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Home⇒ Medical Science⇒ Bochemical Engineering⇒ Agitation and aeration
1-Dont try to cram or spend more time here just read it fast and cover syllabus then practice MCQ's cheptor of same topic to check your progress. . |
2-Wrong options are also given but dont concentrate there, Right answer is in bold format. |
Q1 ⇒ The range of width for the baffle in the fermenter is __________ times of vessel diameter 1/10 to 1/12 [other wrong options] [Discuss in forum] 1/8 to 1/10 1/5 to 1/8 none of these |
Q2 ⇒ Radial flow impellers Both (a) and (b) [other wrong options] [Discuss in forum] provide high shear conditions for breaking up bubbles direct flow towards the walls of the reactor provide low shear conditions and are suited for use in shear sensitive procesess |
Q3 ⇒ Power number is ratio of imposed forced to intertial force [other wrong options] [Discuss in forum] bouyant force to inertial force gravitation force to inertial force imposed force to gravitational force |
Q4 ⇒ When liquid is pumped through cooling coil in a stirred tank reactor to cool. Which of the following is not correct? Faster cooling rates at a slower rate of pumping [other wrong options] [Discuss in forum] If the stirrer speed is increased, the rate will be faster Baffles in the tank will increase the rate of cooling Faster cooling rates at a faster rate of pumping |
Q5 ⇒ The Intermig impeller is All of the above [other wrong options] [Discuss in forum] an axial flow impeller which can be used for the culture of aerobic organisms directed upwards rather than towards the base of the reactor a fork shaped extensions to the impeller facilitate bubble break up |
Q6 ⇒ Impeller damage can be minimized by using specially designed axial flow impellers [other wrong options] [Discuss in forum] using radial flow impellers using Intermig impellers all of the above |
Q7 ⇒ If the stirrer speed is too slow, bubbles will accumulate and coalescese under the impeller. This phenomenon is known as a flooded impeller [other wrong options] [Discuss in forum] coalesced impeller river impeller dry impeller |
Q8 ⇒ A fermentation system has a KLa of 3 s-1 and a C0* of 5 ppm of O2. If the bulk liquid is completely depleted of oxygen, then the oxygen transfer rate will be equal to 15 mg.l-1.s-1 [other wrong options] [Discuss in forum] zero 10 mg.l-1.s-1 5 mg.l-1.s-1 |
Q9 ⇒ For turbulent flow, Reynolds number is correlated with power number as (where K, a constant which depends on the container geometry and shape of stirrer; Rei, is Reynolds number for agitator; Di, stirrer diameter and N, stirrer speed) Np = K [other wrong options] [Discuss in forum] Np = K(Rei)-1 Np = N2Di(Rei)-1 Can't be correlated |
Q10 ⇒ Which of the following impellers generate a flow parallel to the axis of shaft? Axial flow [other wrong options] [Discuss in forum] Radial flow Both (a)and(b) None of these |
Q11 ⇒ Which device is commonly used for measuring the rate of rotation (rpm) of the stirrer shaft? Tachometer [other wrong options] [Discuss in forum] Anemometer Manometer Barometer |
Q12 ⇒ Which of the following impellers are used for wide range of viscosities? turbines [other wrong options] [Discuss in forum] paddles propellers none of these |
Q13 ⇒ If liquid density and viscosity remains constant, then the Reynolds number in a stirred tank reactor will vary with the square of the impeller diameter [other wrong options] [Discuss in forum] impeller diameter square root of the impeller diameter cube of the impeller diameter |
Q14 ⇒ Which of the following would be best described as an axial flow impeller? Both (a) and (b) [other wrong options] [Discuss in forum] An impeller with blades pitched at 45° to the vertical An impeller which directs liquid flow towards the base of the reactor An impeller with blades pitched at 75° to the vertical |
Q15 ⇒ Power consumption by agitation is all of the above [other wrong options] [Discuss in forum] a function of physical properties a function of operating conditions a function of vessel and impeller geometry |
Q16 ⇒ For aerated mixing vessels in an aqueous solution, the mass transfer coefficient (kL) co-relating power consumption (Pm) and fermenter volume (V) can be expressed as kL ∝ (Pm/V)0.33 [other wrong options] [Discuss in forum] kL ∝ (Pm/V)0.66 kL ∝ (Pm/V)0.50 kL ∝ (Pm/V) |
Q17 ⇒ A cylindrical reactor fitted with Rushton Turbine has a liquid volume of 100,000 litres. It has an aspect ratio (the ratio of the channel height to the width) of 2:1. The diameter of the impeller should be approximately: 1.3 m [other wrong options] [Discuss in forum] 3.3 m 5.3 m 7.3 m |
Q18 ⇒ The addition of antifoams to an aerated bioreactor will decrease oxygen transfer rates because antifoams All of the above answers [other wrong options] [Discuss in forum] increase the tendency of bubbles to coalesce tend to accumulate in the gas liquid interface reduce the surface tension of the liquid |
Q19 ⇒ Turbulent flow range of mixing speed is obtained for Rei>104 [other wrong options] [Discuss in forum] Rei<10 10<Rei<104 None of these |
Q20 ⇒ In a two-phase system where the continuous phase remains in place, the gas hold up can be expressed as (where Vs and Vt are the superficial gas velocity and bubble rise velocity) H = Vs/(Vs+ Vt) [other wrong options] [Discuss in forum] H = Vs/(Vs-Vt) H = Vs/(Vs.Vt) H = (Vs+Vt)/Vs |
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