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Consider a simple uni-substrate enzyme that follows Michaelis-Menten kinetics. When the enzyme catalyzed

Consider a simple uni-substrate enzyme that follows Michaelis-Menten kinetics. When the enzyme catalyzed

Q. Consider a simple uni-substrate enzyme that follows Michaelis-Menten kinetics. When the enzyme catalyzed reaction was carried out in the presence of 10 nM concentration of an inhibitor, there was no change in the maximal velocity. However, the slope of the Lineweaver-Burk plot increased 3-fold. The dissociation constant for the enzyme-inhibitor complex (in nM) is […]

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First order deactivation rate constants for soluble and immobilized amyloglucosidase enzyme are 0.03 min-1 and 0.005 min-1

First order deactivation rate constants for soluble and immobilized amyloglucosidase enzyme are 0.03 min-1 and 0.005 min-1

Q. First order deactivation rate constants for soluble and immobilized amyloglucosidase enzyme are 0.03 min-1 and 0.005 min-1, respectively. The ratio of half-life of the immobilized enzyme to that of the soluble enzyme is (rounded off to the nearest integer)        Ans: 6 to 6

First order deactivation rate constants for soluble and immobilized amyloglucosidase enzyme are 0.03 min-1 and 0.005 min-1 Read More »

In a chemostat, the feed flow rate and culture volume are 100 ml/h and 1.0 L, respectively

In a chemostat, the feed flow rate and culture volume are 100 ml/h and 1.0 L, respectively

Q. In a chemostat, the feed flow rate and culture volume are 100 ml/h and 1.0 L, respectively. With glucose as substrate, the values of µmax and Ks are 0.2 h-1 and 1 g/L, respectively. For a glucose concentration of 10 g/L in the feed, the effluent substrate concentration (in g/L) is          Ans: 1

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A microbial strain is cultured in a 100 L stirred fermenter for secondary metabolite production

A microbial strain is cultured in a 100 L stirred fermenter for secondary metabolite production

Q. A microbial strain is cultured in a 100 L stirred fermenter for secondary metabolite production. If the specific rate of oxygen uptake is 0.4 h-1 and the oxygen solubility in the broth is 8 mg/L, then the volumetric mass transfer coefficient (KLa) (in s-1) of oxygen required to achieve a maximum cell concentration of

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Match the industrial products mentioned in Group I with their producer organisms in Group II

Match the industrial products mentioned in Group I with their producer organisms in Group II

Q. Match the industrial products mentioned in Group I with their producer organisms in Group II Group I                    Group II P. Citric acid            1. Trichoderma viride Q. Cellulase               2. Clostridium acetobutylicum R. Vitamin B12             3. Aspergillus niger S. Butanol           4. Propionibacterium freudenreichii   (A) P-4, Q-3, R-1, S-2 (B) P-3, Q-1, R-2, S-4   (C)

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