Note: Please fill your answer in eth table and submit this answer-sheet along with Hysys file for grading Styles Q1. You are a process design engineer at a reputed company named NMM in Abu Dhabi. You are designing a plant where n-heptane will be transported from storage area to the reactor. > You have two design to consider Design A: Use a big pump to deliver the feed to the reactor (with 35% Adiabatic efficiency) O Design B: Using a set of three pumps connected in series (each pump has 37% efficiency and can increase pressure by a maximum of 600kpa) The desired pressure at the reactor is 1950 kpa The feed stream (Inlet/IN) consist of pure n-Heptane, flowrate is 1000 Kgmoor 25 C and 200 kpa. Use Peng Robinson Equation of state as property method You can use balance to calculate net energy Design A pump names should be your first name > > Note: Hysys Filename must be your lastname_last four digit of KUID (example nafees 1234). The design that will require lowest energy will be preferred choice. Inlet Pressure Temperature Molar Flow Master Comp Mole Frac (n-Heptane) 200.0 kPa 15.00 C 1000 kgmole/h 1.0000 Outlet Pressure 1950 kPa P-100 Outlet Inlet E P2 IN3 P3 Outlet2 P1 IN2 IN P2 Energy P3 Energy P1 Energy 2 Net BAL-1 Temperature Molar Flow Master Comp Mole Frac (n-Heptane) 15.00 C 1000 kgmole/h Outlet Pressure 1950 kPa 1.0000 Inlet P-100 Outlet E P2 IN3 P1 IN2 P3 Outlet2 IN P1 Energy P2 Energy P3 Energy Net BAL-1 Answer the followings Student Answer Maximum Grade Student Grade 2 1 1. Which design is better Design A or Design B ii. Energy required in design A (kW) iii. Energy required in design B (KW) iv. Find molar volume of outlet stream v. Viscosity of "IN" Stream vi. Net stream's heat Flow (kJ/h) vill Pressure head of pump in design Am 2 1 2 1 Page 1 of 1 Note: Please fill your answer in eth table and submit this answer-sheet along with Hysys file for grading Styles Q1. You are a process design engineer at a reputed company named NMM in Abu Dhabi. You are designing a plant where n-heptane will be transported from storage area to the reactor. > You have two design to consider Design A: Use a big pump to deliver the feed to the reactor (with 35% Adiabatic efficiency) O Design B: Using a set of three pumps connected in series (each pump has 37% efficiency and can increase pressure by a maximum of 600kpa) The desired pressure at the reactor is 1950 kpa The feed stream (Inlet/IN) consist of pure n-Heptane, flowrate is 1000 Kgmoor 25 C and 200 kpa. Use Peng Robinson Equation of state as property method You can use balance to calculate net energy Design A pump names should be your first name > > Note: Hysys Filename must be your lastname_last four digit of KUID (example nafees 1234). The design that will require lowest energy will be preferred choice. Inlet Pressure Temperature Molar Flow Master Comp Mole Frac (n-Heptane) 200.0 kPa 15.00 C 1000 kgmole/h 1.0000 Outlet Pressure 1950 kPa P-100 Outlet Inlet E P2 IN3 P3 Outlet2 P1 IN2 IN P2 Energy P3 Energy P1 Energy 2 Net BAL-1 Temperature Molar Flow Master Comp Mole Frac (n-Heptane) 15.00 C 1000 kgmole/h Outlet Pressure 1950 kPa 1.0000 Inlet P-100 Outlet E P2 IN3 P1 IN2 P3 Outlet2 IN P1 Energy P2 Energy P3 Energy Net BAL-1 Answer the followings Student Answer Maximum Grade Student Grade 2 1 1. Which design is better Design A or Design B ii. Energy required in design A (kW) iii. Energy required in design B (KW) iv. Find molar volume of outlet stream v. Viscosity of "IN" Stream vi. Net stream's heat Flow (kJ/h) vill Pressure head of pump in design Am 2 1 2 1 Page 1 of 1
