In the pipe system shown below the pipe has a diameter of $25cm,$ and it is $560m$ long from $A$ to $S.$ The equivalent roughness height of the pipe, e$,$ is $0\mathrm{.}13mm.$ The kinematic viscosity is $n=1\mathrm{.}1310-6m\frac{2}{s}.$ The minor head loss coefficients are: $Ke=0\mathrm{.}5$ for entrance losses, and $Kd=1\mathrm{.}0$ for exit losses. The water surface elevations are $h1=750m,$ and $h2=615m.$ The discharge is $Q=445\frac{L}{s}.$

Determine the pressure head at $S$ in $m.$

$\backslash$table$[[$Diameter of Pipe, $D=,25],[$Length from $A$ to $S=,560],[$Pipe roughness, e $=,0\mathrm{.}13],[$Total head in reservoir $A=,750],[$Total head in reservoir $B=,615],[$Elevation head at $S=,715],[Q=,445]]$

Report $3-5$ sig fig$$: don't include units