Questions 11–20 of 24. Imported answers require independent review unless marked reviewed.

Topic practice 24 questionsPage 2 of 3

Question 54

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Fermentation medium is cooled from 121 °C to 30 °C in a double pipe heat exchanger. If cold water is flowing in the counter-current direction and is heated from 10 °C to 70 °C, then the Log-Mean Temperature Difference (LMTD) is ______ °C (rounded off to the nearest integer).

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Question 55

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Aspergillus niger is grown in a 10,000 L stirred batch bioreactor under aerated conditions to produce citric acid. At steady state oxygen transfer conditions, the specific oxygen uptake rate of the organism and the volumetric mass transfer coefficient are

and 60 min

, respectively.
If the oxygen solubility is

kg m

under the operating conditions, based only on oxygen dynamics, the maximum possible cell concentration is ______ kg m

(Answer in integer).

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Question 56

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Ethanol is produced in a 10,000 L stirred bioreactor using an impeller of diameter 1 m. The density and viscosity of fermentation broth are 1000 kg m

and 1 cp, respectively. The data relating the Power number and Impeller Reynolds number is given below:
| Reynolds number | 1-5 | 5-500 | > 10

| | Power number | 70 | 10 | 5 |
Using the above data, the power required for the stirrer to operate at 300 rpm is ______ kW (Answer in integer).

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Question 62

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The values of the consistency index ‘K’ and the flow behavior index ‘n’ of a dilatant fluid are 0.415 (in CGS units) and 1.23, respectively. The value of the apparent viscosity (in

) of this fluid at a shear rate of

(rounded off to the nearest integer) is ____________.

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Question 63

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An evaporator is insulated using glass wool material of 0.15 m thickness. The inner most surface and the outer surface of the insulation are at 700 °C and 80 °C, respectively. The mean thermal conductivity of the glass wool under these conditions is 0.29 W m

K

. The rate of heat loss (in W) through 1.2 m

of the evaporator wall surface (rounded off to the nearest integer) is ____________.

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Question 13

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For a double-pipe heat exchanger, the inside and outside heat transfer coefficients are 100 and 200 W m

K

, respectively. The thickness and thermal conductivity of the thin-walled inner pipe are 1 cm and 10 W m

K

, respectively. The value of the overall heat transfer coefficient is ________ W m

K

.
Your answerChoose one option.

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Question 34

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A fermentation broth of density 1000 kg m

and viscosity 10

kg m

s

is mixed in a 100 L fermenter using a 0.1 m diameter impeller, rotating at a speed of 2 s

. The impeller Reynolds number is ________________.

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Question 60

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Liquid-phase mass transfer coefficient (

) 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

is

mol L

. Solubility of O

in water at 25 °C is

mol L

.
If the oxygen consumption rate is

mol L

s

, and interfacial area is 100 m

/m

, the value of

is __________ cm s

.

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Question 47

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A sedimentation tank of height 100 cm is used in a conventional activated sludge process to separate a suspension of spherical shaped granular sludge biomass of 0.5 mm diameter. The viscosity of the liquid is 1 cP. The difference in density between the suspended biomass and the liquid is 0.1 g cm⁻³. If the biomass reach their terminal velocity instantaneously, the biomass settling time in min (rounded off to two decimal places) is _____.

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Question 52

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Milk flowing through a stainless steel inner tube (40 mm inner diameter) of double tube-type heater is to be heated from

to

by saturated steam condensing at

on the outer surface of the inner tube. Total heat transferred (

) is

and the overall heat transfer coefficient is

. The total length of the heating tube in

(rounded off to one decimal place) is ________.

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