Process Flow Diagram and Safety and Other Considerations

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Presentation transcript:

Process Flow Diagram and Safety and Other Considerations Fed-Batch Production of Humanized Monoclonal Antibodies Test Tube Babiez Inc. George Moskos, Kayla Lawlor, John Gwozdz, Liam Corless Department of Chemical Engineering, University of New Hampshire Background Process Flow Diagram and Material Balances Objectives Produce humanized monoclonal antibodies to treat colon and breast cancer Customer Requirements Produce titers from 5-10 g/L Produce ~1,000 kg/yr Business Case Selling for $2,000/g  Contracting option Seed Train Fermentation Protein A Chromatography Virus Inactivation Polishing Ultrafiltration Diafiltration Economic Analysis Safety and Other Considerations Conclusions Complies to GMP and European regulations Inherent safe design methods were implemented All process vessels were equipped with relief valves Clean-in-Place and Steam-in-Place protocol were used for cleaning 50 kg/batch of MAbs, 20 batches/year DCFRR is 737% with $726 MM after tax net profit Inherent safe design for all equipment and HAZOP analysis  Process vessels and piping cleaned with CIP and SIP procedures Relief Valve Kill Tank Q-710 Rupture Disc Guide Word Deviation Cause Consequences Action No No steam flow Utility malfunction Biological waste not killed, sent to sewer while active Shut down kill tank, assess the steam utility control system No cooling tower water Tank overheats, potential risk of explosion Shut down tank, fix cooling water. Install temperature monitor No flow out via Stream 90 Blockage Tank becomes over pressurized, risk of explosion Shut down kill tank, clear the blockage More More material in inlet streams Pump malfunction Rupture disc breaks due to pressurized system Shut down kill tank, fix pump. Install PAH. Less Less flow into the tank Pump malfunction/less production Tank overheats due to less material inside Lessen steam flow Recommendations Acknowledgements TTB Inc. currently recommends a GO for this process We would like to thank the Department of Chemical Engineering, Dr. Jeffrey Halpern, and Greg Williams from Thermo Fisher for the continued support and resources throughout this project.