Optimization of Fermentation processes Both at the · PDF fileOptimization of Fermentation...
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Optimization of Fermentation processesBoth at the Process and Cellular Levels 'Simultaneous saccharification and fermentation
of starch to lactic acid'
K. V. Venkatesh
Department of Chemical EngineeringIIT Bombay
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Introduction
• Living cells can be used to produce biochemical products
• Natural screening of the environment to isolate microorganisms
• Isolated microorganisms or cells as pure cultures are grown in bioreactor – fermentation processes
• Fermentation processes are used to produce chemicals ranging from food, polymer, pharmaceuticals, bulk chemicals, bio-energy, waste management etc
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Metabolism
Multiple Enzymatic ReactionsSubstrate Products
1. Diverse products can be produced by various living cells2. Diversity depends on the metabolism evolved in a
particular organism; Yeast – ethanol, Lactobacillus – Milk to yogurt etc
Cell
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Fermentation Process• Cells/Microorganisms require a medium for its
growth
• Medium typically contains a carbon, nitrogen and essential nutrients
• Optimal pH and temperature
• Optimization at the process level: Media, environmental conditions
• Operation – batch, fed-batch or continuous
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Starch as a carbon Source
• Starch is a polysaccharide of glucose molecules
• Enzymatic hydrolysis to glucose
Starch Dextrin GlucoseAlpha - amylase Gluco-amylase
Inhibits
Rate of the enzymatic process is reduced due to glucose inhibition
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Lactic acid fermentation• Lactobacillus strain converts glucose to
lactic acid
GlycolysisGlucose Lactic Acid
GlycolysisStarch Lactic acid
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Inhibition of Saccharification by fermentative products
• Lactic acid
• Ethanol
• Butanol
• Diacetyl
• Acetoin
• Citric acid
The above products offer lesser inhibition than glucose
Dextrin GlucoseGluco-amylase
Lactic Acid
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Simultaneous Saccharification and fermentation
GlycolysisGlucose Lactic AcidDextrinGluco-amylase
Enzymatic reaction and fermentation in the same reactorwill not allow the accumulation of glucose toinhibit the saccharification step
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Strategy• Detailed modeling and experimental analysis of
the saccharification step• Detailed modeling and experimental analysis of
the fermentation step• Prediction of optimal condition for SSF using
model• Temperature (45C), pH (5.5) and glucose
concentration (< 20 g/L) crucial for the operation of SSF
• Experimental verification to demonstrate increased rates and productivities
• Fed-batch operation for reducing product inhibition
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Cellular Optimization• Cells screened from nature are typically
optimized for growth
• Cells are the micro-reactors in the fermentation process
• The main step for economical process is to perform cellular optimization.
• Metabolic and genetic engineering can be used to alter the cellular behaviour.
• Directed mutation versus random mutation.
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Metabolic Network analysisMetabolic Network analysis
1.1. Determine the limiting step in the Determine the limiting step in the
MetabolismMetabolism
2.2.Quantification of feasible metabolic spaceQuantification of feasible metabolic space
3.3. Removal of the limiting step in the Removal of the limiting step in the
network.network.
4.4.Detailed Kinetics of the process using Detailed Kinetics of the process using
metabolism.metabolism.
5.5. Elementary mode analysisElementary mode analysis
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What are the elementary modes ?
An elementary mode is a minimal subset of enzymes in a network that can operate at steady state with all irreversible reactions proceeding in the direction as prescribed by thermodynamics.
Elementary mode analysis links network structure to flux balance (evaluation of reaction rates)
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Methodology: Hypothetical Network
Elementary modesSystem chosen
Kalyan Gayen and K. V Venkatesh ESBES -2006
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Problem formulationRates of external metabolites
In matrix form
Linear programming formulation
Kalyan Gayen and K. V Venkatesh ESBES -2006, Austria
ExperimentallyDetermined
(known)
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Biochemical Network of Corynebacterium glutamicum
Metabolites : 39Reactions: 40
Substrates: Glucose, ammonia and oxygen
Products: Lysine, Biomass, Trehalose and Carbon dioxide
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Elementary Modes for the network of C. glutamicum
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Fourteen elementary modes
Kalyan Gayen and K. V Venkatesh BMC Bioinformatics, 2006
Elementary modes operational in Corynebacterium glutamicum
Maximum biomass (124)
Maximum Lysine (63.5)
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Flux distribution map of Flux distribution map of C. glutamicumC. glutamicum for lysine productionfor lysine production
OptimalBiomass
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Conclusions• Two level Optimization of fermentation
processes – reactor and cellular• Reactor: Engineering approaches - SSF, fed-
batch operation, in situ separation etc• SSF concept has been used for conversion of
cellulose to biofuels• Cellular: Metabolic Engineering• Quantification of biological processes is a key
step in such an application
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AcknowledgementAcknowledgement
1.1. Prof. A. K. SureshProf. A. K. Suresh
2.2. Dr. Anuradha Raghunathan (Scientist, NCL)Dr. Anuradha Raghunathan (Scientist, NCL)
3.3. DST for fundingDST for funding
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Thank Thank you !you !