Q2
MCQ • 1M
Quantitative Aptitude
Two straight lines pass through the origin (𝑥, 𝑦) = (0,0). One of them passes through the point (𝑥ଵ, 𝑦ଵ) = (1,3) and the other passes through the point (𝑥ଶ, 𝑦ଶ) = (1,2). What is the area enclosed between the straight lines in the interval [0, 1] on the 𝑥-axis?
Q9
MCQ • 2M
Analytical & Spatial Aptitude
In the square grid shown on the left, a person standing at P2 position is required to move to P5 position. The only movement allowed for a step involves, “two moves along one direction followed by one move in a perpendicular direction”. The permissible directions for movement are shown as dotted arrows in the right. For example, a person at a given position Y can move only to the positions marked X on the right. Without occupying any of the shaded squares at the end of each step, the minimum number of steps required to go from P2 to P5 is 1 2 3 4 5 P Q R S T Example: Allowed steps for a person at Y
Q13
MCQ • 1M
Biomolecules, enzyme kinetics
For a double-pipe heat exchanger, the inside and outside heat transfer coefficients are 100 and 200 W m-2 K-1, respectively. The thickness and thermal conductivity of the thin-walled inner pipe are 1 cm and 10 W m-1 K-1, respectively. The value of the overall heat transfer coefficient is ___________ W m-2 K-1.
Q28
NAT • 1M
Bioreactor types, scale-up
A microorganism is grown in a batch culture using glucose as a carbon source. The apparent growth yield is 0.5 ୠ୧୭୫ୟୱୱ ୱ୳ୠୱ୲୰ୟ୲ୣ. The initial concentrations of biomass and substrate are 2 g L-1 and 200 g L-1, respectively. Assuming that there is no endogenous metabolism, the maximum biomass concentration that can be achieved is _________________ g L-1.
Q34
NAT • 1M
Bioreactor types, scale-up
A fermentation broth of density 1000 kg m-3 and viscosity 10-3 kg m-1 s-1 is mixed in a 100 L fermenter using a 0.1 m diameter impeller, rotating at a speed of 2 s-1. The impeller Reynolds number is ____________. .35 For a pure species, the slope of the melting line ௗ ௗ் at -2 ˚C is -5.0665×106 Pa K-1. The difference between the molar volumes of the liquid and solid phase at -2 ˚C is -4.5×10-6 m3 mol-1. The value of the latent heat of fusion (rounded off to nearest integer) is __________ J mol-1. .36 - Q.65 Carry TWO marks each.
Q56
NAT • 2M
Biomolecules, enzyme kinetics
For 1 0x and 2 0x , the value of 1 2 1 2 1 2 2 lim ln x x x x xx x is __________. .57 Figure below depicts simplified metabolic and transport reactions taking place in the production of B from A in a cell. The subscript ' i' refers to intracellular metabolites. rj is the jth reaction flux in ( ୢ୰୷ ୫ୟୱୱ) ୦. Under pseudo-steady-state condition, the following reaction fluxes are available. r1 = 4, r3 = 1 and r6 = 1. The transport flux of B, r4, is _____________ ( ୢ୰୷ ୫ୟୱୱ) ୦.
Q57
NAT • 2M
Biomolecules, enzyme kinetics
Figure below depicts simplified metabolic and transport reactions taking place in the production of B from A in a cell. The subscript ‘i’ refers to intracellular metabolites. rj is the jth reaction flux in ( ୢ୰୷ ୫ୟୱୱ) ୦. Under pseudo-steady-state condition, the following reaction fluxes are available. r1 = 4, r3 = 1 and r6 = 1. The transport flux of B, r4, is _____________ ( ୢ୰୷ ୫ୟୱୱ) ୦.
Q60
NAT • 2M
Bioreactor types, scale-up
Liquid-phase mass transfer coefficient ( kL) is measured in a stirred tank vessel using steady-state method by sparging air. Oxygen uptake by the microorganism is measured. The bulk concentration of O 2 is 10 -4 mol L -1. Solubility of O 2 in water at 25 ˚C is 10-3 mol L-1. If the oxygen consumption rate is 9×10 -4 mol L -1 s-1, and interfacial area is 100 m2/m3, the value of kL is __________cm s-1. .61 Consider a piston-cylinder assembly shown in the figure below. The walls of the cylinder are insulated. The cylinder contains 1 mole of an ideal gas at 300 K and the piston is held initially at the position z 1 using a stopper. After the stopper is removed, the piston suddenly rises against atmospheric pressure (1.013×10 5 Pa) to the new position z2 where it is held by another stopper. The heat capacity (Cv) of the gas is 12.5 J mol -1 K-1. The cross-sectional area of the cylinder is 10-3 m2. Assume the piston is weightless and frictionless. If zଶ - zଵ = 1 m, the final temperature of the gas (rounded off to nearest integer) is ___________K. .62 Consider the growth of S. cerevisiae under aerobic condition in a bioreactor and the specific growth rate of yeast is 0.5 h-1. The overall reaction of the process is 2C6H12O6 +0.2NH3+10.35O2 CH1.8O0.5N0.2+0.2C2H6O+10.6CO2+10.8H2O The heat of combustion values for different compounds are tabulated below with the reference to CO2, H2O, O2, and N2 at standard conditions. Compound Heat of combustion (kJ mol-1) C6H12O6 2802 NH3 383 CH1.8O0.5N0.2 560 C2H6O 1366 The specific rate of heat production (rounded off to nearest integer) is _____________ kJ mol-1 h-1. .63 A pilot sterilization was carried out in a vessel containing 100 m 3 medium with an initial spore concentration of 10 8 spores/ml. The accepted level of contamination after sterilization is 1 spore in the entire vessel. The specific death rate constant for the spore is 2 min -1 at 121 ˚C. Assuming no death takes place during the heating and cooling cycles, the holding time at 121 ˚C (rounded off to nearest integer) is _____________min.
Q61
NAT • 2M
Biomolecules, enzyme kinetics
Consider a piston-cylinder assembly shown in the figure below. The walls of the cylinder are insulated. The cylinder contains 1 mole of an ideal gas at 300 K and the piston is held initially at the position z1 using a stopper. After the stopper is removed, the piston suddenly rises against atmospheric pressure (1.013×105 Pa) to the new position z2 where it is held by another stopper. The heat capacity (Cv) of the gas is 12.5 J mol-1 K-1. The cross-sectional area of the cylinder is 10-3 m2. Assume the piston is weightless and frictionless. If 𝑧ଶ− 𝑧ଵ = 1 m, the final temperature of the gas (rounded off to nearest integer) is ___________K.
Q62
NAT • 2M
Bioreactor types, scale-up
Consider the growth of S. cerevisiae under aerobic condition in a bioreactor and the specific growth rate of yeast is 0.5 h-1. The overall reaction of the process is 2C6H12O6 +0.2NH3+10.35O2 CH1.8O0.5N0.2+0.2C2H6O+10.6CO2+10.8H2O The heat of combustion values for different compounds are tabulated below with the reference to CO2, H2O, O2, and N2 at standard conditions. Compound Heat of combustion (kJ mol-1) C6H12O6 2802 NH3 383 CH1.8O0.5N0.2 560 C2H6O 1366 The specific rate of heat production (rounded off to nearest integer) is _____________ kJ mol-1 h-1.