What is the effect of crushing industrial catalysts on their performance?
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We now have industrial catalysts for the oxidation process, which are Raschig ring-type catalysts with a surface coating. Since we intend to use microreactors, we break these industrial catalysts into smaller pieces before inserting them into the microreactors. I would like to ask what effect this crushing has on the catalyst’s performance What if a part of the surface active components is removed?
The conclusion drawn in this way is completely different from the original one.
What if, I mean what if, I used some special method to turn industrial catalysts into small catalysts with uniform particle sizes, and then tested their performance? What would be the result?