Dynamics of Laminar Mixing in Continuous Stirred Tank Reactors
PowerPoint Presentation€¦ · PPT file · Web view · 2014-06-19Insulin Bioreactor Design...
Transcript of PowerPoint Presentation€¦ · PPT file · Web view · 2014-06-19Insulin Bioreactor Design...
Presented by:Shehneela Baseer
117113Zainab Sajjad
117114
Introduction to Bioreactors Types of Bioreactor designs Conclusion
Any manufactured or engineered device or system that supports a biologically active environment
Stirred tank reactors Bubble-column reactors Air lift reactors Drum rotating reactors Immobilized plane cell reactors
Membrane reactors
Air is dispersed by mechanical agitation.
Better control over the environment of the culture.
Can cause damage to the cells
High energy demand
Complexity in construction
Difficult to scale up.
One of the simplest type of gas – liquid bioreactors.
Facilitates sterile operation
Less damaging to shear-sensitive cells
Scale up is relatively easy.
Undefined fluid flow pattern inside the reactor.
Non-uniform mixing.
Works on draught tube principle.
Reasonable mixing with low shear
Operating cost is low.
Less contamination
Insufficient mixing at high cell densities.
Consists of horizontally rotating-drum on rollers connected to a motor.
High oxygen transfer.
Good mixing
Facilitated better growth and impart less hydrodynamic stress.
Difficult to scale up.
Immobilization of plant cell into a suitable carriers.
Either in natural (alginate, agar) or synthetic (polyacrylamide)
Cells are separated from growth medium by membrane
Environment is more easily controlled
Better control over cell density.
Reactor type
Oxygen transfer
Hydrodynamic stress
Mixing Scale up limitations
Stirred-tank High Highly destructive
Completely uniform
Difficult Cell death; contamination due to moving parts
ST-low agitation and modified impeller
Medium Low Reasonably uniform
Difficult Insufficient mixing at very high cell densities
Bubble-column
Medium Low Non-uniform
Easy Dead zones; settling of cells due to poor mixing
Air-lift High Low Uniform Easy Dead zones at high cell densities
Rotating-drum
High Low Uniform Difficult Non-uniform mixing at very large scale.
Insulin Bioreactor Design
Production of insulin precursor 5000 kg insulin per year
Assumes 20 % loss due to purification kLa within 10% of 2088 hr -1
Prevents oxygen limited reactionPrevents anaerobic metabolism
Glucose concentration < 0.5 g/LPrevents formation of ethanol
CSTR configuration Jacket heat exchanger Price
Substrate feedGlucose, ammonia, mineral salts
Cellular metabolism of substrate Extracellular production of insulin Air sparging for oxygen delivery Impellers for mixing of nutrients and
oxygen
Hence, with the help of different types of bioreactors, commercial production of secondary metabolites is not only possible but also profitable.