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andreev551 [17]
2 years ago
11

Consider atmospheric air at 20°C and a velocity of 30 m/s flowing over both surfaces of a 1-m-long flat plate that is maintained

at 130°C. Determine the rate of heat transfer per unit width from the plate for values of the critical Reynolds number corresponding to 105 , 5 × 105, and 106 .
Engineering
1 answer:
serg [7]2 years ago
5 0

Answer:

At 10^5 = 17270W/m

At 5*10^5 = 13127.84 W/m

At 10^6 = 8472.2 W/m

Explanation:

We are given:

T_o = 20°C

Flat plate temp, T_s = 230°C

v = 30m/s

Let's find the mean:

T_f = \frac{20+130}{2}

= 75°C

Using air table at 75°C at 1 atm pressure, we have:

Thermal conductivity, k = 29.66*10^-^3 W/m•K

Prandtl number, Pr = 0.7087

Viscosity, v= 20.82*10^-^6 m^2/s

Calculating Reynolds number, we have:

Re_L = \frac{VL}{v}

Re_L = \frac{30*1}{20.82*10^-^6}

= 1.44*10^6

Since the Reynolds number is higher than the critical Reynolds number, we can say there is a turbulent flow.

Therefore we'll now use the formula:

Nu_L = (0.037Re_L^0^.^8 - A)Pr^0^.^3^3

For Re_x = 10^5

To get A using the formula, we have:

A = 0.037(10^5) - 0.664(10^5)^0^.^5

= 160.024

To find Nu_L

Nu_L =(0.037(1.44*10^6)^0^.^8-160.024)(0.7087)^0^.^3^3

= 2646.78

Connective heat transfer:

h_L = \frac{Nu_L K}{L}

=\frac{(2646.78)(2966*10^-^3)}{1}

=78.50W/m^2•K

Lets calc for heat transfer:

q_1_0_^_5 = 2h_L L(T_s-T_o)

= 2(78.50)(1)(130-20)

= 1720W/m

For Re_x = 5*10^5

A = 0.037Re_x^0^.^8-0.664Re_x^0^.^5

= 0.037(5*10^5)^0^.^8-0.664(5*10^5)^0^.^5

= 871.323

Calculating Nu_L we have:

h_L =\frac{Nu_L K}{L}

= \frac{2011.88*29.66*10^-^3}{1}

= 59.672W/m²•K

For the heat transfer:

q_5_*_1_0_^5 = 2(59.672)(1)(130-20)

= 13127.84W/m

For Re_x = 10^6

A= 0.037(10^6)^0^.^8-0.664(10^6)^0^.^5

= 1670.54

Calculating Nu_L:

Nu_L = (0.037(1.44*10^6)^0^.^8-1670.54)(0.7087)^0^.^3^3

= 1298.51

Calculating the convective heat transfer coefficient:

h_L = \frac{Nu_L*k}{L}

\frac{(1298.51)(29.66*10^-^3)}{1}

=38.51 W/m²•K

To calculte for rate of heat transfer, we have:

q_1_0_^6=2h_LL(T_s-T_o)

=2(38.51)(1)(130-20)

= 8472.2W/m

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The roof of a refrigerated truck compartment consists of a layer of foamed urethane insulation (t2 = 21 mm, ki = 0.026 W/m K) be
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Answer:

Tso = 28.15°C

Explanation:

given data

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t1 = 9 mm

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As when energy on the outer surface at roof of a refrigerated truck that is balance as

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now we compare both equation 1 and 2 and put here value

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3 0
3 years ago
Chlorine is one of the important commodity chemicals for the global economy. Before the advent of large scale
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The composition of gas in the feed, the percentage conversion and the

theoretical yield are combined to give the product stream composition.

Response:

The composition of gas in the product stream are;

  • HCl: 0.4 kmol/h, Cl₂: 1.6 kmol/h, H₂O: 1.6 kmol/h, O₂: 0.5 kmol/h

<h3>How can percentage conversion give the contents of the product stream?</h3>

The amount of oxygen used = 30% exceeding the theoretical amount

Number of moles of hydrochloric acid = 4 kmol/h

Percentage conversion = 80%

Required:

The composition of the gas in the product feed.

Solution;

The given reaction is; 4HCl + O₂ \longrightarrow 2Cl₂ + 2H₂O

Percentage \ conversion = \mathbf{ \dfrac{Moles \ of \ limiting \ reactant \ reacted}{Moles \  of \ limiting \ reactant \ supplied \ in \ the \, feed}}

Which gives;

80 \% = \mathbf{ \dfrac{Moles \ of \ limiting \ reactant \ reacted}{4 \, kmol/h}}

Moles of limiting reactant reacted = 4 kmol/h × 0.80 = 3.6 kmol/h

Which gives;

Number of moles of HCl in the stream = 4 kmol/h - 3.6 kmol/h = 0.4 kmol/h

Number of moles of Cl₂ produced = 2 kmol/h × 0.8 = 1.6 kmol/h

Similarly;

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Number of moles of O₂ in the product stream = 30% × 1 kmol/h + 20% × 1 kmol/h = 0.5 kmol/h

The composition of the production stream is therefore;

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  • <u>H₂O: 1.6 kmol/h</u>
  • <u>O₂: 0.5 kmol/h</u>

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