I might have been not clear enough in explaining the situation.
The flow is normal to the surface of the cylinder. The cylinder is fixed to the piping wall.
Piping is DN50, and the cylinder has a diameter of 20 mm and a length of 35 mm.
On the internet I found a picture of how the flow is around the cylinder in this existing situation.
Flow will be approx. 18 m3/h (is approx. 2,5 m/s) and the fluid is light viscous (estimated at 10 mPas), which makes flow turbulent.
Pressure drop is very low, but it needs to be quantified.
DYV