Multistream multistage operation

We may conclude from the previous section that the experimental possibilities of single-stream continuous systems are rather limited. There are many more possibilities with multistream systems, since these have multiple medium inflows that are independently variable and that may, if desired, contain a [Pg.334]

The dilution rates of the two fermenters are respectively = F /V and D2 = F2/V2. It is convenient mathematically to consider D2 as the sum of two partial dilution rates Dq2 and due to the two different inflows to fermenter 2, and defined as [Pg.335]

the first stage is described with Equs. 6.6 and 6.7. [Pg.335]

From this quadratic form, S2 can be computed by inserting the value of Si from Equ. 6.6, and the steady-state behavior for any value of and D2 can be derived the only precondition concerns the values of kinetic parameters. [Pg.335]

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