If ?² = 100 and ?² = 10, the number of tanks necessary to model a real reactor as N ideal tanks in series is ____
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State true or false. Kinetics of microbial fermentation cannot be expressed by Monod kinetics.
The hierarchy of phases for the microbes in a fermentation process is ____
With an accumulation of waste formed during the reaction, the value of observed Monod rate constant ____
What is the most important factor to be considered for designing a fluidized bed reactor?
What is the best combination of fluidized bed for fluid catalytic cracking?
What is the maximum range of superficial gas velocity when the TDH of the bed is 0.25m to prevent eluitrition in a circular type fluidized bed reactor?
What is the advantage of fluidized bed over spouted bed and teeter bed in the drying process?
In case of naphtha cracking, use of batch type is better than circulation type fluidized bed?
There is a missing part in the fluidized bed construction shown in figure.1, state the required equipment and if any replacement for that part and possible explanation?
In a fluidized bed reactor, for a specific gas flow rate, any kind of Geldart type particles can be used. True of False?
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