A converging tube has a cross section area at the inlet of 0.75 m^2 and has a fluid velocity of 250 m/s with a corresponding density of 1.0 kg/ [m] ^3. At the outlet, the cross section area is 0.57 [m] ^2 and the corresponding density of 1.1750kg/ [m] ^3. Calculate for the final velocity. *

A converging tube has a cross section area at the inlet of 0.75 m^2 and has a fluid velocity of 250 m/s with a corresponding density of 1.0 kg/ [m] ^3. At the outlet, the cross section area is 0.57 [m] ^2 and the corresponding density of 1.1750kg/ [m] ^3. Calculate for the final velocity. *

College Physics

11th Edition

ISBN:9781305952300

Author:Raymond A. Serway, Chris Vuille

Publisher:Raymond A. Serway, Chris Vuille

Chapter1: Units, Trigonometry. And Vectors

Section: Chapter Questions

Problem 1CQ: Estimate the order of magnitude of the length, in meters, of each of the following; (a) a mouse, (b)...

See similar textbooks

Similar questions

A fluid with a density of 920 kg/m³ and an absolute viscosity of 1.75x103 kg/m s is passing thru a 7.4 cm diameter tube at a mass flow rate of 3.9 kg/s. What is the Reynold's number of this fluid flow?
A liquid of density 1370 kg/m³ flows steadily through a pipe 7. of varying diameter and height. At Location 1 along the pipe, d, the flow speed is 9.13 m/s and the pipe diameter dj is 10.3 cm. At Location 2, the pipe diameter d2 is 16.1 cm. At Location 1 Location 1, the pipe is Ay = 9.05 m higher than it is at Location 2. Ignoring viscosity, calculate the difference AP between the fluid pressure at Location 2 and the fluid pressure at Location 1. Ду Location 2 ΔΡ- Ра d,
5) A disk of mass m = 75.0 g and radius r = 4.20 cm glides across an air table at a speed v = 1.5 m/s. It makes a glancing collision with a hoop of radius R = 5.80 cm and mass M = 130 g (initially at rest) such that their rims just touch. Because their rims are coated with instant-acting glue, the two objects stick together and rotate after the collision. a) What is the angular momentum of the system relative to the center of mass? b) What is the angular speed about the center of mass?
Water moves through a constricted pipe in steady, ideal flow. At the lower point shown in the figure below, the pressure is 1.65 ✕ 105 Pa and the pipe radius is 2.60 cm. At the higher point located at y = 2.50 m, the pressure is 1.29 ✕ 105 Pa and the pipe radius is 1.40 cm. a) Find the speed of flow in the lower section. b) Find the speed of flow in the upper section. c) Find the volume flow rate through the pipe.
Solve
Hi please help: A cylindrical container with a cross-sectional area of 69.2 cm^2 holds a fluid of density 856kg/m^3. At the bottom of the container the pressure is 128kPa. Assume Pat= 101kPa A. What is the depth of the fluid? B. Find the pressure at the bottom of the container after an additional 2.25x10^-3m^3 of this fluid is added to the container. Assume that no fluid spills out of the container
An ideal (non-viscous, incompressible) fluid flows through a pipe of fixed diameter that is positioned vertically with the fluid flowing from bottom to top. The pipe is 1 meter long with a diameter of 1 cm. The fluid density is 900 kg/m3 and the fluid flows at a speed of 10 m/s. At the bottom, the pressure is 13,000 N/m2. What is the pressure at the top of the pipe? (Use the valueg = 10 m/s^2.) 1300 N/m^2 4000 N/m^2 O 1000 N/m^2 12000 N/m^2 O N/m^2
Water is flowing through a pipe with a constriction. The area of the narrow section is one-half the area of the wide section. If the velocity of the incompressible fluid is 3.2 m/s in the narrow section, then what is the velocity of the fluid in the wide section? Multiple Choice 0.9 m/s 1.0 m/s 1.6 m/s 1.8 m/s 1.9 m/s
A liquid of density 1310 kg/m³ flows steadily through a pipe of varying diameter and height. At Location 1 along the pipe, the flow speed is 9.61 m/s and the pipe diameter di is 10.1 cm. At Location 2, the pipe diameter d₂ is 17.9 cm. At Location 1, the pipe is Ay = 9.19 m higher than it is at Location 2. Ignoring viscosity, calculate the difference AP between the fluid pressure at Location 2 and the fluid pressure at Location 1. AP= Pa Location 1 z Ay Location 2 d₂
A liquid of density 1350 kg/m3 flows steadily through a pipe of varying diameter and height. At Location 1 along the pipe, the flow speed is 9.83 m/s and the pipe diameter ?1 is 10.9 cm. At Location 2, the pipe diameter ?2 is 17.3 cm. At Location 1, the pipe is Δ?=9.47 m higher than it is at Location 2. Ignoring viscosity, calculate the difference Δ?between the fluid pressure at Location 2 and the fluid pressure at Location 1.
4.0 mm 16. Consider the following diagram. (let air be an ideal, incompressible fluid) 2.0 cm 1200 cm'/s a. If the air is found to have a flow rate of 1200 cm3/s as it leaves the 4.00 mm diameter pipe, what is the velocity of the air in both segments of the pipe? b. If the density of air is 1.28 kg/m3 and the end of the pipe on the right opens up to the atmosphere, what is the pressure of the pipe at the 2.00 cm diameter section? C. If the fluid in the bottom of the U-tube is mercury with a density of 13,600 kg/m3 what is the difference between the surface levels of both sides of the tube, marked as h in the diagram?
A liquid of density 1370 kg/m³ flows steadily through a pipe 7. of varying diameter and height. At Location 1 along the pipe, d, the flow speed is 9.83 m/s and the pipe diameter dị is 11.5 cm. At Location 2, the pipe diameter d2 is 16.9 cm. At Location 1 Location 1, the pipe is Ay = 9.65 m higher than it is at Location 2. Ignoring viscosity, calculate the difference AP between the fluid pressure at Location 2 and the fluid pressure Ду at Location 1. Location 2 AP = Ра d,