Types of bioreactors: Airlift reactor MCQs With Answer

Introduction: Types of bioreactors: Airlift reactor MCQs With Answer is aimed at M.Pharm students who need a concise, application-focused review of airlift reactors within bioprocess engineering. This blog covers internal and external airlift designs, draft tube function, hydrodynamics, gas holdup, mass transfer (kLa), scale-up considerations, and suitability for different biological systems. The questions probe conceptual understanding, practical implications for aerobic fermentations and cell cultures, and modelling approaches used in development and scale-up. Use these MCQs to test and strengthen your ability to select and design airlift reactors for pharmaceutical bioprocesses involving shear-sensitive microbes and oxygen-limited reactions.

Q1. What fundamentally distinguishes an airlift reactor from other gas-liquid reactors?

  • Mixing driven primarily by an external mechanical impeller
  • Circulation established by density difference created by gas injection into a riser and downcomer
  • Operation as a packed bed with fixed catalyst particles
  • Use of sparged liquid jets without gas-induced circulation

Correct Answer: Circulation established by density difference created by gas injection into a riser and downcomer

Q2. Which pair correctly names the two main airlift reactor configurations?

  • Stirred-tank and bubble column
  • Internal-loop and external-loop airlift reactors
  • Baffled and unbaffled airlift reactors
  • Packed-bed and fluidized-bed airlift reactors

Correct Answer: Internal-loop and external-loop airlift reactors

Q3. What is the primary function of a draft tube in an internal-loop airlift reactor?

  • To inject nutrients into the culture medium
  • To separate the riser and downcomer zones and enhance circulation velocity
  • To provide mechanical agitation to break bubbles
  • To act as a heat exchanger for temperature control

Correct Answer: To separate the riser and downcomer zones and enhance circulation velocity

Q4. In a draft-tube airlift, how does gas holdup typically compare between the riser and the downcomer?

  • Gas holdup is higher in the downcomer than riser
  • Gas holdup is equal in riser and downcomer under all conditions
  • Gas holdup is higher in the riser than in the downcomer
  • Gas holdup is negligible in both riser and downcomer

Correct Answer: Gas holdup is higher in the riser than in the downcomer

Q5. Which characteristic makes airlift reactors especially suitable for shear-sensitive cultures?

  • High-intensity mechanical shear from impellers
  • Large-scale turbulent eddies created by baffles
  • Low shear environment with gentle gas-driven circulation
  • Intermittent high-shear mixing from pulsating pumps

Correct Answer: Low shear environment with gentle gas-driven circulation

Q6. Which operational parameter most directly increases the volumetric oxygen transfer coefficient (kLa) in airlift reactors?

  • Increasing substrate concentration while keeping gas flow constant
  • Increasing superficial gas velocity (gas flow per cross-sectional area)
  • Decreasing liquid height only
  • Operating at lower temperature to increase gas solubility

Correct Answer: Increasing superficial gas velocity (gas flow per cross-sectional area)

Q7. Compared with an equivalent stirred-tank reactor, the power input requirement of an airlift reactor is typically:

  • Much higher for the same oxygen transfer rate
  • Lower per unit volume for comparable circulation and aeration
  • Identical because mixing is always matched
  • Negligible and independent of gas flow

Correct Answer: Lower per unit volume for comparable circulation and aeration

Q8. Which type of bioprocess is generally less suitable for airlift reactors without modification?

  • Aerobic fermentations of suspension bacteria
  • Mammalian cell cultures that are shear-sensitive
  • Highly viscous or filamentous biomass processes prone to clogging
  • Algal cultures requiring low shear

Correct Answer: Highly viscous or filamentous biomass processes prone to clogging

Q9. What is the primary driving force for liquid circulation in an airlift reactor?

  • Mechanical pumping by external pumps
  • Density difference between aerated riser and deaerated downcomer due to gas holdup
  • Thermal convection from heat exchange surfaces
  • Electro-osmotic flow induced by applied electrical fields

Correct Answer: Density difference between aerated riser and deaerated downcomer due to gas holdup

Q10. Which scale-up criterion is commonly applied for airlift reactors to maintain similar hydrodynamics?

  • Constant impeller tip speed
  • Constant superficial gas velocity
  • Constant number of baffles per tank diameter
  • Constant stirrer geometry

Correct Answer: Constant superficial gas velocity

Q11. Which mathematical approach is widely used to model two-phase flow in airlift reactors?

