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GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering PDF Download

Q1: Consider a hydrodynamically and thermally fully-developed, steady fluid flow of 1 kg/s in a uniformly heated pipe with diameter of 0.1 m and length of 40 m. A constant heat flux of magnitude 15000 W/m2 is imposed on the outer surface of the pipe. The bulk-mean temperature of the fluid at the entrance to the pipe is 200°C. The Reynolds number (Re ) of the flow is 85000, and the Prandtl number ( Pr ) of the fluid is 5. The thermal conductivity and the specific heat of the fluid are 0.08 WGATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering −1 GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering −1 and 2600 J GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering g−1GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering− 1, respectively. The correlation Nu = 0.023 Re 0.8 Pr 0.4 is applicable, where the Nusselt Number (Nu) is defined on the basis of the pipe diameter. The pipe surface temperature at the exit is ________ °C (round off to the nearest integer). [GATE ME 2022, SET-2]
Ans:
(317 to 324)
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical EngineeringGATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering= 1kg/ sec
Re = 85000
Pr = 5
K = 0.08W/mK
C = 2600j/kgK
Nu = 0.023 Re 0.8 Pr 0.4
Nu = hD/k
Ts = ?
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering
1500 x π x 0.1 x 40 = 1 x 2600 x (T0 - 200)
To = 275.5°C
Newtons law of cooling
q = h (Ts - Tm)
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical EngineeringGATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering


Q2: Which of the following non-dimensional terms is an estimate of Nusselt number?  [GATE ME 2022 SET-2]
(a) Ratio of internal thermal resistance of a solid to the boundary layer thermal resistance
(b) Ratio of the rate at which internal energy is advected to the rate of conduction heat transfer
(c) Non-dimensional temperature gradient
(d) Non-dimensional velocity gradient multiplied by Prandtl number
Ans:
(c) 
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineeringθ* = (Ts - T) / (T- T)
y* = y / L
dy */dy = 1/L
dθ*/dy = -dT/dy
Ts and T are constant
At boundary
q conduction = q convection
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering
Applying chain rule

GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering

dθ*/dy* = hL / Kf = Nusselt Number
Nu = dθ*/dy*
Nu represents non dimensional temperature gradient.


Q3: In forced convective heat transfer, Stanton number (St), Nusselt number (Nu), Reynolds number (Re) and Prandtl number (Pr) are related as  [GATE ME 2021, SET-2]
(a) St = Nu/Re Pr
(b) St = Nu Re/ Pr
(c) St =Nu Pr Re
(d) Nu Re/Pr
Ans: 
(a) 
St = Nu/Re Pr


Q4: A hot steel spherical ball is suddenly dipped into a low temperature oil bath.
Which of the following dimensionless parameters are required to determine instantaneous center temperature of the ball using a Heisler chart?  [GATE ME 2021 SET-1]
(a) Biot number and Fourier number
(b) Reynolds number and Prandtl number
(c) Biot number and Froude number
(d) Nusselt number and Grashoff number
Ans: 
(a)
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering


Q5: Water flows through a tube of 3 cm internal diameter and length 20 m, The outside surface of the tube is heated electrically so that it is subjected to uniform heat flux circumferentially and axially. The mean inlet and exit temperatures of the water are 10 °C and 70°C, respectively. The mass flow rate of the water is 720 kg/h. Disregard the thermal resistance of the tube wall. The internal heat transfer coefficient is 1697 W/m2. Take specific heat Cp of water as 4.179 kJ/kg. K. The inner surface temperature at the exit section of the tube is __________ °C(round off to one decimal place). [GATE ME 2020, SET-2]
Ans:
(85.1 to 86.1)
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering

h=1697W/m 2
From energy balance equation, 
Heat flux × Area of HT
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical EngineeringApplying Newton's law of cooling at exit
q" = h x (Ttube at exit - T water at exit) W/m2
266604.34 = 1697 x (Ttube at exit - 70) W/m2
(Ttube at exit = 85.67°C


