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Generic Protocol for Optimization of Heterologous Protein Production Using Automated Microbioreactor Technology
Published on: December 15, 2017
Single versus multiple bioreactor scale-up: economy for high-value products
1Department of Chemical Engineering, University of Waterloo, Ont., N2L 3G1, Waterloo, Canada
Summary
Scaling up bioreactor production using multiple units significantly boosts return on investment (ROI) by 122%. This strategy reduces downstream processing costs for high-value products like tissue plasminogen activator (t-PA).
Area of Science:
- Biotechnology
- Chemical Engineering
- Process Economics
Background:
- Scaling up biopharmaceutical production presents economic challenges, particularly concerning downstream processing costs.
- Tissue plasminogen activator (t-PA) is a high-value biopharmaceutical produced using animal cell culture.
- Traditional scale-up often relies on increasing bioreactor size, impacting overall process economics.
Purpose of the Study:
- To evaluate the economic feasibility of scaling up bioreactor production by increasing the number of units versus using a single large unit.
- To compare the return on investment (ROI) for a multiple bioreactor approach versus a single large bioreactor for t-PA production.
- To analyze the impact of scale-up strategy on downstream processing costs and equipment contributions.
Main Methods:
- Integrated flowsheet simulations were developed for both single large bioreactor and multiple smaller bioreactor scenarios.
- Economic analysis focused on return on investment (ROI) and breakdown of equipment purchase costs.
- Downstream unit scheduling was optimized to allow equipment sharing in the multiple bioreactor case.
Main Results:
- A multiple bioreactor scale-up strategy increased the ROI of the base process by 122%.
- This significant ROI increase is attributed to the reduced size and cost of downstream processing units.
- Downstream processing costs, which account for approximately 80% of total costs for products like t-PA, were substantially lowered.
- The proportion of cell culture equipment cost increased from 14% to 37%, while chromatography column costs decreased from 52% to 33% of total equipment purchase cost.
Conclusions:
- Scaling up bioreactor production through a multiple-unit approach offers substantial economic advantages over the single large-unit method.
- Optimized scheduling and equipment sharing in downstream processing are key drivers for improved ROI in multi-bioreactor systems.
- This strategy effectively mitigates the high cost associated with downstream processing for valuable biopharmaceuticals like t-PA.
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