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Product Drying and Recovery Scott MacLean CHEE 450 April 2, 2004.

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Presentation on theme: "Product Drying and Recovery Scott MacLean CHEE 450 April 2, 2004."— Presentation transcript:

1 Product Drying and Recovery Scott MacLean CHEE 450 April 2, 2004

2 Goals of Drying Stage Recover product Ensure it is intact/usable Minimize losses Minimize costs Maximize shelf life

3 Options Tray Drying Freeze Drying Spray Drying

4 Known Information Recover 190kg Insulin Crystal, 1.4 kg Insulin, 0.6 kg Water per batch Ultrafilter, centrifuge are previous process steps for removal of water

5 Assumptions Ultrafilter and Centrifuge reduce water to 30% by weight Process requires a continuous drying stage when in operation All other volatile components removed prior to drying stage

6 Drying Stage Flow Diagram

7 Freeze, Tray, or Spray – A Question of Stability Insulin is a Protein Zn-Insulin Crystals are stable below ~60 o C Above 60 o C, begins to denature Heat disrupts hydrogen bonds, causing vibrations  Think of egg frying

8 Tray Drying – Is it hot in here, or is it just me? http://info.chee.queensu.ca/chee440/chee440.htm

9 Tray Drying – Is it hot in here, or is it just me? Temperature - High Time - Long Cost – Low Capital, High operation Requires pre-drying steps currently employed to minimize moisture content

10 Freeze Drying – The Traditional Choice http://wine1.sb.fsu.edu/chm1045/notes/Forces/Phase/Forces06.htm

11 Freeze Drying – The Traditional Choice Freezing  This provides a necessary condition for low temperature drying. Vacuum  After freezing, the product is placed under vacuum. Heat  Heat is applied to the frozen product to accelerate sublimation. Condensation  Low-temperature condenser plates remove the vaporized solvent from the vacuum chamber by converting it back to a solid.

12 Freeze Drying – Equipment Selection Sizing based on SuperPro Insulin Simulation – Scale Up 15 kg of Insulin Crystal requires 40m 2 of drying area Allow 20% additional space 600 m 2 required for 190kg of product 15 o C, 24h typically used for protein drying

13 Freeze Drying – Product Concerns Stability  Long-term Moisture  Product is very hygroscopic Shelf life  Light, porous product Method of Delivery  Useful for re- suspension in sterile water for injection Cost  Expensive, long process

14 Spray Drying – The Next Challenge? Spray Drying – Basics  Fluid sprayed into air in droplets  Fluid evaporates, solid particle remains  Spherical, hollow (Like a gumball)

15 Spray Drying – The Next Challenge? http://info.chee.queensu.ca/chee440/chee440.htm

16 Spray Drying – The Next Challenge Stable, light product Inhalation? Temperature problems Cost  Expensive capital, low cost to operate

17 Which to choose? Freeze Drying – The Traditional Choice Spray Drying – The Next Challenge

18 References & Questions References CHEE 440 Website. http://info.chee.queensu.ca/chee440/chee440.htm (Amsden, 2004)http://info.chee.queensu.ca/chee440/chee440.htm Khachidze, D.G., Y.L Kalandadze, and J.R. Monaselidze. Microcalorimetric studies of insulin and Zn(II)-insulin over a wide range of pH and protein concentration. 2001. Phase Diagrams. http://wine1.sb.fsu.edu/chm1045/notes/Forces/Phase/Forces06.htm (Blaber, 1996.)http://wine1.sb.fsu.edu/chm1045/notes/Forces/Phase/Forces06.htm


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