Forced Convection MCQ Quiz in मल्याळम - Objective Question with Answer for Forced Convection - സൗജന്യ PDF ഡൗൺലോഡ് ചെയ്യുക

Last updated on Mar 11, 2025

നേടുക Forced Convection ഉത്തരങ്ങളും വിശദമായ പരിഹാരങ്ങളുമുള്ള മൾട്ടിപ്പിൾ ചോയ്സ് ചോദ്യങ്ങൾ (MCQ ക്വിസ്). ഇവ സൗജന്യമായി ഡൗൺലോഡ് ചെയ്യുക Forced Convection MCQ ക്വിസ് പിഡിഎഫ്, ബാങ്കിംഗ്, എസ്എസ്‌സി, റെയിൽവേ, യുപിഎസ്‌സി, സ്റ്റേറ്റ് പിഎസ്‌സി തുടങ്ങിയ നിങ്ങളുടെ വരാനിരിക്കുന്ന പരീക്ഷകൾക്കായി തയ്യാറെടുക്കുക

Latest Forced Convection MCQ Objective Questions

Top Forced Convection MCQ Objective Questions

Forced Convection Question 1:

Air at 1 atmospheric pressure and 27 °C blows across a 12 mm diameter sphere at a a small heater inside the sphere maintains the surface temperature at 77 °C. With k = 0.026 W/m (kelvin) and with (Nu) = 31.4, the heat loss by the sphere would be

  1. 1.93 J/s
  2. 1.76 J/s
  3. 1.65 J/s
  4. 1.54 J/s

Answer (Detailed Solution Below)

Option 4 : 1.54 J/s

Forced Convection Question 1 Detailed Solution

Concept:

Heat loss through the convection is given by

Qloss = h × A × (∆T)

Nusselt number \(Nu = \frac{{h{l_c}}}{k}\)

Where l­c is the characteristic length, in case of heater it is equal to the diameter of the sphere

Calculation:

Given, Nu = 31.4, k = 0.026 W/mK, D = 12 mm ⇒ r = 6 × 10-3 m , Surface temperature Ts = 27°C and atmospheric temperature T = 77°C

\(Nu = \frac{{h{l_c}}}{k}\)

⇒ \(h = \frac{{Nu\times{k}}}{l_c}\)

\(h = \frac{{31.4 \times 0.026}}{{0.012}} = 68.03\;W/{m^2}K\;\)

Surface area of sphere A = 4 × π × r2 = 4 × 3.14 × (6 × 10-3)2

Qloss = 68.03 × 4 × 3.14 × (6 × 10-3)2 × (77 – 27) = 1.54 J/s

Forced Convection Question 2:

A methanol is flowing over a plate length of 35 cm. The thermal conductivity of the fluid is  0.02685 W/mK and the average Nusselt number of heat transfer is 716. Calculate the average heat transfer coefficient between methanol and plate?

  1. 39 W/m2K
  2. 48 W/m2K
  3. 55 W/m2K
  4. 73 W/m2K

Answer (Detailed Solution Below)

Option 3 : 55 W/m2K

Forced Convection Question 2 Detailed Solution

Explanation:

Nusselt number

It is the ratio of heat flow rate by convection process to the heat flow rate by the conduction process or it can be defined as the ratio of conductive thermal resistance to the surface convective resistance.

\(Nu = \frac{{{Q_{conv}}}}{{{Q_{cond}}}} =\frac{R_{conduction}}{R_{Convection}}= \frac{{hA{\rm{\Delta }}T}}{{\frac{{kA{\rm{\Delta }}T}}{L}}} = \frac{{hL}}{k}\)

Calculation:

Given:

Nu = 716, k = 0.02685 W/mK, L = 35 cm

\(716 =\frac{h \times 0.35}{0.02685}\)

h = 54.92 W/m2K

Forced Convection Question 3:

The Ratio of average heat transfer coefficient to local heat transfer coefficient, in case of free convection heat transfer through vertical plate is

  1. \(\frac{1}{2}\)
  2. \(\frac{3}{2}\)
  3. \(\frac{3}{4}\)
  4. \(\frac{4}{3}\)
  5. \(\frac{5}{4}\)

Answer (Detailed Solution Below)

Option 4 : \(\frac{4}{3}\)

Forced Convection Question 3 Detailed Solution

Explanation:

The variation of local heat transfer coefficient hx with the distance x for free convection from a vertical heated plate is given as, hx = Cx-1/4

where C is constant.

