recategorized by
0 0 votes
The dimensions and operating condition of a lab-scale fermentor are as follows:

Volume = $1\:L$

Diameter = $20$ cm

Agitator speed = $600$ rpm

Ratio of impeller diameter to fermentor diameter = $0.3$

This fermentor needs to be scaled up to $8,000\:L$ for a large scale industrial application. If the scale-up is based on constant impeller tip speed, the speed of the agitator in the larger reactor is ___________ rpm. Assume that the scale-up factor is the cube root of the ratio of fermentor volumes.

Please log in or register to answer this question.

Answer:

Related questions

0 0 votes
0 0 answers
gatecse asked Feb 23
A packed bed bioreactor with length $1 \text{~m}$ and inside diameter $10 \text{~cm}$ has liquid flowing at an interstitial velocity of $1 \mathrm{~cm} \mathrm{~s}^{-1}$....
0 0 votes
0 0 answers
soujanyareddy13 asked Nov 3, 2020
Yeast biomass $\left ( C_{6}H_{10}O_{3}N \right )$ grown on glucose is described by the stoichiometric equation given below:$$C_{6}H_{12}O_{6}+0.48\:NH_{3}+3\:O_{2} \to 0...
0 0 votes
0 0 answers
soujanyareddy13 asked Nov 3, 2020
Phenolic wastewater discharged from an industry was treated with Pseudomonas $sp$. in an aerobic bioreactor. The influent and effluent concentrations of phenol were $10,0...
0 0 votes
0 0 answers
soujanyareddy13 asked Nov 3, 2020
In a cross-flow filtration process, the pressure drop $\left ( \Delta P \right )$ driving the fluid flow is $2$ atm, inlet feed pressure $\left ( P_{i} \right )$ is $3$ a...
0 0 votes
1 1 answer
soujanyareddy13 asked Nov 3, 2020
An industrial fermentor containing $10,000\:L$ of medium needs to be sterilized. The initial spore concentration in the medium is $10^{6}$ spores $mL^{-1}$. The desired ...