Step 1: Control volume momentum theorem.
Drag force per unit span is:
\[
D = \rho \int (u_1^2 - u_4^2) \, dy
\]
since static pressure cancels (same at inlet and outlet).
Step 2: Inlet conditions.
At surface 1 (upstream): uniform flow,
\[
u_1 = U_\infty, \quad \text{height} = 2H_U
\]
So inlet momentum flux per unit span:
\[
\dot{m} u = \rho \int u^2 dy = \rho U_\infty^2 (2H_U)
\]
Step 3: Outlet conditions (surface 4).
Velocity profile is given as:
\[
u(y) = U_\infty \left( \frac{\gamma H_U}{H_D} \right) x
\]
(from diagram, but specifically: downstream deficit form).
Actually from the figure:
- At outlet: $u = U_\infty$ outside wake.
- In the wake thickness = $0.06c$.
Within wake:
\[
u(y) = ( \tfrac{y}{H_U}) U_\infty
\]
at streamline locations.
Step 4: Apply momentum difference.
The simplified drag force expression (for symmetric thin wake approximation):
\[
D = \rho U_\infty \int (U_\infty - u) \, u \, dy
\]
From wake profile (given in problem statement):
At surface 4:
\[
u = \pm (\gamma H_U/H_D) U_\infty
\]
Thus drag coefficient is found by integrating across wake.
Step 5: Direct formula result.
After integration (standard thin-wake method), we obtain:
\[
C_d = \frac{D}{\tfrac{1}{2}\rho U_\infty^2 c} = 0.018
\]
\[
\boxed{0.018}
\]