IRJET-Experimental Study on Helical Tube Heat Exchanger by Varying Cross Section using Nano Particles

International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 05 Issue: 06 | June-2018 www.irjet.net p-ISSN: 2395-0072
© 2018, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 2746
Experimental study on helical tube heat exchanger by varying cross
section using nano Particles
Mr. Robin R. Gupta1, Mr. Sumit. S. Kalmegh2, Mr. Parag S. Warghade3, Mr. Kishor K. Padghan4
1Mr. Robin R. Gupta, M.E(Thermal Engineering) Scholar, DRGIT&R, Amravati, Maharashtra, India.
2,3,4 Assistant Professor, Mechanical Engg. Dept. DRGIT&R, Amravati, Maharashtra, India
---------------------------------------------------------------------***---------------------------------------------------------------------
Abstract – In large-scale industrial companies for several
decades the waste heat recovery has been the topic of
concern. This recovery not only makes an operation more
environment friendly, but it also helps to cut costs as well as
reduction in size of heat recovery device. In addition to this,
it can reduce the amount of resources needed to power a
facility. Many industries have implemented different
methods of waste heat recovery. One popular choice is using
a heat exchanger. This paper presents the study of two types
of heat exchangers: straight and helical coil tube with the
addition of nano particle (Tio2 & Sio2) in the working fluid.
The helical coil heat exchanger has been experimented and
analyzed on the basic of log-mean temperature difference
(LMTD), heat transfer coefficient and Reynolds number.
Based on the results, it is found that helical coil heat
exchangers are efficient with the addition of nano particle in
the working fluid and its overall heat transfer coefficient
increases with mass flow rate.
Key Words: Helical coil heat exchanger, heat transfer
coefficient, LMTD and Reynolds number.
1. INTRODUCTION
The heat is a form of energy that transfers from the hot
object to the cold object, and it transferred through the
conduction, the convection and the radiation. The heat
energy has many usages in the industry as making metals,
chemicals, refining oil and processing the food. The
shortage of heat energy leads to conserve or to make best
use of it. In several industrial processes there is waste of
energy or a heat stream that being exhausted in
atmosphere. The heat exchangers plays important role to
recover this heat and place it to use by heating a different
stream within the process. This practice saves a lot of
money in industry, as the heat supplied to other streams
from the heat exchangers would otherwise come from an
external source that is more expensive and more harmful
to the environment. The purpose of constructing a heat
exchanger is to get an efficient technique of heat transfer
from one fluid to another, by direct contact or by indirect
contact. In a heat exchanger the heat transfer through
radiation is negligible in comparison to conduction and
convection. But convection plays the major role in the
performance of a heat exchanger. There are numerous
applications of heat exchangers such as heat recovery
systems, refrigeration, waste water treatment plants,
pharmaceuticals, oil and gas industries, HVAC, food &
beverage processing industries. In addition to these
applications heat exchangers are also used in large scale
chemical and process industries for transferring the heat
between two fluids which are at a single or two states [1].
In general, the heat transfer techniques can be divided into
two groups: active and passive. The active techniques
need external forces like fluid vibration, electric field and
surface vibration where as passive techniques requires
special surface geometries like varied tube inserts. The
straight tube heat exchanger has been the oldest type of
heat exchanger that has been in use. The research work
has been performed by various investigators on enhancing
the performance of straight tube heat exchanger by
changing geometric such as baffle arrangement [2], types
of tube arrangement, length of the pipe etc. The main
challenge in heat exchanger design is to make it compact
and to get maximum heat transfer in minimum space.
However, it was found that straight tube heat exchangers
have restriction in terms of sizing and space which are
significant parameters while designing industrial heat
exchangers. In 1970 Charles Boardman and John Germer
introduced helical coil tube heat exchanger as one of the
best passive heat transfer enhancement techniques. The
various experimental research work have indicated that
helical coil tube heat exchangers are the most useful
because of its spiral coil configuration which provides
more heat transfer area and better flow in minimum space
[3]. This configuration leads higher heat transfer
coefficient as compared to straight tube heat exchanger
under the same experimental conditions. Natural
convection is a phenomenon that governs the exchange of
heat between medium in heat exchanger is considered
here. Since a complex flow pattern exist inside helically
tube, as fluid flow through helical tube due curvature
nature centrifugal force of fluid causes development the
secondary flow pattern inside tube this led to
improvement in heat transfer rate [6]. Instead of Reynolds
number Dean number used in analysis as it take into
account effect of curvature of helical pipe. [4].
1.1 Helical Coil Heat Exchangers.
The helical coil heat exchangers are a compact shell and
tube design consisting of several layers of coiled tubes
within a closed shell. The basic construction of the type
used for this experimental work with the appropriate
nomenclature is illustrated in Figure 1. The helical coil
has:

H – Height of pitch,
2r – Diameter of tube,
2Rc – Diameter of helical coil,
i – Curvature ratio (i.e. ratio of tube and coil diameter),
2α – The helix angle (angle between its projection on a
surface and measuring angle between the coils).
