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UCH402

This document outlines the end semester examination for the Heat Transfer course at Thapar Institute of Engineering and Technology, detailing the exam structure, questions, and marks distribution. Students are required to attempt five questions covering various topics such as heat exchangers, evaporators, condensers, and thermal radiation. The exam is scheduled for May 23, 2024, with a total of 50 marks available.

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0% found this document useful (0 votes)
9 views3 pages

UCH402

This document outlines the end semester examination for the Heat Transfer course at Thapar Institute of Engineering and Technology, detailing the exam structure, questions, and marks distribution. Students are required to attempt five questions covering various topics such as heat exchangers, evaporators, condensers, and thermal radiation. The exam is scheduled for May 23, 2024, with a total of 50 marks available.

Uploaded by

siddhjain94
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
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Roll Number: __________________________

Thapar Institute of Engineering and Technology Patiala


Department of Chemical Engineering
B. E. (Second Year): Semester-IV Course Code: UCH402
(Chemical Engineering) Course Name: Heat Transfer
End Semester Exam; May 23, 2024 Thursday, 9:00 AM
Time: 3 Hours, M. Marks: 50 Name of Faculty: Dr. J. P. Kushwaha

Note: Attempt any five questions.


Assume missing data, if any, suitably.

Q. No. Question Marks CO BL


Q1 (a) Hot oil (Cp = 2200 J/kg · °C) is to be cooled by water (Cp = 4180 J/kg · °C) 6 CO2 L3
in a 2-shell-pass and 12-tube-pass heat exchanger. The tubes are thin-walled
and are made of copper with a diameter of 1.8 cm. The length of each tube
pass in the heat exchanger is 3 m, and the overall heat transfer coefficient is
340 W/m2 · °C. Water flows through the tubes at a total rate of 0.1 kg/s, and
the oil through the shell at a rate of 0.2 kg/s. The water and the oil enter at
temperatures 18°C and 160°C, respectively. Determine the rate of heat
transfer in the heat exchanger and the outlet temperatures of the water and
the oil. Consider the effectiveness of this exchanger as Ꜫ = 0.61
Q1 (b) What is the role of the baffles in a shell-and-tube heat exchanger? How does 4 CO2 L2
the presence of baffles affect the heat transfer and the pumping power
requirements? Explain.
Q2 (a) Draw the boiling curve and identify the different boiling regimes. Also, 5 CO1 L2
explain the characteristics of each regime.
Q2 (b) A single effect evaporator is used to concentrate cane sugar juice from 10% 5 CO3 L4
to 40% concentration at a rate of 2000 kg/h. Inlet temp. of feed is 30 C and
pressure 0.33 kg /cm2 is maintained in vapour space. Liquid is boiling at
75C at this pressure. Saturated steam (latent heat = 529.5 kcal/kg) is
supplied at 115 C. Calculate the steam required and number of tubes used
(OD= 0.025 m, ID= 0.021 m), if height of tubes is 1.6 m.
Given: Specific heat of feed = 0.946 kcal/kg C; Latent heat of steam (at
0.33 kg/cm2) =556.5 kcal/kg); Overall heat transfer coefficient = 2150
kcal/h m2 C.
Q3 (a) Explain the difference in working of Falling-film-type evaporator and 5 CO3 L1
agitated-film-type evaporator.
Q3 (b) Steam in the condenser of a steam power plant is to be condensed at a 5 CO3 L3
temperature of 50 °C (latent heat = 2305 kJ/kg) with cooling water (Cp =
4180 J/kg · °C) from a nearby lake, which enters the tubes of the condenser
at 18 °C and leaves at 27 °C. The surface area of the tubes is 58 m2, and the
overall heat transfer coefficient is 2400 W/m2 · °C. Determine the mass flow
rate of the cooling water needed and the rate of condensation of the steam in
the condenser considering counter flow arrangement.

PTO
Q4 (a) Water (Cp = 4180 J/kg · °C) enters the 2.5-cm internal-diameter tube of a 5 CO2 L3
double-pipe counter-flow heat exchanger at 17 °C at a rate of 3 kg/s. It is
heated by steam condensing at 120 °C (hfg = 2203 kJ/kg) in the shell. If the
overall heat transfer coefficient of the heat exchanger is 1500 W/m2 · °C,
determine the length of the tube required in order to heat the water to 80 °C.
Q4 (b) With neat sketch, compare the working of low level and high level counter 5 CO3 L2
flow jet condensers.
Q5 (a) A copper wire of 5.2 mm diameter is insulated with PVC (polyvinyl chloride) 4 CO1 L3
of thermal conductivity Kc = 0.43 W/m ⁰C. The wire carries current and its
temperature is 60 ⁰C. The film coefficient at the outer surface of the
insulation is 11.35 W/m2 ⁰C. Calculate the critical insulation thickness.
Q5 (b) A shell-and-tube heat exchanger (counterflow arrangement) with 2-shell 6 CO2 L3
passes and 8-tube passes is used to heat ethyl alcohol (Cp = 2670 J/kg · °C)
in the tubes from 25 °C to 70 °C at a rate of 2.1 kg/s. The heating is to be
done by water (Cp = 4190 J/kg · °C) that enters the shell side at 95 °C and
leaves at 45 °C. If the overall heat transfer coefficient is 950 W/m2 · °C,
determine the heat transfer surface area of the heat exchanger.

Fig. 1. Correction factor for Two-shell passes and 4, 8, 12, etc. tube passes

Q6 (a) How is the intensity of emitted radiation defined? For a diffused surface, how 5 CO1 L2
is the emissive power related to the intensity of emitted radiation?
Q6 (b) A 20 cm diameter spherical ball (assume black body) is at 800 K. Determine 5 CO1 L3
(a) the total blackbody emissive power, (b) the total amount of radiation
emitted by the ball in 5 min, and (c) the spectral blackbody emissive power
at a wavelength of 3 μm.
Stefan-Boltzmann constant (σ) = 5.67 x10-8 W/m2K4
Monochromatic emissive power is given by the following relation:
Marks Distribution

Bloom's level-wise marks Course outcome-wise marks distribution


distribution 36
8.33 35
8.33 35

34 33.33
31.67
51.66 33

32 31.67

31

L1 8.33 L2 31.67 30
L3 51.66 L4 8.33 CO1 CO2 CO3

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