Which of the following is/are optimally based methods ? 

TLS Online TPP Program

#Question id: 19915

#Section 5: Bioprocess Engineering and Process Biotechnology

A continuous reactor has a dilution rate of 0.5 h^-1. Its residence time would be

TLS Online TPP Program

#Question id: 19916

#Section 5: Bioprocess Engineering and Process Biotechnology

Which of the following is used to calculate mass of substrate in the reactor?

TLS Online TPP Program

#Question id: 19927

#Section 5: Bioprocess Engineering and Process Biotechnology

Fluidized bed bioreactors provide higher mass transfer rates than packed bed bioreactors because

TLS Online TPP Program

#Question id: 19928

#Section 5: Bioprocess Engineering and Process Biotechnology

A chemostat has a liquid volume of 2 litres and is being fed at a rate of 4 litres per hour. Dilution rate for this reactor will be

TLS Online TPP Program

#Question id: 19929

#Section 5: Bioprocess Engineering and Process Biotechnology

he growth of an organism on glucose is described by the following Monod model parameters: μm = 0.5 h^-1 and Ks =0.1 g.l^-1, if the concentration of glucose in the feed is 10 g.l^-1 and the dilution rate is set to 0.4 h^-1, then the steady state concentration of glucose in the effluent will be

TLS Online TPP Program

#Question id: 19954

#Section 5: Bioprocess Engineering and Process Biotechnology

A continuous reactor at steady state contains 0.04 g.l^-1 of biomass and 0.02 g.l^-1 of phenol. The feed contained 0.1 g.l^-1 of phenol. The biomass yield would be