Typical simulation time is between 1-10 seconds, depending on complexity.
Welcome to the alfa-build of my online bioprocess simulator!
First time users: just jump to results tab and click the "Run Bioreactor" button. This will show you a typical outcome of a simulation, using default input values.
Explore the Tabs: Navigate through the tabs like 'Bioreactor', 'Gas Flows', 'Microbes', and more to input your specific parameters.
Input Your Data: Each tab comes with a set of inputs where you can enter details about your bioreactor setup, microbial culture, gas flows, and other critical aspects.
Run the Simulation: Once you've input all necessary data, hit the 'Run bioreactor' button in the 'Results' tab to see the simulation in action.
Analyze the Results: View real-time graphs and data analytics on the 'Results' tab to understand the performance and output of your bioreactor model.
All bioprocess simulations follow a specific set of steps, listed below:
step 1) fermentor is filled with substrate.
step 2) sterilization in place. In the current model it is merely a waiting time.
step 3) inoculation. The bioreactor is inoculated with a biomass concentration. Typically, a short procedure as it tends to be a small volume.
step 6) bioreactor washing/cleaning. Currently just a waiting step.
upcoming features:
Gas mass balances (O2/CO2)
Biochemical production (incl product inhibition)
Pre-selection tool of what type of reactor you intend to use (bubble column, CSTR, airlift)
Use database of microbe growth parameters
Techno-economic evaluations
Some of the literature that is used in the models:
Van't Riet, K. (1991). Basic Bioreactor Design. Marcel Dekker.
Garcia-Ochoa, F., & Gomez, E. (2009). Bioreactor scale-up and oxygen transfer rate in microbial processes: An overview. Biotechnology Advances, 27(2), 153-176. doi:10.1016/j.biotechadv.2008.10.006
Garcia-Ochoa, F., & Gomez, E. (2009). Oxygen mass transfer in biopharmaceutical processes: Numerical and experimental approaches. Chemical Engineering Science, 64(12), 2939-2948. doi:10.1016/j.ces.2009.03.018
Higbie, R. (1935). The rate of absorption of a pure gas into a still liquid during short periods of exposure. Transactions of the American Institute of Chemical Engineers, 31, 365-389.
Shah, Y. T., Kelkar, B. G., Godbole, S. P., & Deckwer, W. D. (1982). Bubble column reactors. Wiley.
Van't Riet, K., & Tramper, J. (1991). Basic engineering principles of bioreactor scale-up. Journal of Biotechnology, 15(1-2), 1-20. doi:10.1016/0168-1656(91)90055-Q
Oosterhuis, N. M. G., & Kossen, N. W. F. (1986). Theoretical and practical aspects of the scale-down of bioreactors. Chemical Engineering Science, 41(12), 3099-3105. doi:10.1016/0009-2509(86)81822-7
Linek, V., & Vacek, V. (1981). Mass transfer in bubble columns for individual flow regimes. Chemical Engineering Science, 36(9), 1747-1768. doi:10.1016/0009-2509(81)80073-5
Zlokarnik, M. (1999). Scale-up in Chemical Engineering. Wiley-VCH.