The flowsheet contains the following unknowns:
Flowrates: \(F_1, F_2, F_3, F_4, F_5, F_6\) (6 unknowns).
Mole fractions: each stream has two components (A and B). For each stream, only one independent mole fraction exists.
Thus, composition unknowns:
\[
6\ \text{streams} \times 1 = 6
\]
Total unknowns:
\[
6\ (\text{flows}) + 6\ (\text{compositions}) = 12
\]
Available independent equations:
Mass balance for each unit (separation unit & mixer): 4 equations.
Component balances across units: 2 components → 4 more equations.
Given constraint: \(F_1 + F_2 = 100\ \text{kg h}^{-1}\) gives 1 additional equation.
Total equations:
\[
4 + 4 + 1 = 9
\]
Therefore, degrees of freedom:
\[
\text{DOF} = 12 - 9 = 6
\]