The average heat transfer coefficient havg is given as,

\({h_{avg}} = \frac{1}{x}\mathop \smallint \limits_0^x {h_x}dx = \frac{1}{x}\mathop \smallint \limits_0^x C{x^{ - 1/4}}dx\)

\({h_{avg}} = \frac{C}{x}\mathop \smallint \limits_0^x {x^{ - 1/4}}dx = \frac{C}{x}\left[ {\frac{{{x^{ - \frac{1}{4} + 1}}}}{{ - \frac{1}{4} + 1}}} \right]_0^x = \frac{4}{3}\frac{C}{x}\;{x^{3/4}} = \frac{4}{3}\;C{x^{ - 1/4}}\;\)

\({h_{avg}} = \frac{4}{3}\;{h_x}\)

\(\frac{h_{avg}}{h_x}=\frac43\)

Forced Convection Question 4:

For the fluid flowing over a flat plate with Prandtl number greater than unity, the thermal boundary layer for laminar forced convection

  1. is thinner than the hydrodynamic boundary layer
  2. has thickness equal to zero 
  3. is of same thickness as hydrodynamic boundary layer
  4. is thicker than the hydrodynamic boundary layer
  5. can't say

Answer (Detailed Solution Below)

Option 1 : is thinner than the hydrodynamic boundary layer

Forced Convection Question 4 Detailed Solution

Explanation:

The relationship between the thermal boundary layer and the hydrodynamic boundary layer is given by Prandtl number 

Prandtl Number: It is defined as the ratio of momentum diffusivity to thermal diffusivity.

\(Pr = \frac{\nu }{\alpha } = \frac{{momentum\;diffusivity}}{{Thermal\;diffusivty}} = \frac{{\frac{\mu }{\rho }}}{{\frac{k}{{{c_p}\rho }}}} = \frac{{\mu {c_p}}}{k}\)

CIL ME HT Subject Test-2 Images-Q11

The relationship between the two is given by the equation

\(\frac{{{\delta }}}{\delta_t } = P_r^{ \frac{1}{3}}\)

δ = the thickness of the hydrodynamic boundary layer; the region of flow where the velocity is less than 99% of the far-field velocity.

δT = the thickness of the thermal boundary layer; the region of flow where the local temperature nearly reaches the value (99%) of the bulk flow temperature

  • If Pr > 1 the momentum or hydrodynamic boundary layer will increase more compared to the thermal boundary layer. 
  • If Pr < 1 the thermal boundary layer will increase more compared to the momentum or hydrodynamic boundary layer.
  • If Pr = 1 The the thermal boundary layer and momentum or hydrodynamic boundary layer will increase at the same rate.

Forced Convection Question 5:

In forced convection, over the flat plate, the average value of Nusselt number is given as:

  1. 0.664 Re0.3 Pr0.5
  2. 0.664 Re0.5 Pr0.3
  3. 0.332 Re0.3 Pr0.5
  4. 0.332 Re0.5 Pr0.3

Answer (Detailed Solution Below)

Option 2 : 0.664 Re0.5 Pr0.3

Forced Convection Question 5 Detailed Solution

Concept:

Nusselt number

It is the ratio of heat flow rate by convection process to the heat flow rate by the conduction process or it can be defined as the ratio of conductive thermal resistance to the surface convective resistance.

\(Nu = \frac{{{Q_{conv}}}}{{{Q_{cond}}}} =\frac{R_{conduction}}{R_{Convection}}= \frac{{hA{\rm{\Delta }}T}}{{\frac{{kA{\rm{\Delta }}T}}{L}}} = \frac{{hL}}{k}\)

The average value of Nusselt number is given as, 0.664 Re0.5 Pr0.3

26 June 1

The Nusselt number is in

Forced Convection

Nu = f (Re, Pr )

 

Free Convection

Nu = f (Gr, Pr )

 

here Nu = Nusselt's Number

Re = Reynold's Number, Pr = Prandtl Number, Gr = Grashoff Number 

Other important dimensionless numbers are:

  • Biot number  → Ratio of internal thermal resistance to boundary layer thermal resistance
  • Grashof number  → Ratio of buoyancy to viscous force
  • Prandtl number  → Ratio of momentum to thermal diffusivities
  • Reynolds number  → Ratio of inertia force to viscous force

Forced Convection Question 6:

Which of the following scenarios best represents an example of forced convection?

