Structural Analysis
6th Edition
ISBN: 9781337630931
Author: KASSIMALI, Aslam.
Publisher: Cengage,
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- A decision has to be made on wether touse 3 in or 4 in ID tubing for a well with the flowing conditions: steady state flow Initial =2500 psi Pressure PI=2.0STB/psi Bubble point pressure =1200 psi Depth(TVD)=5000ft Required THP=300psi GOR=200 SCF/bbIarrow_forwardSolution step by step..arrow_forwardholes Water flows through a 100 mm diameter pipe with a velocity of 0.015 m/s. If the kinematic viscosity of water is 1.13× 106 m²/s. The friction factor of the pipe material isarrow_forward
- 1. An oil of sp. gr. 0.9 is contained in a vessel. At a point the height of the oil is 50 m. Find the corresponding height of water at the point.arrow_forwardPlease need answerarrow_forwardTROROPITS A e Sign i Example 10: A 40-lb, 0.8-f8-diameter, 1-ft-tall cylindrical tank slides slowly down a ramp with a constant speed of 0.1 ft's astshown in Figure below. The uniform-thickness oil layer on the ramp has a viscosity of 0.2 Ib s/t. Determine the angle, 6, of the ramp. SConvert POr 0.002 01 hsarrow_forward
- A smooth concrete pipe with a 1.5 ft diameter carries carbon tetrachloride at 20 C from a tank to a facility 1 mile away, where it discharges into the air. The pipe begins in the tank 3 feet below the surface and descends on a 1:100 (vertical: horizontal) slope. Determine the flow rate, assuming minor losses are negligible.arrow_forward4.3 A homogeneous circular cylinder of length h, radius r and specific gravity S, floats in water. It is noted that r= 2/3h Under which one of the following conditions will the flotation be unstable? (a) 0.11 < S< 0.22 (b) 0.22arrow_forwardSHOW SOlution Ans. F= 733.16kN 1.844m from the bottom of the tank parallel to the gatearrow_forward6. Crude oil of relative density 0.91 (viscosity 1.24 poise) is pumped through a supply pipeline 75 mm diameter, where a flow of 420 litres/min takes place between pipeline section 1.25 km from the feeder reservoir, and section 1.60 km from the feeder reservoir. A piezometer records a pressure of 12425 Pa at the section D. Taking head loss due to friction into consideration as per viscous flow or turbulent flow prevailing, evaluate the pressure head at section 2.arrow_forwardThe pipe bend shown is in a horizontal plane. Oil with a specific gravity of 0.86 enters the reducing bend at section A with a velocity of 3.2 m/s and a pressure of 150 kPa. Neglecting head loss, determine (a) The velocity at section B, V3 (m/s) (b) The pressure at section B, ps (kPa) (c) FMx (N) de = 100 mm B da = 150 mm 30°arrow_forwardA well produces 850STBD amd1.67MMCF/STB the tubing diameter is4.5at a certain depth pressure is1002 psi calculated density for oil and gas is 805Kg/m^3 and 0.715kg/m^3 respectively Bo is 1.1 ,Bg=0.01ft^3/scf and Rs is 255 scf/stb calculated fluid slippage ,liquid hold up ,type of flow in the tubing and real phase velocities Using this equation to calculate itarrow_forwardarrow_back_iosarrow_forward_ios
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