Step 1: Define the recycle ratio.
The recycle (return sludge) ratio is $R = Q_r/Q = 6000/20000 = 0.3$. This means the return flow is 30% of the influent flow.
Step 2: Relate the MLSS concentration to the return sludge concentration through $R$.
At the aeration tank inlet, a solids mass balance (with negligible solids entering with the influent) gives, per unit of influent flow $Q$:
$R\,Q\,X_r = (1+R)Q\,X$
Dividing through by $Q$: $R X_r = (1+R)X$, so
$X_r = X\times\dfrac{1+R}{R} = 3000\times\dfrac{1.3}{0.3}$
Step 3: Evaluate $X_r$.
$X_r = 3000\times4.333 = 13000$ mg/l, the same return-sludge concentration found through the direct mass balance, confirming the recycle-ratio shortcut is consistent.
Step 4: Use the solids-inventory form of the SRT definition.
The mass of biomass held in the tank is $M = V\times X = 6000\times3000 = 18{,}000{,}000$ (mg/l times m$^3$ units). At steady state, this stock must be replaced (wasted) once every $\theta_c=6$ days, so the daily solids wasting rate needed is
$\dfrac{M}{\theta_c} = \dfrac{18{,}000{,}000}{6}=3{,}000{,}000$ (same units per day)
Step 5: Since sludge is wasted from the return line at concentration $X_r$, find the flowrate that removes exactly this much solid mass per day.
$Q_w\times X_r = 3{,}000{,}000 \implies Q_w = \dfrac{3{,}000{,}000}{13000}=230.8$ m$^3$/day
Rounding, the wasting flowrate needed is about 231 m$^3$/day, matching the direct substitution method exactly.
\[ \boxed{Q_w \approx 231 \text{ m}^3/\text{day}} \]