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Past Year Questions: Free And Forced Convection - Mechanical Engineering MCQ


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13 Questions MCQ Test Additional Study Material for Mechanical Engineering - Past Year Questions: Free And Forced Convection

Past Year Questions: Free And Forced Convection for Mechanical Engineering 2024 is part of Additional Study Material for Mechanical Engineering preparation. The Past Year Questions: Free And Forced Convection questions and answers have been prepared according to the Mechanical Engineering exam syllabus.The Past Year Questions: Free And Forced Convection MCQs are made for Mechanical Engineering 2024 Exam. Find important definitions, questions, notes, meanings, examples, exercises, MCQs and online tests for Past Year Questions: Free And Forced Convection below.
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Past Year Questions: Free And Forced Convection - Question 1

Match List-I with List-ll and select the correct answer using the code given below the lists:
List-I
A. Grashof number
B. Schmidt number
C. Weber number
D. Fourier number

List-II
1. Mass diffusion
2. Transient heat conduction
3. Free convection
4. Forced convection
5. Surface tension
6. Radiation

[1996]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 1
  1. Grashof Number (A): The Grashof number is used in fluid dynamics to describe free convection. It relates the buoyancy forces to the viscous forces within a fluid. In simpler terms, it helps in analyzing the flow of fluid when there are temperature differences causing movement.
    Matches with: 3 (Free convection)

  2. Schmidt Number (B): The Schmidt number is a dimensionless number used in fluid dynamics that describes the ratio of momentum diffusivity (viscosity) to mass diffusivity. It is important in mass transfer operations.
    Matches with: 1 (Mass diffusion)

  3. Weber Number (C): The Weber number is a dimensionless number in fluid mechanics that is used to analyze the relative importance of the fluid's inertia compared to its surface tension. It is commonly used in the study of droplets, bubbles, and liquid surfaces. 
    Matches with: 5 (Surface tension)

  4. Fourier Number (D): The Fourier number is a dimensionless number used in heat conduction problems. It represents the ratio of heat conduction rate to the rate of heat storage, making it crucial in transient heat conduction analysis.
    Matches with: 2 (Transient heat conduction)

The correct matching code is (b) 3, 1, 5, 2,

Past Year Questions: Free And Forced Convection - Question 2

The ratio of momentum diffusivity (v) to thermal diffusivity (α), is called

[2015]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 2

The ratio of momentum diffusivity (ν) to thermal diffusivity (α) is called the Prandtl number.

  • Prandtl Number (Pr): This is a dimensionless number that represents the ratio of momentum diffusivity (kinematic viscosity, ν) to thermal diffusivity (α). It is used to relate the relative thickness of the momentum boundary layer to the thermal boundary layer in fluid flow.

  • Nusselt Number (Nu): It represents the ratio of convective to conductive heat transfer across a boundary.

  • Biot Number (Bi): It relates the internal resistance to heat conduction within a body to the external convective heat transfer.

  • Lewis Number (Le): This is the ratio of thermal diffusivity to mass diffusivity.

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Past Year Questions: Free And Forced Convection - Question 3

Grashof number signifies the ratio of

[2016]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 3

The Grashof number signifies the ratio of buoyancy force to viscous force in a fluid.

Grashof Number (Gr): It is a dimensionless number that compares the relative significance of buoyancy forces to viscous forces in fluid flow. It is important in the study of natural convection, where fluid motion is caused by temperature-induced density differences (buoyancy).

A high Grashof number indicates that buoyancy forces dominate, leading to strong natural convection.

Past Year Questions: Free And Forced Convection - Question 4

In pool boiling the highest HTC occurs in

[1990]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 4

The highest Heat Transfer Coefficient (HTC) in pool boiling occurs in the nucleate boiling zone.

  • Nucleate Boiling Zone: This is the regime where small bubbles form on the heated surface and then detach into the liquid. The heat transfer is extremely efficient in this zone because the bubbles enhance the mixing of the liquid, thus increasing the heat transfer rate significantly.

  • Subcooled Boiling Zone: This occurs when the bulk liquid is at a temperature below its boiling point, so boiling happens only near the surface. The HTC here is lower compared to nucleate boiling.

  • Partial Film Boiling Zone: In this zone, part of the surface is covered by a vapor film, which reduces heat transfer because vapor has lower thermal conductivity than liquid.

  • Film Boiling Zone: In this zone, the surface is completely covered by a stable vapor film, which significantly lowers the heat transfer coefficient due to the insulating effect of the vapor.

Past Year Questions: Free And Forced Convection - Question 5

Heat transfer coefficients for free convection in gases, forced convection in gases and vapours, and for boiling water lie, respectively, in the range of

[1998]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 5

The heat transfer coefficients for free convection in gases, forced convection in gases and vapours, and for boiling water lie, respectively, in the range of:

  • Free convection in gases: 5-15 W/m²K
  • Forced convection in gases and vapours: 20-200 W/m²K
  • Boiling water: 3000-50000 W/m²K

Explanation:

  • Free convection in gases: Heat transfer by natural or free convection in gases has a relatively low heat transfer coefficient because the fluid movement is primarily due to buoyancy forces.

