Design a shell-and-tube exchanger for the following duty. 20,000 kg/h of kerosene (42° API) leaves the base of a kerosene side-stripping column at 190 °C and is to be cooled to 80 °C by exchange with 75,000 kg/h light crude oil (34° API) coming from storage at 30 °C. The kerosene enters the exchanger at a pressure of 5 bar and the crude oil at 6.5 bar. A pressure drop of 1 bar is permissible on both streams. Allowance should be made for fouling by including a fouling factor of 0.0003 (W/m². °C)' on the crude stream and 0.0002 (W/m². °C)" on the kerosene stream.