Finding Density Constant for Part (c) of Question

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To find the density for part (c) of the question, it is suggested to assume the density of the soft drink is similar to that of water, though it may vary due to sugar content. The continuity equation can be applied to relate the flow rates and densities at points 1 and 2. By using the formula ρ = ρ1A1v1/A2v2, the density can be calculated with known values of flow speeds and cross-sectional areas. The ideal gas law can also be adapted to find density, resulting in a calculated density of approximately 0.01475 kg/m^3 at point 2, which can then be used to determine the gauge pressure at that point. This approach provides a method to solve for the required gauge pressure at point 2.
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Hey I am completely stumped as to how to find the density in this following question so I can answer part (c)
Q: At a bottling plant soft drink flows in a pipe at a rate that would fill 200 375mL cans per minute. At point 1 in the pupe the gauge pressure is 152 kPa and the crossectional area is 8cm^2. At point 2, 1.35 m above point 1, the cross sectional area is 2cm^2. Find
(a) the volume flow rate - which I have found
(b) the flow speeds at points 1 and 2 - which I also have found
(c) the gauge pressure at point 2 -this one has got me in a spin :smile:

Can someone help me out?
Thanks in advance!
 
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WY said:
Hey I am completely stumped as to how to find the density in this following question so I can answer part (c)
If they didn't give you the density of the soft drink, you'll have to make some assumptions. I'd take the density to be that of water. (Of course, that's not quite right. Sugar-laden sodas probably have a density greater than water; diet sodas, less.)
 


To find the density in this question, we can use the continuity equation, which states that the volume flow rate at one point in a pipe is equal to the volume flow rate at another point in the pipe. In other words, the amount of fluid entering a pipe must be equal to the amount of fluid leaving the pipe.

Since we already have the volume flow rate and flow speeds at points 1 and 2, we can use the continuity equation to find the density. The equation is:

ρ = m/V = ρ1A1v1/ A2v2

Where:
ρ = density
m = mass
V = volume
A1 = cross sectional area at point 1
v1 = flow speed at point 1
A2 = cross sectional area at point 2
v2 = flow speed at point 2

Plugging in the values from the question, we get:

ρ = ρ1(8cm^2)(v1)/(2cm^2)(v2)

Since we don't have the density at point 1, we can use the ideal gas law to find it. The ideal gas law states that PV = nRT, where P is pressure, V is volume, n is the number of moles of gas, R is the gas constant, and T is the temperature. Since we are dealing with a liquid, we can assume that n and R are constant and cancel out. Therefore, we can rearrange the equation to solve for density:

ρ = P/RT

Plugging in the values for pressure, temperature, and the gas constant, we get:

ρ1 = (152 kPa)/(8.31 J/molK)(298 K) = 0.059 kg/m^3

Now, we can plug this value into our original equation to solve for the density at point 2:

ρ = (0.059 kg/m^3)(8cm^2)(0.5 m/s)/(2cm^2)(1.5 m/s) = 0.01475 kg/m^3

Therefore, the density at point 2 is approximately 0.01475 kg/m^3. This can then be used to find the gauge pressure at point 2 using the ideal gas law:

P2 = ρ2RT = (0.01475 kg/m^3)(8.31 J/molK)(298 K) = 36.9 kPa

 
If have close pipe system with water inside pressurized at P1= 200 000Pa absolute, density 1000kg/m3, wider pipe diameter=2cm, contraction pipe diameter=1.49cm, that is contraction area ratio A1/A2=1.8 a) If water is stationary(pump OFF) and if I drill a hole anywhere at pipe, water will leak out, because pressure(200kPa) inside is higher than atmospheric pressure (101 325Pa). b)If I turn on pump and water start flowing with with v1=10m/s in A1 wider section, from Bernoulli equation I...

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