Heat and Mass Transfer

A tubular heat exchanger has overall heat transfer coefficient $U = 800\text{ W/(m}^2\cdot\text{K)}$ and surface area $A = 5.0\text{ m}^2$. If the log mean temperature difference is $\text{LMTD} = 25.0^\circ\text{C}$, calculate the rate of heat transfer in $\text{kW}$.