WATER at $90C$ IS PUMPED at A VOLVIETRIC FLOURATE OF $0,2\frac{m^3}{m}ia$ THROUCH A HEAT EXCHANGER TO ANOTHER STORAGE TANK THE HEAT EXCHANGER REMOVES $700kW$ OF ENEREY FROTI THE FLOWING WATER WHILE THE PUMP HAS A RATING OF $1\mathrm{.}5kW.$ THE WATER STARTS AND ENDS ITS JOURNEY AT REST IN STORAGE TANKS WITH THE SECOND STORAGE TANK POSITIONED $16M$ ABOVE THE FIRST. WHAT TEMPERATURE WILL THE WATER IN THE SECOND $($FINAL TANK$)$ BE AT $($ASSUME NC FRICTION LOSSES AND PERFECTLY INSULATED PIPES$).$