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Test: One-Dimensional Steady-State Conduction - 3 - Mechanical Engineering MCQ


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30 Questions MCQ Test Heat Transfer - Test: One-Dimensional Steady-State Conduction - 3

Test: One-Dimensional Steady-State Conduction - 3 for Mechanical Engineering 2024 is part of Heat Transfer preparation. The Test: One-Dimensional Steady-State Conduction - 3 questions and answers have been prepared according to the Mechanical Engineering exam syllabus.The Test: One-Dimensional Steady-State Conduction - 3 MCQs are made for Mechanical Engineering 2024 Exam. Find important definitions, questions, notes, meanings, examples, exercises, MCQs and online tests for Test: One-Dimensional Steady-State Conduction - 3 below.
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Test: One-Dimensional Steady-State Conduction - 3 - Question 1

The critical thickness of insulation for sphere is given by

Test: One-Dimensional Steady-State Conduction - 3 - Question 2

As the thickness of insulation around a heated cable gradually increases from zero, heat transfer from the conductor

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 2

As the thickness of insulation around a heated cable gradually increases form zero upto critical radius, heat transfer increases and when the radius of insulation exceed form the critical radius of insulation heat transfer decreases.

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Test: One-Dimensional Steady-State Conduction - 3 - Question 3

Upto critical radius of insulation

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 3


Hence upto critical thickness heat transfer increases and after critical thickness there will be reduction in heat transfer, when more insulation is provided.

Test: One-Dimensional Steady-State Conduction - 3 - Question 4

A critical radius of insulated pipe leads to

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 4

From the above figure one can analyse that at critical radius heat transfer is maximum.

Test: One-Dimensional Steady-State Conduction - 3 - Question 5

If the radius of any current carrying wire is less than the critical radius, then the addition of electrical insulation will enable the wire to carry a higher current because

Test: One-Dimensional Steady-State Conduction - 3 - Question 6

In case of hollow cylinder, as the ratio of outer radius to inner radius increases, the heat transfer

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 6

In case of hollow cylinder

as  increases Q decreases

Test: One-Dimensional Steady-State Conduction - 3 - Question 7

For a given heat flow and for the same thickness the temperature drop across the material will be maximum for

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 7

From the Fourier’s law of .conduction

Test: One-Dimensional Steady-State Conduction - 3 - Question 8

At steady state, the temperature variation in a plane wail, made of two different solids I and II is shown below figure.

Then the thermal conductivity of material I

Test: One-Dimensional Steady-State Conduction - 3 - Question 9

What is the equivalent thermal conductivity of a composite wall made of two layers of different material of thermal conductivity k1 and k2 and having thickness δ1 and δ2 respectively

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 9


Req = R+ R2


Test: One-Dimensional Steady-State Conduction - 3 - Question 10

An electronic device in the form of a wire is found to dissipate maximum heat when its outer most diameter = 32 mm. Keeping all the parameter same, it is proposed to use the same device in spherical form. The ideal diameter would be

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 10


Test: One-Dimensional Steady-State Conduction - 3 - Question 11

An aluminium sheet of 10 mm thickness is brought into contact with an iron sheet of 20 mm thickness. The outer surface of aluminium is kept at 100°C. Where as the outer surface of iron is maintained at 0°C. if the ratio of thermal conductivity of aluminium and iron is 3 : 1, then the interface temperature in °C is

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 11




Test: One-Dimensional Steady-State Conduction - 3 - Question 12

A metal wall has an area of 5 m2, thickness 10 cm and a thermal conductivity 200 W/mK, what is the value of thermal resistance of the wall in K/W?

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 12

Thermal resistence = L/kA

Test: One-Dimensional Steady-State Conduction - 3 - Question 13

A steel plate of thermal conductivity 50 W/m-K and thickness 10 cm passes a heat flux by conduction of 25 kW/m2. If the temperature of the hot surface of the plate is 100°C then what is the temperature of the cooler side of the plate?

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 13


Test: One-Dimensional Steady-State Conduction - 3 - Question 14

A composite wall of a furnace has 3 layers of equal thickness having thermal conductivities the ratio of 1 : 2 : 4. What will be the temperature drop ratio across the three respective layer

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 14

From the fourier law of heat conduction

Test: One-Dimensional Steady-State Conduction - 3 - Question 15

A long Glass cylinder of inner diameter = 0.03 m and outer diameter = 0.05 m carries hot fluid inside. If the thermal conductivity of glass = 1.05 W/mK the thermal resistance (K/W) per unit length of the cylinder is

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 15

Thermal resistance

Test: One-Dimensional Steady-State Conduction - 3 - Question 16

A stainless steel tube (ks = 19 W/mK) of 2 cm ID and 5 cm OD in insulated with 3 cm thick asbestos (ka = 0.2 W/mK). If the temperature difference between the inner most and outer most surface is 600°C the heat transfer rate per unit length is

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 16


Given
r1 = 1 cm
r2 = 2.5 cm
r3 = 5.5 cm
Equivalent thermal resistance

Test: One-Dimensional Steady-State Conduction - 3 - Question 17

Heat flows through a composite slab, as shown below. The depth of the slab is 1 m. The k values are in W/mK. The overall thermal resistance in K/W is

