Biological Reactors: Material Balances and Kinetics
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TERZA PARTE
1. Fed-batch biological reactor: material balances with Monod kinetics and operating methods:
- it maintains some operational characteristics of the batch, while ensuring constant biomass production such as a CSTR
- Therefore, there is an inlet supply with V˙e and [substrate] Cse and negligible Cxe
- since it is not a continuous reactor, it will never reach the steady state condition, there will always be an accumulation
- at zero time there will be: a certain initial VR with an initial [substrate], initial [biomass] and subsequently the volume will increase over time.
- Total biomass balance:
- dmtot / dt = me, with me = ρe V ,e,
- from this relationship we obtain that
- dVr / dt = V˙e.
- At this point two feeding strategies can be considered,
- 1. one with