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Design of Enzyme Reactor

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Savings on enzyme requirements and downstream processing. Trypsin-Agarose ... From V, calculate tres. From Vmax, k2, calculate [Eo] and total amount of enzyme required ... – PowerPoint PPT presentation

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Title: Design of Enzyme Reactor


1
Design of Enzyme Reactor
  • Geoff Greer
  • Joseph Gvildys
  • Aaron McGregor
  • April 2nd, 2007

2
Enzyme Selection
  • Transpeptidation
  • Trypsin or Achromobacter lyticus proteinase I
  • Optimal enzyme conditions
  • 4oC and a pH of 7

Eli Lilly
3
Enzyme Immobilization
  • Benefits
  • Savings on enzyme requirements and downstream
    processing
  • Trypsin-Agarose
  • 211 for 100 units ( 3mL)

Property
Biological Source trypsin from bovine pancreas
Extent of Labeling 15-35 units per ml (packed gel)
Matrix beaded agarose
Storage Temperature 2-8oC
4
Reactor Comparison
  • Batch
  • High operating costs
  • Batch-to-batch variations
  • PFR
  • Difficult to control pH and Temperature
  • CSTR
  • Simple pH, Temperature control
  • Simple catalyst charging and replacement

5
Design Parameters
Parameter Value
Q 7.786 L/h
Ro 0.0179 mol/L
Vmax 2.35 10-7 mol/L.s
Km 9.90 10-5 mol/L
k2 0.1285 s-1
MWreactant 6000 g/mol
MWtrypsin 25 000 g/mol
6
Reactor Design
  • Specify conversion, calculate R
  • From R, calculate v
  • From v, calculate D

7
Reactor Design
  • From D, calculate V
  • From V, calculate tres
  • From Vmax, k2, calculate Eo and total amount of
    enzyme required

8
Reactor Sizing
9
Reactor Sizing
  • Conversion of 99.25
  • 120 L reactor required
  • Increase conversion by 0.5 to 99.75
  • 360 L reactor required

10
Enzyme required
  • Required amount of enzyme is
  • 1.83 µmol/L
  • 5.5 g pure trypsin
  • 2.6 kg immobilized trypsin
  • Based on difference in activity between
    immobilized and non-immobilized enzyme
  • 18 000

11
Reactor Design Considerations
  • Temperature control
  • pH control
  • Level control
  • Sterilizable
  • Wire-mesh sieve
  • Sample port

12
Simplified Reactor Schematic
13
Costing of the Reactor
  • Several different manufacturers
  • New Brunswick Scientific
  • Novaferm AB
  • Scigenics
  • New MBR
  • Quote from New Brunswick Scientific
  • BioFlo Pro 150 L (120 L working volume)
  • 140 000 (US)
  • Batch reactor

14
Final Reactor Schematic
15
Overall Cost of Unit
  • For reactor and enzyme, estimated cost is at
    least 160 000
  • Additional considerations
  • Reactor modifications
  • De-naturation of enzyme

16
Thank You
  • Questions?
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