Please answer all with work

atmoschere Aliquid flows through a piping system from Ps to the top of a structure at P2 Sections and Bare 2 sch 40 pipe The puno suction proine is che AO CAN BE ASSUMED FRICTIONLESS Section 15sch 40 pipe The piping stem is intended to provide liquidata rate of som while maintaining a P2 pressure of 2 psg The flowrate at 1 and 2 are the same. Be there is no splitting or branching of the tow The friction factor, Fanning), can be sumed to be 0.00 The purp efficiency can be assumed to be Given The demity of water $ 62.4tbmit - The specific gravity of the fluid is 0.15 The Vhcosity of the fuld stop The vapor pressure of the fluid ipsia The piping system dimensions are as follows ABC And section Csection hitting type stine Kvalue be of weberete 90 degree bend 71 30 gate valve 51 6 5 check valve . tee run 18 2 tee branch 521 . 3 reducer KTO ST1-3 2/2 1 NOTE: smaller flow diameter larger flow diameter) What is the volumetric flow ft3/s, through the pipe! What is the velocity in sections A and B. 7/22 What is the only is section, What is the pressure at Pt. For the next questions, do not include the pressure drop due to elevation changes what the pressure drop. psi, due to pipe la sections - what is the pressure drop, psi, due to pipe section What is the pressure drop, psi, due to the pipe and fittings in sections A-22 What is the pressure drop, psi, due to the pipe and fittings in section What is the pressure drops due to the elevation change from 1 tot What is the required TD, ft, of the pump? What is the NPA, net positive suction head available it for the pump? What is the required hydraulic horsepower hp! What is the BHP. trahe horsepower of the pump In order to select a pump for this system, the stunt be solved for serveral additional flowiates. With this in mind, what the Tom, t. required when the pump is turning and am af flowing through the system