1 / 10

Production of Recombinant Human Insulin

Production of Recombinant Human Insulin. Design of an Enzyme Reactor. Review. Pro-Insulin (45% w/v) ~825 L. (Trypsin, 0.2 kg). Product. Trypsin is added to the aqueous stream of pro-insulin (@ 0.015 mol%) Target 100% conversion to the insulin ester. Enzymatic Digestion of Pro-Insulin.

diata
Download Presentation

Production of Recombinant Human Insulin

An Image/Link below is provided (as is) to download presentation Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author. Content is provided to you AS IS for your information and personal use only. Download presentation by click this link. While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server. During download, if you can't get a presentation, the file might be deleted by the publisher.

E N D

Presentation Transcript


  1. Production of Recombinant Human Insulin Design of an Enzyme Reactor

  2. Review Pro-Insulin (45% w/v) ~825 L (Trypsin, 0.2 kg) Product • Trypsin is added to the aqueous stream of pro-insulin (@ 0.015 mol%) • Target 100% conversion to the insulin ester

  3. Enzymatic Digestion of Pro-Insulin • Trypsin is a serine protease whose catalytic triad is; Asp, His, Ser.1 Catalytic pocket • Trypsin cleaves the cationic amino acids Arginine and Lysine (carboxyl side)2

  4. Enzyme Kinetics • Km values range from; 0.5 - 0.0007 M • K2 from; 0.2 – 0.05 s-1 • Enzyme functions from pH 4-9 and T 75-160°F • Iso-electric point, pH 5.4 • Operate above pI; pH~7 • Kinetic data valid for T=101°F, 38.3 ° C • Bovine trypsin; 23,500 g/mol Refs 1,3

  5. Stream Composition Feed 364.62 kg of pro-insulin (5958 g/mol) ~825 L aq. solution Product 328.16 kg of insulin ester (5706 g/mol) 36.45 kg of denatured insulin (288 g/mol) ~825 L aq. solution

  6. Reactor Choice • Trypsin is cheap => use the soluble enzyme • PFR Batch CSTR • ? ? • Use of the free enzyme renders batch, PFR kinetics equivalent when Q is variable Inefficient at high X Ref 1, 4

  7. Reactor Specification I • Best case (X~100%), t=11 h • Worst case (X~100%), t=40h • Design for t=25h

  8. Reactor Specification II • Long residence time • High value/conversion product Batch Liquid volume= 825L Add 20% Headspace~ 1000L Rules of thumb; HL=DT DT, HL=1.0m DT=3Di HR=1.25m Wb=0.1DT Include coils or a jacket Ref 5

  9. Reactor Cost/Source • “No-frills,” 1000L s/s reactor ~$95,000 CDN • Manufacturers; • Pfaudler, De Dietrich, Apache, Northland • Or buy used from Loeb;

  10. References • Voet et al. Fundamentals of Biochemistry. Toronto: Wiley, 1999. • Swiss Institute of Bioinformatics. Peptide Cutter (simulation software). http://ca.expasy.org/tools/peptidecutter/peptidecutter_enzymes.html# • Sigma Life Sciences. Trypsin from Bovine Pancreas, Prod. T8802. www.sigmaaldrich.com • Fogler, H.S. Elements of Chemical Reaction Engineering. Upper Saddle River: Prentice Hall. 1999. • Hasbrouck Engineering. Sample Batch Reactor Drawing. www.hasbrouckengineering.com

More Related