  1. Air movement caused by a fan in a computer. 
  2. Natural wind causing a lake's surface water to circulate. 
  3. The warming of a room by a radiator,
  4. The cooling effect around a melting ice cube in still water.

Answer (Detailed Solution Below)

Option 1 : Air movement caused by a fan in a computer. 

Forced Convection Question 6 Detailed Solution

Explanation:

Forced Convection

Definition: Forced convection is a mechanism or type of heat transfer in which fluid motion is generated by an external source (like a pump, fan, suction device, etc.). This differs from natural convection, where the fluid motion is caused by buoyancy forces that result from density variations due to temperature gradients in the fluid.

Working Principle: In forced convection, the external device (such as a fan or pump) actively moves the fluid, enhancing the heat transfer process. The movement of the fluid increases the rate at which heat is transferred from a surface to the fluid or from the fluid to a surface, depending on the temperature difference.

Advantages:

  • Increased heat transfer rate compared to natural convection.
  • Better control over the heat transfer process due to the ability to regulate the speed and direction of the fluid flow.
  • Enhanced cooling or heating efficiency in various applications, such as electronic devices, industrial processes, and HVAC systems.

Disadvantages:

  • Requires an external power source to operate the fan, pump, or other devices.
  • Can be more complex and expensive to implement compared to natural convection systems.

Applications: Forced convection is widely used in many applications, including cooling of electronic components, HVAC systems, automotive cooling systems, and industrial heat exchangers.

Forced Convection Question 7:

The forced convection heat transfer coefficient of a plate  depends on which of the following 

  1. gravity
  2. velocity of fluid
  3. conductivity of fluid
  4. conductivity of plate material

Answer (Detailed Solution Below)

Option :

Forced Convection Question 7 Detailed Solution

Concept:

Laminar forced convection in a flat plate:

\(Nu_x=0.332(Re_x)^{\frac{1}{2}}(Pr)^{\frac{1}{3}}\)

\(\bar{Nu}=0.664(Re)^{\frac{1}{2}}(Pr)^{\frac{1}{3}}\)

∴ Nu ∝ (Re)1/2

∴ h ∝ (U)1/2

As \(Re=\frac{\rho U_{∞}D}{\mu}=\frac{U_∞ D}{\nu}\) and \(Nu=\frac{hD}{k}\)

As the R is the function of velocity and Nis the function of Thermal conductivity, Hence forced convection depends on the Velocity and conductivity of the fluid.

  • Free convection heat transfer coefficient depends on gravity 
  • Heat transfer coefficients depend on the conductivity of the fluid.
  • the conductivity of material has nothing to do with heat transfer coefficients
  • as velocity of fluid increases heat transfer coefficient increases.

Forced Convection Question 8:

In forced convection, over the flat plate, the average value of Nusselt number is given as:

  1. 0.664 Re0.3 Pr0.5
  2. 0.664 Re0.5 Pr0.3
  3. 0.332 Re0.3 Pr0.5
  4. 0.332 Re0.5 Pr0.3
  5. There is no such relation

Answer (Detailed Solution Below)

Option 2 : 0.664 Re0.5 Pr0.3

Forced Convection Question 8 Detailed Solution

Concept:

Nusselt number

It is the ratio of heat flow rate by convection process to the heat flow rate by the conduction process or it can be defined as the ratio of conductive thermal resistance to the surface convective resistance.