  • Michaelis-Menten kinetics
  • Two-fluid (Euler–Euler) multiphase model
  • Langmuir adsorption isotherm
  • Fourier conduction equation only

Correct Answer: Two-fluid (Euler–Euler) multiphase model

Q12. How does increasing hydrostatic pressure (holding gas flow constant) generally affect gas holdup in an airlift reactor?

  • Gas holdup increases because bubbles expand under pressure
  • Gas holdup decreases because gas compressibility reduces volumetric fraction
  • Gas holdup is independent of pressure
  • Gas holdup becomes infinite at high pressure

Correct Answer: Gas holdup decreases because gas compressibility reduces volumetric fraction

Q13. What is the main structural difference between a bubble column and a draft-tube airlift reactor?

  • Bubble columns always have mechanical agitators, while airlifts do not
  • Draft-tube airlifts include an internal partition (draft tube) to create riser and downcomer
  • Bubble columns operate under vacuum, airlifts at positive pressure
  • Bubble columns use immiscible liquids, airlifts use miscible liquids

Correct Answer: Draft-tube airlifts include an internal partition (draft tube) to create riser and downcomer

Q14. Compared to a stirred-tank reactor at similar power input, how does an airlift reactor typically perform in terms of kLa?

  • Generally higher kLa for same power input
  • Generally lower kLa for same power input
  • Exactly the same regardless of geometry
  • kLa does not depend on reactor type

Correct Answer: Generally lower kLa for same power input

Q15. For cultivation of shear-sensitive mammalian cells, what feature of airlift reactors is most beneficial?

  • High-intensity turbulent mixing near impellers
  • Low shear stress and gentle mixing environment
  • Frequent formation of large inertial eddies
  • Aggressive bubble breakup by static mixers

Correct Answer: Low shear stress and gentle mixing environment

Q16. The flow pattern inside many airlift reactors is best approximated as which of the following?

  • Perfectly mixed continuous stirred-tank behavior throughout
  • Plug flow with axial dispersion in the riser/downcomer
  • Purely laminar single-phase flow with no dispersion
  • Stationary stratified layers with no circulation

Correct Answer: Plug flow with axial dispersion in the riser/downcomer

Q17. Which type of biochemical process most commonly benefits from airlift reactor operation?

  • Anaerobic digestion with no gas injection
  • Aerobic fermentations requiring oxygen transfer and gentle mixing
  • High-shear enzymatic reactions needing impeller-induced shear
  • Solid-phase peptide synthesis in packed columns

Correct Answer: Aerobic fermentations requiring oxygen transfer and gentle mixing

Q18. A simple experimental method to estimate gas holdup in an airlift reactor is:

  • Measuring dissolved oxygen only
  • Measuring the difference in liquid height between aerated and unaerated columns (static height method)
  • Counting bubbles visually at the sparger only
  • Estimating from temperature measurements alone

Correct Answer: Measuring the difference in liquid height between aerated and unaerated columns (static height method)

Q19. How does introducing a concentric draft tube typically change reactor performance?

  • It eliminates axial circulation and reduces gas holdup
  • It enhances axial circulation by separating riser and downcomer, increasing circulation velocity
  • It reduces oxygen transfer capability to zero
  • It transforms the reactor into a packed-bed reactor

Correct Answer: It enhances axial circulation by separating riser and downcomer, increasing circulation velocity

Q20. Which of the following is a common limitation of airlift reactors for pharmaceutical bioprocesses?

  • Excessive mechanical shear that always destroys mammalian cells
  • Limited applicability for highly viscous broths and processes prone to solids accumulation
  • Inability to provide any oxygen transfer for aerobic processes
  • Inherent requirement for corrosive construction materials only

Correct Answer: Limited applicability for highly viscous broths and processes prone to solids accumulation

Author

  • G S Sachin Author Pharmacy Freak
    : Author

    G S Sachin is a Registered Pharmacist under the Pharmacy Act, 1948, and the founder of PharmacyFreak.com. He holds a Bachelor of Pharmacy degree from Rungta College of Pharmaceutical Science and Research and creates clear, accurate educational content on pharmacology, drug mechanisms of action, pharmacist learning, and GPAT exam preparation.

    Mail- Sachin@pharmacyfreak.com

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