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book Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler cover

Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler

Edition 2ISBN: 9780130819086
book Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler cover

Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler

Edition 2ISBN: 9780130819086
Exercise 15
Ethanol is to be used as a substrate for single-cell protein production in a chemostat. The
available equipment can achieve an oxygen transfer rate of 10 g Ethanol is to be used as a substrate for single-cell protein production in a chemostat. The available equipment can achieve an oxygen transfer rate of 10 g   of liquid per hour. As- sume the kinetics of cell growth on ethanol is of the Monod type, with     cells/g ethanol, and   We wish to operate the chemostat with an ethanol concentration in the feed of 22 g/L. We also wish to maximize the biomass productivity and minimize the loss of unused ethanol in the effluent. Determine the required dilution rate and whether sufficient oxygen can be provided. of liquid per hour. As-
sume the kinetics of cell growth on ethanol is of the Monod type, with Ethanol is to be used as a substrate for single-cell protein production in a chemostat. The available equipment can achieve an oxygen transfer rate of 10 g   of liquid per hour. As- sume the kinetics of cell growth on ethanol is of the Monod type, with     cells/g ethanol, and   We wish to operate the chemostat with an ethanol concentration in the feed of 22 g/L. We also wish to maximize the biomass productivity and minimize the loss of unused ethanol in the effluent. Determine the required dilution rate and whether sufficient oxygen can be provided. Ethanol is to be used as a substrate for single-cell protein production in a chemostat. The available equipment can achieve an oxygen transfer rate of 10 g   of liquid per hour. As- sume the kinetics of cell growth on ethanol is of the Monod type, with     cells/g ethanol, and   We wish to operate the chemostat with an ethanol concentration in the feed of 22 g/L. We also wish to maximize the biomass productivity and minimize the loss of unused ethanol in the effluent. Determine the required dilution rate and whether sufficient oxygen can be provided. cells/g ethanol, and Ethanol is to be used as a substrate for single-cell protein production in a chemostat. The available equipment can achieve an oxygen transfer rate of 10 g   of liquid per hour. As- sume the kinetics of cell growth on ethanol is of the Monod type, with     cells/g ethanol, and   We wish to operate the chemostat with an ethanol concentration in the feed of 22 g/L. We also wish to maximize the biomass productivity and minimize the loss of unused ethanol in the effluent. Determine the required dilution rate and whether sufficient oxygen can be provided. We wish to operate the chemostat
with an ethanol concentration in the feed of 22 g/L. We also wish to maximize the biomass
productivity and minimize the loss of unused ethanol in the effluent. Determine the required
dilution rate and whether sufficient oxygen can be provided.
Explanation
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Bioprocess Engineering 2nd Edition by Fikret Kargi,Michael Shuler
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