate consumed (mole of H2/mole of glucose) and HPR is the amount of H2 (ml) produced per unit time and per unit reactor volume (volumetric rate) or per unit biomass (specific rate) [50, 86].
A single-channel microreactor was easier to operate and provide the highest product yield per unit reactor volume compared to the T-shaped and multichannel microreactors.
The purpose was to identify the lower limits of operability, thereby determining the maximum residence time per unit reactor volume for these mesoscale units.
Results were analyzed in terms of overall DBU conversion, TOC conversion, initial reaction rates per unit reactor volume, photonic efficiency and overall process economics.
Results show for the Si-micromonolithic reactor a remarkable improvement of the specific hydrogen production rate (per unit reactor volume and feed flowrate), operating at considerably reduced residence times, due to the increase in contact area per unit volume.
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