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 17

Resistance diagram

Now,

Equivalent resistance between B and C

total resistance = R1 + Re
= 25 + 3.6 = 28.6 K/W

Test: One-Dimensional Steady-State Conduction - 3 - Question 18

Two plates of equal thickness (t) and cross- sectional area, are joined together to form a composite as shown in the figure. If the thermal conductivities of the plates are k and 2k then, the effective thermal conductivity of the composite is

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 18



 

Test: One-Dimensional Steady-State Conduction - 3 - Question 19

The heat flux (from outside to inside) across an insulating wail with thermal conductivity K = 0.04 W/mK and thickness 0.16 m is 10 W/m2. The temperature of the inside wall is -5°C. The outside wall temperature is

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 19

k = 0.04 W/mK
L = 0.16m
Q = 10 W/m2
T1 = - 5°C = T2
From the Fouriers law

Test: One-Dimensional Steady-State Conduction - 3 - Question 20

The composite wall of an oven consists of three materials A, B and C. Under steady state operating conditions, the outer surface temperature Tso is 20°C, the inner surface temperature Tsi is 600°C and the oven air temperature T is 800 °C, For the following data: thermal conductivities kA = 20 W/(mK) and kC = 50 W/(mK), thickness LA = 0.3 m, L= 0.15 m and L= 0.15 m, inner-wall heat transfer coefficient h = 25 W/(m2K) the thermal conductivity kB (W/(mK) of the material B, is calculated as

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 20

Heat lost by convection = Heat conducted by conduction


Test: One-Dimensional Steady-State Conduction - 3 - Question 21

For a plane wall of thickness l with uniformly distributed heat generation qg per unit volume, the temperature t0 at the mid-plahe is given by

Test: One-Dimensional Steady-State Conduction - 3 - Question 22

A slab of thickness L with one side (x = 0) insulated and other side (x = L) maintained at a constant temperature T0 is shown below:

A uniformly distributed internal heat source produces heat in the slab at the rate of W/m3. Assume the heat conduction to be steady state and 1 - D along the x-direction, the maximum temperature in the slab occurs at x equal to

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 22

For maximum temp, in the wall

Test: One-Dimensional Steady-State Conduction - 3 - Question 23

In a composite slab, the temperature at the interface (Tinter) between two materials is equal to the average of the temperature at the two ends. Assuming steady one dimensional heat conduction, which of the following statements is true about the respective thermal conductivities?

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 23

Here Q will be same


Test: One-Dimensional Steady-State Conduction - 3 - Question 24

A metallic rod of uniform diameter and length L connects two heat sources each at 500°C. The atmospheric temperature is 30°C. The temperature gradient dT/dL at the centre of the bar will be

Test: One-Dimensional Steady-State Conduction - 3 - Question 25

A hollow sphere has inner and outer surface areas of 2 m2 and 8 m2 respectively. For a given temperature difference across the surfaces, the heat flow is to be calculated considering the material of the sphere as a plane wall of the same thickness. What is the equivalent mean area normal to the direction of heat flow?

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 25

For sphere

Test: One-Dimensional Steady-State Conduction - 3 - Question 26

The temperature gradient through the two layer composite wall consisting of two metals A and B is as shown in figure. It can be concluded that

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 26

According to the figure, the temperature at the interface of metal A and metal B is observed to be 300 degrees centigrade. This temperature is the highest recorded during the entire process. Additionally, the flow of heat is observed to be from a higher temperature to a lower temperature. Therefore, it can be deduced that the heat must have been generated at the interface of metal A and metal B.

Therefore option C is correct.

Test: One-Dimensional Steady-State Conduction - 3 - Question 27

Heat is being transferred convectively flow through a cylindrical nuclear reactor fuel rod of 50 mm diameter to water at 75°C. Under steady state condition, the rate of heat generation within the fuel element is 5 x107W/m3 and the. convection heat transfer coefficient is 1 kW/m2 K. The outer surface temperature of the fuel element would be

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 27

Test: One-Dimensional Steady-State Conduction - 3 - Question 28

A stagnant liquid film of 0.4 mm thickness is held between two parallel plates. The top plate is maintained at 40°C and the bottom plate is maintained at 30°C. if the thermal conductivity of the liquid is 0.14 W/(m K), then the steady state heat flux (in W/m2) assuming one dimensional heat transfer is

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 28


From Fourier’s law of heat conduction

Test: One-Dimensional Steady-State Conduction - 3 - Question 29

A flat plate has thickness 5 cm, thermal conductivity 1 W/(mK) convective heat transfer coefficients on its two flat faces of 10 W/(m2K) and 20W/(m2K). The overall heat transfer coefficient for such a flat plate is

Detailed Solution for Test: One-Dimensional Steady-State Conduction - 3 - Question 29


Test: One-Dimensional Steady-State Conduction - 3 - Question 30

Steady state one dimensional heat flow by conduction as given by Fourier's low does not assume that

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