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Shalnov [3]
2 years ago
7

Estimate the uncertainty in a 22 m/sec air velocity measurement using a Pitot tube at 20C. Assume the atmospheric pressure is 1

00 kPa and that R and the density of water, H O2  are known with high enough accuracy to consider them as constants (zero uncertainty). The pressure for each tap is measured with separate manometers that have a resolution of 0.5 mm. The manometers use water as the fluid and each are oriented vertically. The absolute pressure (which gives you the density of air) is known with an uncertainty of 0.1 kPa. The temperature is known with an uncertainty of 1C. Assume the stagnation pressure, pt, is indicated by a static height of 7 mm.

Engineering
1 answer:
ivanzaharov [21]2 years ago
4 0

Answer:

Check the explanation

Explanation:

In calculating the second version of velocity that is expected velocity, which involves the division of the overall amount of estimated story points by the amount of sprints. Take for instance, if the development team estimates a total of 150 points over five sprints, then we can say that the team's expected velocity would be 30 points per sprint.

Kindly check the attached image below to see the step by step explanation to the question above.

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Supercharging is the process of (a) Supplying the intake of an engine with air at a density greater than the density of the surr
iVinArrow [24]

Answer:

a)supplying the  intake of an engine  with air at a  density greater  than the density  of the surrounding  atmosphere

Explanation:

Supercharging  is the process of  supplying the  intake of an engine  with air at a  density greater  than the density  of the surrounding  atmosphere.

By doing this , it increases  the power out put  and increases the  brake thermal  efficiency of the  engine.It also  increases the  volumetric efficiency of the  engine.

So the our  option a is  right.

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3 years ago
This color curb is where parking is permitted for a limited time. The time constraints for that park will either be painted on t
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Answer:yellow

Explanation:

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Read 2 more answers
A tank of final volume 10 m3 contains compressed air at 15◦C. The gage pressure in the tank is 4.50 MPa.
GarryVolchara [31]

Answer:

The answers to the question are as follows

(a) W = -175.6 MJ

(b) W = -329.256 MJ

The peak temperature of the isentropic compression process is 886.974 K

Explanation:

(a) We are given the initial conditions as

v₂ = 10 m³

T₂ = 15 °C

p₂ (gauge) = 4.5 MPa gauge  → 4.5 MPa + 1 atm = 4.5 MPa + 101325 Pa = 4.601 MPa

p₁ = 1 atm

Therefore isothermal compression we have the work done given by

W_{12} = p_{2}  v_{2}ln(\frac{v_{1} }{v_{2} } ) per unit mass of the given gas, hence

From the relation

p₁·v₁ =p₂·v₂  therefore v₁ = p₂·v₂/p₁  = 4.6 MPa× 10 m³/(1 atm) = 4.6 MPa× 10 m³/(‪101325‬ Pa) = 454.115 m³

Therefore W₁₂ = 101325 Pa × 454.11 m³× ㏑((10 m³)/(454.115 m³)) = 46013250×(-3.82) = -175575813.855 J = -175.6 MJ

W = -175.6 MJ

(b) For isentropic compression we have

W = m×cv×(T₂ -T₁)

\frac{p_{1} }{p_{2} }  = (\frac{v_{2} }{v_{1} } )^{K} =(\frac{T_{1} }{T_{2} } )^{\frac{K}{K-1} }

for air we put K = 1.4

therefore we have \frac{101325 }{4601325 }  = (\frac{10 }{v_{1} } )^{1.4} from which

v₁ = 152.65 m³

We also have \frac{T_{1} }{T_{2} }  =(\frac{p_{1} }{p_{2} } )^{\frac{K-1}{K} }  or \frac{T_{2} }{T_{1} }  =(\frac{p_{2} }{p_{1} } )^{\frac{K-1}{K} }  from which we find the value of T₂ as {T_{2} }  =298.15( \frac{4601325 }{101325 })^{\frac{0.4}{1.4} }  = 886.974 K (peak temperature)

Therefore from pv = RT and R  =cp -cv = 1.005 -0.718 = 0.287 kJ/kg·K

Therefore number of moles = pv/(RT) = (4601325×10)(287×288.15) = 556.394 kg

m = 556.394 kg

Therefore work done at constant pressure = m·cp·(T₂-T₁)  gives

556.394 kg × 1.005 kJ/kg⋅K×(298.15 K-886.974 K ) = -329256.19 kJ or -329.256 MJ

The peak temperature of the isentropic process = 886.974 K

7 0
3 years ago
Water flows in a constant diameter pipe with the following conditions measured:
Burka [1]

Answer:

a) h_L=-3.331ft

b) The flow would be going from section (b) to section (a)

Explanation:

1) Notation

p_a =31.1psi=4478.4\frac{lb}{ft^2}

p_b =27.3psi=3931.2\frac{lb}{ft^2}

For above conversions we use the conversion factor 1psi=144\frac{lb}{ft^2}

z_a =56.7ft

z_a =68.8ft

h_L =? head loss from section

2) Formulas and definitions

For this case we can apply the Bernoulli equation between the sections given (a) and (b). Is important to remember that this equation allows en energy balance since represent the sum of all the energies in a fluid, and this sum need to be constant at any point selected.

The formula is given by:

\frac{p_a}{\gamma}+\frac{V_a^2}{2g}+z_a =\frac{p_b}{\gamma}+\frac{V_b^2}{2g}+z_b +h_L

Since we have a constant section on the piple we have the same area and flow, then the velocities at point (a) and (b) would be the same, and we have just this expression:

\frac{p_a}{\gamma}+z_a =\frac{p_b}{\gamma}+z_b +h_L

3)Part a

And on this case we have all the values in order to replace and solve for h_L

\frac{4478.4\frac{lb}{ft^2}}{62.4\frac{lb}{ft^3}}+56.7ft=\frac{3931.2\frac{lb}{ft^2}}{62.4\frac{lb}{ft^3}}+68.8ft +h_L

h_L=(71.769+56.7-63-68.8)ft=-3.331ft

4)Part b

Analyzing the value obtained for \h_L is a negative value, so on this case this means that the flow would be going from section (b) to section (a).

5 0
3 years ago
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