PLEASE SOLVE THE HIGHLIGHTED QUESTION. ATTACHED IS THE SOLUTIONS TO THE ORIGINAL PROBLEM STATEMENT. THIS PROBLEMS REQUIRES HTU-NTU CONCEPTS TO BE SOLVED PLEASE USE THEM!

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Use the information for the problem below to find the height of packing for the rectifying and stripping ections of the column. In the stripping section, HL=0.6ft and HG=1.3ft. In the rectifying section, HL=0.8 t and HG=1.2ft. The solution to the original problem is given after the original problem statement. a. Find the height of an overall gas phase transfer unit at 4 locations in each section. b. Find the average height of an overall gas phase transfer unit for each section. c. Find the number of transfer units for each section. d. Find the height of packing for each section. SOLVE HIGHLIGHTED PART Original problem statement: The feed to a distillation column is 100kmol/h,42 mole % more volatile component (MVC), and a compressed liquid with q=1.5. The distillate product is 96 mole %MVC and the bottoms is 4.0mole%MVC. The column has a total condenser and a partial reboiler. CMO applies. The external reflux ratio is 2.0. Find a. the number of trays b. the location of the ideal feed tray c. the flowrates for reflux and liquid and vapor in the rectifying section and the stripping section d. the mole fractions of liquid and vapor leaving the 3rd tray from the top. overall balance around reborler L=B+v V=LB=232.6kmol/h58.7kmod/h=173.9kmol/h check: io some of v condensed to bring the feed to the saturation T ? is v