Please solve it by Aspen+ V12

please put screanshot

PROBLEM 2 DESIGN OF PROPANOL CONDENSER Saturated n-propanol at 2 bar and 245F flowing at a rate of 750kmol/h is to be condensed in a shell and tube heat exchanger using water at 1 bar and 50F flowing at a rate of 4700 kmol/h. Design the exchanger so that the temperature of water rises to 200F and the hot fluid is at tube side. Use Property method "NRTL-2". Take minimum approach temperature as 10F. Use 1) Shortcut method 2) Use same file for detailed design of Shell and Tube Exchanger. DATA GIVEN PRESSURE DROP: Method: Darcy's law, Max. Pressure drop: 0.5 U METHODS: Film co-efficient and U correction factor as 0.9 . FILM CO-EFFICIENT: from geometry; Fouling factor: 0 ; Scaling factor: 0.9 . SHELL: Number of tube passes is 4 ; inside shell diameter is 50 in. TUBES: Tube number is 180 , pattern triangle, length 7ft, pitch 2 in., inner diameter 1.8 in and outer diameter 1.95in. Baffles: Number of baffles all passes is 12 , baffle cut 0.25 . NOZZLES: Shell inlet and outlet nozzle diameter is 8 in. Tube side inlet and outlet nozzle diameter is 6 in