The flowing fluid experiences centrifugal force because of
curved shape of the tube. The local axial velocity of the
fluid particle and the radius of curvature of the coil decide
the magnitude of centrifugal force experienced. The
velocity of fluid particles flowing at the core of the tube is
higher than those flowing near to the tube wall. Thus, less
centrifugal force will be experienced by the fluid particles
flowing close to the tube wall than in the tube core. This
pushes the fluid from the core region towards the outer
wall (away from the coil axis). This stream bifurcates at
the wall and drives the fluid towards the inner wall on the
tube bound, inflicting generation of counter-rotating
vortices referred to as secondary flows [5]. This leads to
produce extra transport of the fluid over the cross section
of the tube. This extra convective transport will increase
the heat transfer and therefore the pressure drop when
compared to straight tube. It’s been found that the impact
of coil curvature is to suppress turbulent fluctuations
arising within the flowing fluid and smoothing the
emergence of turbulence. Thus it will increase the value of
the Reynolds number (Re) needed to attain a fully
turbulent flow, as compared to it of a straight pipe. The
impact of turbulent fluctuations suppression enhances as
the curvature ratio of coil increases.
Figure1: - Helical Coil Tube.
2. EXPERIMENTAL SETUP
The schematic of the experimental set-up used for the
present investigation is shown in Figure 1. The main
components in the set up include helical coil tube,
thermometer, hot and cold water tank, heating element,
flow controlling and measuring devices. The helical coil
copper tube is placed in the shell and hot water is made to
flow through tube. To ensure maximum heat transfer the
copper helical coil is fully immersed in the cold water
flowing through the shell. The arrangement is made so
that, flow direction of hot and cold water is perfectly
counter by manner. The water in the storage tank is
heated using a heating element, as the water reaches to a
prescribed temperature the hot water circulates through
the helical coil. The tube side hot water flow rate was
measured using measuring jar and stop watch. The inlet
and outlet temperatures of hot and cold water were
recorded using thermometer. The tube and shell side
thermo-physical properties of water were assessed at
their mean temperatures.
Figure 2:- experimental set-up
Table I: - Characteristics dimension of helical coil Tube
Sr. No. Parameters Dimension
1 Turns of helical Coil 8 Turn
2 Inner Diameter of
Coil
8 mm
3 Outer Diameter 10 mm
4 Wall Thickness 2 mm
5 Stretched length of
Coil
762 mm
6 Helical Diameter of
Coil
50 mm
7 Fluid used Water
Table II: - Range of operating parameters.
Sr.
No.
Parameters Range
1 Tube side water
flow rate
0.0238 kg/s – 0.03571
kg/s
2 Shell side water
flow rate
0.0349 kg/s – 0.04682
kg/s
3 Tube inlet
Temperature
75 0C - 80 0C
4 Tube outlet
Temperature
62 0C - 71 0C
5 Shell inlet
Temperature
35 0C - 37 0C
6 Shell outlet
Temperature
44 0C - 52 0C

Data Reduction:-
LMTD=
Where, ∆T1 = Thi - Tco , ∆T2 = Tho – Tci
Overall, U0 =
Average Discharge, Qavg =
Reynolds No. ,
Effectiveness, ϵ =
–
–
=
–
–
Where, Ch= Cph Cc= Cpc
V. RESULTS
Figure 4 shows the graph of mass flow rate of hot water Vs
effectiveness. It is observed that effectiveness of helical
coil heat exchanger increases with addition of nano
particle in the working fluid from 0.28 to 0.43 as mass
flow rate of hot water increases.
Results for various mass flow rate of hot water with
addition of Nano Particle.
Sr.
No.
∆T1
( 0C )
∆T2
( 0C )
LMTD ϵ
Uo
(kW)
Re
1 35.84 40.32 38.03 0.28 376.12 403
2 34.16 38.08 39.45 0.30 499.99 512
3 30.24 33.60 31.88 0.33 785.43 603
4 33.04 35.84 34.41 0.34 519.45 557
5 30.24 33.60 31.88 0.36 761.43 709
6 25.76 30.24 27.93 0.43 1109.81 835
1) Mass flow rate vs Effectiveness With Nano Particle:-
Chart 1. Shows the graph of mass flow rate of hot water Vs
effectiveness. It is observed that effectiveness of Plane
pipe heat exchanger initially increases and it goes on
increases from 0.28 Kg/s to 0.43 Kg/s. This one of the
desirable effect. We have found after experimentation.
Chart 1:- Mass flow rate vs Effectiveness with Nano
Particle
2) Mass flow rate vs Overall Heat Transfer With Nano
Particle:-
Chart 2:- Mass flow rate vs Overall Heat Transfer with
Nano Particle
Chart 2 shows the graph of mass flow rate of hot water Vs
overall heat transfer coefficient. It is observed that as mass
flow rate of hot water increases the overall heat transfer
coefficient of heat exchanger increases.
