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hodyreva [135]
2 years ago
3

Asphalt at 120 F, considered to be a Newtonian fluid with a viscosity 80000 times that of water and a specific gravity of 1.09,

flow through a pipe of diameter 2.0 in. If the pressure gradient is 1.6 psi/ft determine the flowrate assuming the pipe is (a) horizontal; (b) vertical with flow up.
Engineering
1 answer:
kari74 [83]2 years ago
4 0

Answer:

a) Flow rate if the pipe is horizontal, Q = 4.69 * 10⁻³ ft³/s

b) Flow rate if the pipe is vertical, Q = 3.30 * 10⁻³ ft³/s

Explanation:

From the BI table, dynamic viscosity of water at 120°F is:

\mu_{H_2O} = 1.164 * 10^{-5} lb.s/ft^2

Pressure gradient, \frac{\delta p}{\delta x} = 1.6 psi/ft

Pipe Diameter, D = 2 in = 2/12 ft = 0.167 ft

Dynamic viscosity of asphalt at 120°F:

\mu = v \mu_{H_2O}\\\mu = 80000 * 1.164 * 10^{-5}\\\mu = 0.9312 lb-s/ft^2

Specific weight of asphalt:

\gamma = SG \gamma_{H_2O}\\\gamma = (1.09)(62.4)\\\gamma = 68.016 lb/ft^3

Flow rate, Q, of the asphalt when the pipe is in horizontal position assuming that the flow is laminar:

Note that if the pipe is horizontal, θ = 0°

Q = \frac{\pi D^4}{128 \mu} [(\frac{\delta p }{\delta x}) - \gamma sin \theta]\\\\Q = \frac{\pi 0.167^4}{128 * 0.9312} [(1.6*144) - 68.016 sin (0)]\\\\Q = 4.69 * 10^{-3} ft^3 / s

b) Flow rate assuming the pipe is vertical:

At vertical pipe position, θ = 90°

Q = \frac{\pi D^4}{128 \mu} [(\frac{\delta p }{\delta x}) - \gamma sin \theta]\\\\Q = \frac{\pi 0.167^4}{128 * 0.9312} [(1.6*144) - 68.016 sin (90)]\\\\Q = 3.30 * 10^{-3} ft^3 / s

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Answer:

The C code is given below with appropriate comments

Explanation:

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{

//checking dollars

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{

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coinVals[2]=userTotal/DIME;

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if(coinVals[1]>1) printf("s");

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//checking dimes

if (coinVals[2]>0)

{

//printing dimes

printf(" %d Dime",coinVals[2]);

if(coinVals[2]>1) printf("s");

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amm1812

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nlexa [21]

Answer:

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velocity = 2.5 m/s.

Step 1: Calculating the mean temperature;

(200 + 15)/2

Mean temperature = 107.5°C = 380.5 K

The properties of air at mean temperature 380.5 K are given as:

v = 24.2689*10⁻⁶m²/s

a = 35.024*10⁻⁶m²/s

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Cp = 1012 J/kg.k

Step 2: Calculating the prantl number using the formula;

Pr = v/a

   = 24.2689*10⁻⁶/ 35.024*10⁻⁶

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Step3: Calculating the reynolds number using the formula;

Re = 4m/πDμ

    = 4 *0.006/π*12*10⁻³ * 221.6 *10⁻⁷

    = 0.024/8.355*10⁻⁷

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Nu = 0.023Re^0.8 *Pr^0.3

Nu = 0.023 * 28725^0.8 * 0.693^0.3

     = 75.955

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Nu = hD/k

h = Nu *k/D

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h   = 204.45 W/m²k

(b)

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v = 14.82 *10⁻⁶m²/s

k = 0.0253 W/m.k

a = 20.873 *10⁻⁶m²/s

Pr(outside) = v/a

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Nu = 0.26Re^0.6 * Pr^0.37 * (Pr(outside)/Pr)^1/4

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h₀ = Nu*k/D

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Calculating the overall heat transfer coefficient using the formula;

1/U =1/h₁ +1/h₀

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1/U = 0.026259

U = 1/0.026259

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T -T₀/T₁-T₀ = e^-[uπDL/Cpm]

T - 15/200-15 = e^-[38.08*π*12*10⁻³*25/1012*0.006]

T - 15/185 = e^-5.911

T -15 = 185 * 0.002709

T = 15+0.50

T = 15.50°C

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