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Published byJanice Russell Modified over 6 years ago
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Optimal Reactor Configuration for Lactic Acid Production
Libby Bol
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Introduction Commercially produced as a commodity chemical
Fermentation limitations Product inhibition Substrate inhibition pH control
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Reactor Options Two-Stage cell recycle reactor with membrane separation High cell concentration High productivity Electrokinetic bioreactor Removes product as it is formed Does not rely on chemical pH control
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Assumptions Normalized reactor conditions are representative of actual conditions Cell growth approximately follows Monod Kinetics
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Calculations Reactor volume required to form 100g/h
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Calculations Lactic Acid Balance
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Comparison 1.8 0.021 204 24.8 92 18 Two-stage Cell Recycle
Electrokinetic Bioreactor Volume 1.8 0.021 Expected Concentration 204 24.8 Actual Concentration 92 18
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Complications Electrokinetic reactor Cell Recycle Mixing problems
If voltage increase is required for larger reactor, could damage cells Cell Recycle High cell conc. could foul membrane
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Conclusions Cell Recycle reactor is safest alternative for industrial use Additional testing on pilot scale equipment of electrokinetic bioreactor should be done
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Questions
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