\(Nu = \frac{{{Q_{conv}}}}{{{Q_{cond}}}} =\frac{R_{conduction}}{R_{Convection}}= \frac{{hA{\rm{\Delta }}T}}{{\frac{{kA{\rm{\Delta }}T}}{L}}} = \frac{{hL}}{k}\)

The average value of Nusselt number is given as, 0.664 Re0.5 Pr0.3

26 June 1

The Nusselt number is in

Forced Convection

Nu = f (Re, Pr )

 

Free Convection

Nu = f (Gr, Pr )

 

here Nu = Nusselt's Number

Re = Reynold's Number, Pr = Prandtl Number, Gr = Grashoff Number 

Other important dimensionless numbers are:

  • Biot number  → Ratio of internal thermal resistance to boundary layer thermal resistance
  • Grashof number  → Ratio of buoyancy to viscous force
  • Prandtl number  → Ratio of momentum to thermal diffusivities
  • Reynolds number  → Ratio of inertia force to viscous force

Forced Convection Question 9:

The Rayleigh number in free convection scenario is essential to predict the onset of turbulence. Which of the following dimensionless groups is represented by the Rayleigh number?

  1. Product of Grashof and Prandtl numbers
  2.  Product of Reynolds and Prandtl numbers
  3. Ratio of advection to diffusion
  4.  Ratio of conduction to convection

Answer (Detailed Solution Below)

Option 1 : Product of Grashof and Prandtl numbers

Forced Convection Question 9 Detailed Solution

Explanation:

Rayleigh Number:

  • The Rayleigh number is a dimensionless number in fluid dynamics and heat transfer that is important in predicting the onset of convection.
  • It characterizes the flow regime in a fluid and is particularly useful in free convection scenarios.
  • The Rayleigh number combines the effects of thermal expansion, viscosity, thermal diffusivity, and the temperature gradient driving the convection.
  • The Rayleigh number (Ra) is given by the product of the Grashof number (Gr) and the Prandtl number (Pr).

Mathematically, it is expressed as:

Ra = Gr × Pr

Where:

  • Gr is the Grashof number, which represents the ratio of buoyancy to viscous forces in the fluid.
  • Pr is the Prandtl number, which represents the ratio of momentum diffusivity (viscosity) to thermal diffusivity.

Working Principle: In a free convection scenario, fluid motion is induced by the buoyancy forces that result from density variations due to temperature gradients within the fluid. The Rayleigh number helps determine whether the fluid flow will remain laminar or transition to turbulence. A higher Rayleigh number indicates a greater likelihood of turbulent flow.

Importance: The Rayleigh number is critical for engineers and scientists to predict and analyze the thermal behavior of fluids in various applications such as heating and cooling systems, natural convection in the atmosphere, and geological processes.

Forced Convection Question 10:

Given that:

Pr = Prandtl number, Nu = Nussett number

Sh = Shewood number, Re = Reynold number

Sc = Schmidt number & Gr = Grashoff number

The functional relationship for forced convection mass and heat  transfer is/are given as:

  1. Nu = f(Gr, Pr)
  2. Sh = f(Sc, Gr)
  3. Nu = f(Re, Pr)
  4. Sh = f(Re, Sc)

Answer (Detailed Solution Below)

Option :

Forced Convection Question 10 Detailed Solution

Explanation:

Convective mass transfer: The transport of material between a boundary surface and a moving fluid or between two immiscible moving fluids separated by a mobile interface.

The ratio of molecular mass transport resistance to the convective mass transport resistance of the fluid is known as the Sherwood number (Sh).It is analogous to the Nusselt number (Nu) in heat transfer.

\(Sh = \frac{{molecular\;mass\;transport\;resistance}}{{convective\;mass\;tranport\;resistance}} = \frac{{{k_c}L}}{D}\)

Where, L is the characteristic length and kis the convective mass-transfer coefficient.

Concentration-driven natural convection flows are based on the densities of different species in a mixture being different.

In natural convection mass transfer, the analogy between the Nusselt and Sherwood numbers is given as

Sh = (Sc, Gr)

i.e. Sherwood number is a function of Grashof number (Gr) and Schimdt Number (Sc).

The Grashof number in this case should be determined directly from

\(Gr = \frac{{g\left( {\frac{{{\rm{\Delta }}\rho }}{\rho }} \right)L_c^3}}{{{\nu ^2}}}\)

Where ρ is density and Δρ is the change in density Lc is the characteristic length and ν is the kinematic viscosity

In forced convection mass transfer, the analogy between the Nusselt and Sherwood numbers is given as

Sh = (Re, Sc)

In forced convection heat transfer, the analogy between the Nusselt and Reynold numbers is given as, Nu = f(Re, Pr)

Hence Statment 3 and 4 are correct.

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