  • Forced convection in gases and vapours: In forced convection, the movement of gases is induced by external forces (e.g., a fan or pump), leading to a higher heat transfer coefficient compared to free convection.

  • Boiling water: Boiling water has a significantly higher heat transfer coefficient due to the phase change from liquid to vapor, which enhances heat transfer.

Correct Answer:

A: 5-15; 20-200 and 3000-50000 W/m²K

Past Year Questions: Free And Forced Convection - Question 6

For the three-dimensional object shown in the figure below, five faces are insulated. The sixth face (PQRS), which is not insulated, interacts thermally with the ambient, with a convective heat transfer coefficient of 10W/m2K. The ambient temperature is 30°C. Heat is uniformly generated inside the object at the rate of 100 W/m3. Assuming the face PQRS to be at uniform temperature, its steady state temperature is

[2000]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 6

Given data;


Volume,
V = 2×1×2=4 m3
Heat generated,
Q = qG × V = 100 × 4 = 400 W
Convection heat transfer from face PQRS,

Past Year Questions: Free And Forced Convection - Question 7

Water (specifie heat, c = 4.18 kJ/kgK) enters a pipe at a rate 0.01 kg/s and a temperature of 20°C. The pipe, of diameter 50 mm and length 3 m, is subjected to a wall heat flux q"w in W/m2.

If q"w = 2500x, where x is in m and in the direction of flow (x = 0 at the inlet), the bulk means temperature of the water leaving the pipe in °C is

[2013]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 7

At the inlet of pipe
x = O
q "wi = 2500 x 0 = 0
At the exit of pipe,
x = 1

Average heat transfer,

Net heat transfer

By solving above equation, we get
To = 62° C

Past Year Questions: Free And Forced Convection - Question 8

Water (specifie heat, c = 4.18 kJ/kgK) enters a pipe at a rate 0.01 kg/s and a temperature of 20°C. The pipe, of diameter 50 mm and length 3 m, is subjected to a wall heat flux q"w in W/m2.

If q"w = 5000 and the convection heat transfer coefficient at the pipe outlet is 1000 W/m2K, the temperature in °C at the inner surface of the pipe at the outlet is

[2013]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 8


Heat transfer through pipe wall,

Q = mCP(T0–Ti), amount of heat gained by the water
2355 = 0.01 × 4180 (T0 – 20)
T0 = 76.33°C

5000 = 1000 (Tso – 76.33)
Tso = 81°C

Past Year Questions: Free And Forced Convection - Question 9

For laminar forced convection over a flat plate, if the free stream velocity increases by a factor of 2, the average heat transfer coefficient​

[2014]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 9

Forlaminar flow, Nu = 0.664 (Re)0.5 (Pr)0.33

So when free stream velocity increases by a factor of 2, then the average heat transfer coefficient rises by a factor of √2.

Past Year Questions: Free And Forced Convection - Question 10

The properties of mercury at 300 K are: Density = 13529 kg/m3, cp = 0.1393 kJ/kgK, dynamic viscosity = 0.1523 × 10–2 Ns/m2 and thermal conductivity = 8.540 W/mK. The Prandtl number of the mercury at 300 K is

[2002]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 10

Prandtl number = 

Past Year Questions: Free And Forced Convection - Question 11

In the laminar flow of air (Pr = 0.7) over a heated plate, if δ and δT denote, respectively, the hydrodynamic and thermal boundary layer thicknesses, then

[2015]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 11

When

Past Year Questions: Free And Forced Convection - Question 12

For a hydrodynamically and thermally fully developed laminar flow through a circular pipe of constant cross-section. The Nusselt number at constant wall heat flux (Nuq) and that at constant wall temperature (NuT) are related as

[2019]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 12

(Nu)q for constant wall heat flux and (Nu)T at constant wall temperature for a hydrodynamically and thermally fully developed laminar flow through a circular pipe of constant cross-section is 4.36 and 3.66 respectively.

Past Year Questions: Free And Forced Convection - Question 13

The wall of a constant diameter pipe of length 1 m is heated uniformly with flux q” by wrapping a heater coil around it. The flow at the inlet to the pipe is hydrodynamically fully developed. The fluid is incompressible and the flow is assumed to be laminar and steady all through the pipe.
The bulk temperature of the fluid is equal to 0°C at the in let and 50°C at the exit. The wal l temperatures are measured at three locations, P, Q an d R as shown in the figure. The flow thermally develops after some distance from the inlet. The following measurements are made :

Among the locations P, Q and R, the flow is thermally at :

[2019]

Detailed Solution for Past Year Questions: Free And Forced Convection - Question 13

In case of uniform heat flux, bulk mean temperature varies linearly. The difference between bulk mean temperature and wall temperature is constant in thermally developed region so bulk tempeature,

Here,

So, Q and R in thermally developed region.

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