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A small unit is needed to treat light crude that has a density equal to 876m3kg. The crude oil is produced at 55500hkg and then passes through the stabilization tank for 10min before it is pumped to a heat exchanger. Steam thru the Shell-side is used to heat the crude oil up to meet the Reactor temperature T=59C and P=30 bar. a. Estimate the required size and type for the tank while considering the 20% design margin. b. Determine the type of equipment needed for the pumping unit that consumes 714kW to deliver the fluid to the separator considering a pressuredrop equal to 15 bar. Justify your results. c. Given Log Mean Difference T equal to 65C, estimate the number of tubes and relevant passes needed for the fluid. Perform all necessary calculations based on the relevant data available in the lectures without any assumptions. d. Estimate the dimensions and volume of the Liquid-Liquid separator