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The main disadvantage of the CD process is the severe catalyst-liquid mass transfer resistance of the CD column and the inability to control temperature independently from pressure.
In subsequent cycles the hydrogen purity drastically decreased as a result of severe catalyst poisoning by Li.
Besides the hydrogenation some dehydrogenation to naphthalene was observed in addition to severe catalyst deactivation.
Stiffer diffusion media, enabling more uniform compression under the channels and lands, can mitigate surface cracks, but flexible cloth diffusion media experienced severe catalyst layer surface damage.
Reactant mixtures with CO2/CH4 ratios close to 2 offered the best results: high H2 recovery yields (above 95%) and lower carbon deposition in the catalysts under the severe conditions imposed by the membrane reactor operation.
Ultra-Deep Hydrodesulfurization (UDHDS) process is considered as one of the subbranches of the conventional HDS process which is conducted in the severe process conditions and using different catalyst to obtain the lower amount of sulfur content.
This continual corrosion process of the CB support leads to a significant thickness reduction of the Pt/CB cathode catalyst layer and the severe detachment of Pt particles from the CB.
Emission control catalysts experience degradation under the severe operating conditions which can negatively impact the product distribution and conversion.
Due to the severe reaction temperatures and short contact time, higher catalyst circulation is required to achieve high conversions [2].
The deactivation is the least severe for those catalysts containing both Pt and Ga.
The Pt0.5/θ-Al2O3 Pt0.5/θ-Al2O3ed severe deacatalystn in alkane dehydrogenation reaction.
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