Q6: A small metal bead (radius 0.5 mm), initially at 100°C , when placed in a stream of fluid at 20°C, attains a temperature of 28°C in 4.35 seconds. The density and specific heat of the metal are 8500 k g/m3 and 400 J/kgK, respectively. If the bead is considered as lumped system, the convective heat transfer coefficient (in W/m2K ) between the metal bead and the fluid stream is [GATE ME 2020, SET-1]
(a) 283.3
(b) 299.9
(c) 149.9
(d) 449.7
Ans:
(b)
r = 0.5mm; cp = 400j/kg; p = 8500kg/m3; t = 4.35sec
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering
⇒ h = 299.95W/m2K

Question for GATE Past Year Questions: Free & Forced Convection
Try yourself: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

GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering

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Question for GATE Past Year Questions: Free & Forced Convection
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Question for GATE Past Year Questions: Free & Forced Convection
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Question for GATE Past Year Questions: Free & Forced Convection
Try yourself:Heat transfer coefficients for free convection in gases, forced convection in gases and vapours, and for boiling water lie, respectively, in the range of

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Question for GATE Past Year Questions: Free & Forced Convection
Try yourself: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
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering

[2000]

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Question for GATE Past Year Questions: Free & Forced Convection
Try yourself: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]

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Question for GATE Past Year Questions: Free & Forced Convection
Try yourself: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]

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Question for GATE Past Year Questions: Free & Forced Convection
Try yourself:For laminar forced convection over a flat plate, if the free stream velocity increases by a factor of 2, the average heat transfer coefficient​

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Question for GATE Past Year Questions: Free & Forced Convection
Try yourself: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]

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Try yourself: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

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Question for GATE Past Year Questions: Free & Forced Convection
Try yourself: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]

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Question for GATE Past Year Questions: Free & Forced Convection
Try yourself: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 :
GATE Past Year Questions: Free & Forced Convection | Heat Transfer - Mechanical Engineering
Among the locations P, Q and R, the flow is thermally at :

[2019]

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FAQs on GATE Past Year Questions: Free & Forced Convection - Heat Transfer - Mechanical Engineering

1. What is the difference between free convection and forced convection in chemical engineering?
Ans. Free convection occurs when fluid motion is caused by buoyancy forces due to density differences arising from temperature variations within the fluid. In contrast, forced convection involves external forces, such as pumps or fans, to induce fluid movement. This distinction is crucial for designing equipment like heat exchangers and reactors.
2. How do you calculate the heat transfer coefficient for forced convection?
Ans. The heat transfer coefficient for forced convection can be calculated using empirical correlations such as the Dittus-Boelter equation, which is given by \( Nu = 0.023 Re^{0.8} Pr^{n} \), where \( Nu \) is the Nusselt number, \( Re \) is the Reynolds number, \( Pr \) is the Prandtl number, and \( n \) is 0.3 for heating and 0.3 for cooling. The heat transfer coefficient, \( h \), can then be derived from \( Nu \) using \( h = \frac{Nu \cdot k}{L} \), where \( k \) is the thermal conductivity and \( L \) is a characteristic length.
3. What role does viscosity play in convection processes in chemical engineering?
Ans. Viscosity affects the momentum transfer in fluids, influencing the flow regime and the heat transfer rate during convection. In free convection, higher viscosity can reduce the buoyant force's effectiveness, leading to lower heat transfer rates. In forced convection, increased viscosity leads to higher pressure drops and can affect the pump sizing and energy consumption.
4. What are some common applications of forced convection in chemical engineering?
Ans. Forced convection is commonly used in applications such as cooling systems for chemical reactors, heat exchangers in industrial processes, air conditioning systems, and the drying of materials. These applications benefit from enhanced heat transfer rates due to the controlled fluid movement.
5. How can one enhance heat transfer in forced convection systems?
Ans. Heat transfer in forced convection systems can be enhanced by using fins, increasing the flow velocity, optimizing the geometry of the heat exchange surfaces, utilizing turbulence promoters, and selecting fluids with higher thermal conductivity. Additionally, using multiple flow paths or counterflow arrangements can significantly improve heat transfer efficiency.
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