A liquid with a specific gravity of 2.6 and a viscosity of 2.0 cP flows through aNominal 2-inch schedule 40 commercial steel pipe. You need to know the expected pressuredrop (loss of pressure per unit length in the pipe).(a) Find the pressure drop in psi for 100 ft of pipe if the flow is 0.5 gpm. (b) Find the pressure drop in psi for 100 ft of pipe if the flow rate is 50 gpm.

A liquid with a specific gravity of 2.6 and a viscosity of 2.0 cP flows through aNominal 2-inch schedule 40 commercial steel pipe. You need to know the expected pressuredrop (loss of pressure per unit length in the pipe).(a) Find the pressure drop in psi for 100 ft of pipe if the flow is 0.5 gpm. (b) Find the pressure drop in psi for 100 ft of pipe if the flow rate is 50 gpm.

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

Section: Chapter Questions

Problem 1.1MA

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A liquid with a specific gravity of 2.6 and a viscosity of 2.0 cP flows through aNominal 2-inch schedule 40 commercial steel pipe. You need to know the expected pressuredrop (loss of pressure per unit length in the pipe).(a) Find the pressure drop in psi for 100 ft of pipe if the flow is 0.5 gpm. should be .0014 psi(b) Find the pressure drop in psi for 100 ft of pipe if the flow rate is 50 gpm. should be 5.11 psi
A 300 mm x 150 mm venturimeter is provided in a vertical pipeline carrying oil of specific gravity 0.9, flowing upward. The difference in elevation of the throat section and entrance section of the venturimeter is 300 mm. The differential U – tube manometer shows a gauge deflection of 250 mm.Calculate i) The discharge of oil ii) The pressure difference between entrance and Throat section. Take : coefficient of discharge of venturimeter is 0.98
1. An 80 mm schedule 40 steel pipe is 1800 m long and carries a lubricating oil between 2 points A and B such that the Reynolds number is 1200. Point B is 10 m higher than point A. The oil has a specific gravity of 0.85 and dynamic viscosity of 6.51 X 10-1 Pa.s. If the pressure at A is 345 KPa, calculate the pressure @ B. 2. Determine the energy loss for a sudden contraction from a 4 in schedule 80 steel pipe to a 1.5 in schedule 80 pipe for a flow rate of 250 gal/min. 3. Determine the equivalent length in meters of pipe of a quarter open gate valve placed in a DN 250 schedule 40 pipe.
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Use g=32.2 */sec2 (9.81 m/s2) and 60°F (16°C) water unless told to do otherwise.• Google schedule-40 pipe’s thickness at different nominal size to obtain the innerdiameter of the pipe for accurate determinaLon of flow velocity.• Must show your work to support your selecLon. Otherwise, no points will be given.• No peer discussion is allowed.. A cylindrical tank 5 ft high has a constant diameter of 4 ft is full of water. The tank has a hole2. A cylindrical tank 5 * high has a constant diameter of 4' is full of water. The tank has a holein its bo]om that measures 0.1ft^2. All losses are insignificant. How long will it take for the tankto empty? Note that you can NOT assume a staLc head and constant flow rate because thewater head in the tank decreases as the water flows out of the tank (A) 35 sec(B) 70 sec(C) 105 sec(D) 140 sec
A pump is used in a building to lift water from a ground floor. The pump is pushing 60l/sec of water through a 0.1m diameter to above floor which is 5m high If the average velocity in the pipe is 6m/s. what will major energy loss if the dynamic viscosity of water is 8.9 x 10-4s. Due to vibration and noise issue in a pipe the velocity of pump is decided to set at 2.5 m/s. What will new major energy? Calculate the minor energy loss if length of the pipe is 15m. use f = 0.03, = 1, = 0.9 Analyse the relationship between frictional energy loss under different gravitational flow conditions
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SOLVES TEP BY STEP DONT USE CHATGPT DONT USE AI 3. An oil of viscosity 1.8 cp and relative density 0.8 is contained in an open tank located above the application site. A 1.5-inch diameter pipe extends vertically from the bottom of the tank and is 5 m long. The oil level in the tank remains constant at 3 m above the bottom of the tank. In a case with friction the discharge speed can be obtained in the form of the following Equation. Calculate the flow rate of oil discharged per hour. Assume that the pipe is commercial steel (ε=0.05 mm). V= 2gh +f-
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