At a soft drink bottling plant, a horizontal section of pipe carrying citric acid in liquid form goes from a cross-sectional area of 8.00 cm2, fluid flow speed of 200 cm/s, and pressure of 1.40 105 Pa to a section of pipe with a cross-sectional area of 3.20 cm2. The density of the citric acid is 1660 kg/m3. For the section of smaller pipe, determine the liquid flow speed and the liquid pressure. (a) the liquid flow speed: ? (b) the liquid pressure: ?

A liquid of density 1170 kg/m3 flows steadily through a pipe of varying diameter and height. At Location 1 along the pipe, the flow speed is 9.75 m/s and the pipe diameter d1 is 11.7 cm. At Location 2, the pipe diameter d2 is 16.3 cm. At Location 1, the pipe is Δy=8.87 m higher than it is at Location 2. Ignoring viscosity, calculate the difference ΔP between the fluid pressure at Location 2 and the fluid pressure at Location 1.

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 manometer using oil (density 0.900 g/cm3) as a fluid is connected to an air tank. Suddenly the pressure in the tank increases by 7.48 mmHg. Density of mercury is 13.6 g/cm3. (A) By how much does the fluid level rise in the side of the manometer that is open to the atmosphere? ____cm (b)By how much does the fluid level rise in the side of the manometer that is open to the atmosphere if the manometer used mercury instead? ___cm

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.

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A level (horizontal) pipe contains a non-viscous, incompressible fluid with a density 1200 kg/m³ that is flowing steadily. At one position within the pipe, the pressure is 300 x 103 N/m2 and the speed of the flow is 20.0 m/s. At another position, the pressure is 200 x 103 N/m². What is the speed of the flow at this second position?

Water has a density of 1500 kg⋅⋅ m-3. One section of a horizontal pipe has a cross-sectional area that is 0.74 times another section. The gauge pressure at the smaller section is 18.5 ××104 Pa, and water flows through the section at a speed of  15.1 m⋅⋅s-1. Calculate the gauge pressure (in ×× 104 Pa) in the wider section of the pipe.