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Vaccine - 4/11/06. 2. POLYHYDROXYALKANOATE COPOLYMERPOLYHYDROXY BUTYRATE
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1. Vaccine - 4/11/06 1 Nodax™ Polyhydroxyalkanoate Development of a Low Cost Fermentation and Recovery Process for a Commodity Polymer
Phillip Green
Karuna Narasimhan
Procter & Gamble Co.
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3. Vaccine - 4/11/06 3 Properties of Interest Biological
- Made from renewable sources
- Aerobically and An-aerobically biodegradable
Thermo –Mechanical
- Similar to polyethylene and polypropylene
- Strength, flexibility, toughness
- Exhibit (Springy) Elasticity
Physio-Chemical
- Higher surface energy – Dyeability, printability
- Chemical digestibility in hot-alkaline medium
- Barrier properties
4. Vaccine - 4/11/06 4 PHA Process Summary
5. Vaccine - 4/11/06 5 Technical Development Overview What is needed technically to reach commercialization? Yield: organism and fermentation protocol that delivers target composition and yield at large scale.
Cost effective and reliable recovery process.
Nucleation package to enable finished article processing.
Long term Making Cost Target = < $2.30/kg
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11. Vaccine - 4/11/06 11 PHA Recovery Process Transformations Lysing of Cell – By
- Mechanical/Chemical digestion/Enzymatic
- Solvents
Dissolving PHA in solvents at moderate Temp., high levels
Separation of cell debris from PHA
Precipitating PHA - modifying the solubility by
- Temperature and/or
- “Non-Solvents”
Separation of PHA from liquid media.
Possible Combinations-
- LSS- Clean up of unwanted material Biomass
- DSPS- Extracting good polymer from Biomass
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14. Vaccine - 4/11/06 14 Aqueous Isolation Process Concept
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16. Vaccine - 4/11/06 16 Solvent Extracted Product
Composition (Mol % Co-polymer content)
MW ( < 20% reduction in MW)
DSC (Melting temp.- Target 100-150 0C, matching copolymer content)
Purity (> 99-100%)
Color (L- > 95, a < +/- 2, b < +/- 4)
Odor (no offensive odor)
Residual Solvents (typical < 200 ppm Vs. target < 1000 ppm)
17. Vaccine - 4/11/06 17 Questions ?
Thank You .