I just help on last 6 problems please

P2 U B Open to atmosphere A P1 A liquid flows through a piping system from P1 to the top of a structure at P2 Sections A and B are 2 sch 40 pipe The pump suction piping is 2 sch 40 pipe AND CAN BE ASSUMED FRICTIONLESS Section C is 1.5 sch 40 pipe The piping system is intended to provide liquid at a rate of 65 gpm while maintaining a P2 pressure of 3 psig. The flowrate at P1 and P2 are the same. (ie.. there is no splitting or branching of the flow) The friction factor, f (fanning), can be assumed to be 0.007 The pump efficiency can be assumed to be 45% Given: The density of water is 62.4 lbm/ft3 The specific gravity of the fluid is 0.75 The viscosity of the fluid is 10 CP The vapor pressure of the fluid is 6 psia The piping system dimensions are as follows: A=26ft; B=175ft ; C=80ft ; L=18ft A and B section C section fitting_type fitting K value number of fittings number of fittings 90 degree bend 9f 10 8 gate valve 8f 4 6 check valve 30 f 3 1 tee (run) 15 f 3 3 tee (branch) 54 f 2 reducer K1=0.5*(1-B^2)^2 1 NOTE: B = (smaller flow diameter)/(larger flow diameter) 2 = What is the volumetric flow, ft3/s, through the pipe? .14482 What is the velocity in sections A and B, ft/s? 6.2146 What is the velocity in section C, ft/s? 10.2433 What is the pressure at P1, psig? -5.85 For the next 4 questions, do not include the pressure drop due to elevation changes What is the pressure drop, psi, due to pipe in sections A + B? 6.371 What is the pressure drop, psi, due to pipe in section C? 8.84 What is the pressure drop, psi, due to the pipe and fittings in sections A+B? 6.8744 What is the pressure drop, psi, due to the pipe and fittings in section C? 10.0112 10.012130023129 What is the pressure drop, psi, due to the elevation change from P1 to P2? What is the required TDH, ft, of the pump? What is the NPSHA, net positive suction head available, ft, for the pump? What is the required hydraulic horsepower, hp? What is the BHP, brake horsepower, of the pump? In order to select a pump for this system, the system curve must be solved for serveral additional flowrates. With this in mind, what is the TDH, ft, required when the pump is running and 0 gpm if flowing through the system