I need help on just last 5 problems.

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 = O 6.216 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? O 10.243 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? What is the pressure drop, psi, due to pipe in section C? What is the pressure drop, psi, due to the pipe and fittings in sections A+B? What is the pressure drop, psi, due to the pipe and fittings in section C? 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 = O 6.216 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? O 10.243 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? What is the pressure drop, psi, due to pipe in section C? What is the pressure drop, psi, due to the pipe and fittings in sections A+B? What is the pressure drop, psi, due to the pipe and fittings in section C