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victoriafello
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A power station is supplied with water from a reservoir. A pipeline connects the reservoir to the turbine hall
The flow of water through the pipeline is controlled by a valve which is located exactly 500 metres below the surface of the water in the reservoir. The pipeline is 0.30 m in diameter.
Calculate the static pressure at the lower end of the pipeline when the valve is in the closed position
relivant equation
bernouliis equation
P + 1/2 rho v^2 + pgh = constant
my attempt so far -
for the surface of the reservior
P1 - atmospheric pressure 1.00x10^5
rho1 = density of water 1.00x10^3
g = 9.81
h1 = 0
v1 = 0 (water is not moving)
for the bottom of the pipe
p2 - unknown
rho 2 = density of water 1.00x10^3
g = 9.81
h2 = 500
v2 - 0 (water not moving)
rearrange for p2
p2 = 1/2 Rho (V1-V2)g(h1-h2)-P1
this gives
1/2*1.00x10^3+1.00x10^3*9.81*(0-500)-1.00x10^5
so p2 = 4904500
or 4.9x10^6
can someone let me know if i went wrong anywhere as this doesn't look correct? i don't think the diamter of the pipe is important for this part of the equation,
The flow of water through the pipeline is controlled by a valve which is located exactly 500 metres below the surface of the water in the reservoir. The pipeline is 0.30 m in diameter.
Calculate the static pressure at the lower end of the pipeline when the valve is in the closed position
relivant equation
bernouliis equation
P + 1/2 rho v^2 + pgh = constant
my attempt so far -
for the surface of the reservior
P1 - atmospheric pressure 1.00x10^5
rho1 = density of water 1.00x10^3
g = 9.81
h1 = 0
v1 = 0 (water is not moving)
for the bottom of the pipe
p2 - unknown
rho 2 = density of water 1.00x10^3
g = 9.81
h2 = 500
v2 - 0 (water not moving)
rearrange for p2
p2 = 1/2 Rho (V1-V2)g(h1-h2)-P1
this gives
1/2*1.00x10^3+1.00x10^3*9.81*(0-500)-1.00x10^5
so p2 = 4904500
or 4.9x10^6
can someone let me know if i went wrong anywhere as this doesn't look correct? i don't think the diamter of the pipe is important for this part of the equation,