A 4m Oil (0.90) 3.75 mm Mercury (13.57) This vertical pipeline with attached gage and manometer contains oil and mercury as shown. The manometer is open to the atmosphere. There is no flow in the pipe. Express the pressure reading at A in terms of head in meters of the oil. Do not write the unit. You will only input the numerical answer in the space provided. Unit of the Correct Answer: m Decimal Places required in the final answer: 3 B.

A 4m Oil (0.90) 3.75 mm Mercury (13.57) This vertical pipeline with attached gage and manometer contains oil and mercury as shown. The manometer is open to the atmosphere. There is no flow in the pipe. Express the pressure reading at A in terms of head in meters of the oil. Do not write the unit. You will only input the numerical answer in the space provided. Unit of the Correct Answer: m Decimal Places required in the final answer: 3 B.

Structural Analysis

6th Edition

ISBN:9781337630931

Author:KASSIMALI, Aslam.

Publisher:KASSIMALI, Aslam.

Chapter2: Loads On Structures

Section: Chapter Questions

Problem 1P

See similar textbooks

Similar questions

(Flow through Single Pipes). Determine the flow in each pipe and the pressure at the junction node, D. Assume elevation at Node, D to be 328 feet and friction factor, f, of 0.02 for all pipes. [NOTE: This is a three-part problem]. A B Elevation (ft) Length (ft) 19,680 Diameter (ft) Reservoir Pipe Part A) A 656 AD 3.28 В 590 BD 13,120 2.5 558 CD 29,520 2.5 19,680 13,120 Part B) A 656 AD 3.28 В 574 BD 3.28 CD 29,520 19,680 19,680 492 2.5 Part C) A 656 AD 3.28 В 590 BD 3.28 492 CD 19,680 3.28
this is the correct answer i just need the solution.
5. For the setup shown in figure below calculate the pressure at A. assume standard atmospheric pressure is 101.3 kPa Air H₂O W 600 mm 200 mm 140 mm 90mm -Oil specific gravity-0.83
2- Oil (p = 80o kg/m2) flow through a 5omm-diameter smooth pipe at a velocity of 2m/s, the pressure drop due to friction loss in the pipe 5023 pa. The pipe length is 1om. a- Calculate the friction factor, f. %3D b- Determine whether the flow is laminar or turbulent. C- Calculate the oil viscosity. (b) o.0157 (d) 487x10-6 N s/m2]
A fluid is flowing in a pipe 8 inches in diameter with a mean velocity of 10 feet/second. The pressure at the center of the pipe is 5 psi and the eleva-tion of the pipe above the assumed datum is 15 ft, compute the total head in feet if the fluid is a) water, b) oil (sp gr = 0.80), c) molasses (sp gr = 1.5) and d) gas (w = 0.040 psf). *can you also provide its figure, Thank you.
The figure shows a portion of a hydraulic circuit. The pressure at point B must be 250psig. When the volume of flow rate is 80gal/min. The hydraulic fluid has a specific gravity of 0.90 and a dynamic viscosity of 6.00 X 10-5 lb.s/ft2. The total length of the pipe between A and B is 25ft. The elbows are standards. Calculate the pressure at the outlet of the pump at A.
Oricul Q3: Three pipes (A, B and C) are interconnected as shown in figure (3). Determine the flow rate in each pipe. The pipes characteristics are given as follows: Pipe L (m) D (mm) f A 610 152 0.020 B 488 102 0.032 C 1220 203 0.024 Good Luck -re (2) Water qure (3) EL=7om A B EL-15m
The ligure showWs a tank dischaPging through a pipe with a nozzle at Its end. Find the discharge and the pressure at the base of the nozzle. Losses are: Tank to the base of nozzle is 5(V/2g and through the nozzle is 0.05(Va)/2 (V, is the velocity in the pipe and Vi is the velocity at the tip of the nozzle) Water D= 150mm! D,= S0mm
O -0.13 Darcy Experiment A set-up of Darcy Experiment involves measuring the pressure head at two piezometers separated a distance, L. Given the set-up shown, determine the hydraulic gradient if the hydraulic head at (1) is 24 inches, hydraulic head at (2) is 11 inches, and the travel distance is 100 inches. O 7.7 O -7.7 (1) O 0.13 e - - - -
I need the answer as soon as possible
Compute the pressure @ point n ( Pn ) as shown by the differential manometer in KPa if pressure @ point m ( Pm ) is equal 1027.66 mm Hg. air plpeline where: a= 12" b=3,2 C-4.0 d- 12 m mercury density (16 300 kghm) water pipeline
1. A pump station design fills a pressurized water tank by pumping water from a reservoir. The flow rate is 0.75 cfs. The pump is 10 feet above the reservoir, and the water tank is 100 ft above the pump. The pressure in the water tank is 10 psi. The suction and discharge lines are both (actual diameter) 6-inch Sch 40 steel (pipe roughness = 0.00015 ft). Use a kinematic viscosity of 1.21 x 10-5 ft²/s. Total pipe length is 200 ft. The suction line is 10 ft. You must account for friction loss, but you can neglect the minor losses. a. What is the head added by the pump in ft? b. What is the power added by the pump in HP (recall 1 HP = 550 ft*lb/s)? 110 ft 10 ft 0 ft