Hello .. please i need answer for this question .. 3,4,5,6?

4. The caiculated surface area of the packing in squared meters is: (1 Point) 67.0 27.80 97.80 7.80 5. The required volume of the packing for this cooling tower in m3 ic: ES (1 Point) 3.01m2.1.50m3.2.01m3.1.01m3 5. The evaporated cooling water rate is in kg/h is: : (1 Point) 3697kgh 9697kg/h 8697kg/h 9697kg/h 3. In a chemical process, heat exchangers E-102. E-104 B E-105 use cooling wster trom a single counterllow induced draft cooling tower with available packing surface ares concentration of 77 m2/m3. The cooling water enters the process at 25C from the cooling tower and is zeturned to the cooling tower at 45C. The heat duty of E102 is 5660Mu/h,8350M/h for E104 and 9850 M./h for E-105. Given data: Cooling water density. 1000kg/m3, water specitic heat 4.18k//kg/C latent heat of vaporization for water 24108M/kg. Woter concentration rate is: 1.50gal/t t/min. 1gal=3.785 utre, 1m=3.28ft, cost of makeup water 50.067/1000kg. T(f)=1.8T(C)+32 Answer the following questions: The required cooling water circulation rate in kg/h is " DS (1 Point) 175407kgh 34540t hgm 205407kg/h 295400kg/h