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TLS Online TPP Program
#Question id: 24057
#Unit 12. Biochemical Engineering
An exponentially increasing leaf of concentrated .substate is led Soo a led batch reactor to maintain a courant specific growth rate 0.35 H-1. if the feed is 5ml/hr at time. t 0. then feed alter 4 hrs will be approximately
TLS Online TPP Program
#Question id: 21634
#Unit 12. Biochemical Engineering
The equation for aerobic production of acetic acid from ethanol is:
CH2OH+O2→CH3CO2H+H2O.
(ethanol) (acetic acid)
Acetobacter aceti bacteria are added to vigorously-aerated medium containing 10 g.14 ethanol. After some time, the ethanol concentration is 2 g.-2 and 7.5 g.11 of acetic acid is produced. What is the observed yield (Yoing-) and theoretical yield (Yting-8") of acetic acid from ethanol?
TLS Online TPP Program
#Question id: 21644
#Unit 12. Biochemical Engineering
In an exponentially growing batch culture of Saccharomyces cerevisiae, the cell density is 30 𝒈𝑳−𝟏(𝑫𝑪𝑾), the specific growth rate (𝝁) is 𝟎.𝟒𝒉−𝟏 and substate uptake rate (𝒒) is 𝟏𝟖𝒈𝑳−𝟏𝒉−𝟏. The cell nyield coefficient 𝒀𝒙/𝒔 will be
TLS Online TPP Program
#Question id: 21671
#Unit 12. Biochemical Engineering
A stirred tank bioreactor of 𝟐.𝟕𝒎𝟑 is agitated using a Rushton turbine with diameter 0.5 m and stirrer speed of 𝟏 𝒔−𝟏. If the fermentation broth has viscosity and density of 𝟏𝟎−𝟐 𝒑𝒂.𝒔 and 𝟏𝟎𝟎𝟎𝒌𝒈.𝒎−𝟑 respectively, the mixing time (in seconds) for the bioreactor will be
TLS Online TPP Program
#Question id: 22775
#Unit 12. Biochemical Engineering
Identify the parameter among the following used for scale up of a shear sensitive cells in a fermentation process
TLS Online TPP Program
#Question id: 22776
#Unit 12. Biochemical Engineering
Sterilization of air by absolute filtration mechanism is primarily based on
