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Determine the permissible X-range for which the F/M ratio is maintained (Use Equation/inequality (6) for the purpose).
(5) Choose a suitable sludge recycled ratio αmin < α < αmax (6) Determine the permissible X-range for which the F/M ratio is maintained (Use Equation/inequality (6) for the purpose) (7) Calculate the optimum value of X by Eq. (19) (8) Calculate the area of the settling tank by Eq. (14) (9) Calculate the reactor area by Eq. (15) or volume by Eq. (4). .
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The desirable conversion level is maintained using initiator flow rate as the manipulated variable.
A full 3D velocity space dependence is maintained using cylindrical coordinates (v∥,v⊥,γ).
Pressure head is maintained using one ball check valve at the outlet of the pump.
In the second mode, the group formation is maintained using a hierarchical coordination.
The buffer is maintained using a first in, first out (FIFO) queue.
Time synchronization is maintained using SYNC messages exchanged during active period.
The nominal attitude profile is maintained using the micro-propulsion subsystems.
An index of all pathways is maintained using the Apache Lucene library [6].
The CCD is maintained using Concurrent Versions System.
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