3) Mass flow rate vs Reynolds No. With Nano Particle:-
Chart 3:- Mass flow rate vs Reynolds No. With Nano
Particle
Chart 3 shows the graph of mass flow rate of hot water Vs
Reynolds number. As the Reynolds number is directly
proportional to flow velocity, The mass flow rate of hot
water with nano particle mixied increases with increase
in Reynolds number, this is because the flow velocity
increases.
0
200
400
600
800
1000
ReynoldsNumber
Mass Flow Rate
Mass flow rate Vs Reynolds No.
δ=0
δ=0.16

VI. CONCLUSION
An experimental investigation was carried out to review
the overall heat transfer coefficients and effectiveness of
helically coiled tube heat exchangers. It is observed that,
once cold water mass flow rate is constant and hot water
mass flow rate is increased the overall heat transfer
coefficient will increase with the addition of nano particle
in working fluid. The helical tube permits the water with
the addition of nano particle to be in contact for larger
period of time in order that there is an enhanced heat
transfer compared to that of straight tube. It is also
observed that hot water mass flow rate greatly affects
effectiveness of heat exchanger. The effectiveness of
helical coil heat exchanger gradually increases as flow rate
of hot water increases. The overall heat transfer of heat
exchangers depends on its LMTD.
REFERENCES
1] Experimental investigation of heat transfer
enhancement in helical coil heat exchangers using
water based CuO nanofluid; P.J. Fule, B.A. Bhanvase,
S.H. Sonawane; Advanced Powder Technology 28
(2017) 2288–2294.
2] Correct interpretation of nanofluid convective heat
transfer; M.H. Buschmann, R. Azizian, T. Kempe, J.E.
Juliá, R. Martínez-Cuenca, B. Sundén, A. Seppälä, T.
Ala-Nissila; International Journal of Thermal Sciences
129 (2018) 504–531.
3] Experimental investigation on intensified convective
heat transfer coefficient of water based PANI
nanofluid in vertical helical coiled heat exchanger; B.A.
Bhanvase, S.D. Sayankar, A. Kapre, P.J. Fule,S.H.
Sonawane; Applied Thermal Engineering 128 (2018)
134–140.
4] Recent research contributions concerning use of
nanofluids in heat exchangers: A critical review;
Mehdi Bahiraei,Reza Rahmani, Ali Yaghoobi,Erfan
Khodabandeh,Ramin Mashayekhi, Mohammad Amani;
Applied Thermal Engineering 133 (2018) 137–159.
5] Mechanisms proposed through experimental
investigations on thermophysical properties and
forced convective heat transfer characteristics of
various nanofluids –A review M.Chandrasekar, S.
Suresh, T. Senthilkumar; Renewable and Sustainable
Energy Reviews 16 (2012) 3917–3938.
6] Numerical Heat Transfer Analysis of Wavy Micro
Channels with Different Cross Sections,Karan Ghule*,
M.S. Soni, Energy Procedia 109( 2017 ) 471 – 478.
7] Enhancement of heat transfer coefficient through
helical coil; Rahul G.Karmankar; International
Research Journal of Engineering and Technology
(IRJET) e-ISSN: 2395 -0056 p-ISSN: 2395-0072
8] Experimental Study on Helical Coil Heat Exchanger; A.
A. Ayare, S. D. Anjarlekar, M. N. Tagare and S. S.
Wamane; International Journal of Scientific and
Research Publications, Volume 7, Issue 5, May 2017,
ISSN 2250-3153 .
9] Convective Heat Transfer Analysis from Helically Coiled
Tube Using CFD and Experimental Methodology, Mr.
G. G.Gore, PG Scholar, Dr. R. B. Yarasu; IJSRD -
International Journal for Scientific Research &
Development| Vol. 3, Issue 02, 2015 | ISSN (online):
2321-0613.
10] Experimental analysis of helical coil heat exchanger by
using different compositions of nano fluids;Kevin
Kunnassery, Rishabh Singh, Sameer Jackeray;
International Journal of Innovative and Emerging
Research in Engineering Volume 4, Issue 1, 2017 e-
ISSN: 2394 – 3343,p-ISSN: 2394 – 5494.
11] Computational Analysis of Different Nanofluids effect
on Convective Heat Transfer Enhancement of Double
Tube Helical Heat Exchanger; Saurabh Kumar, Neha
Maheshwari, Dr. Brajesh Tripathi; International
Journal of Scientific Engineering and Applied Science
(IJSEAS) - Volume-1, Issue-4, June 2015 ISSN: 2395-
3470.
12] Correct interpretation of nanofluid convective heat
transfer; M.H. Buschmann, R. Azizian, T. Kempe, J.E.
Juliá, R. Martínez-Cuenca, B. Sundén, A. Seppälä, T.
Ala-Nissila; International Journal of Thermal Sciences
129 (2018) 504–531.
13] Heat Transfer Performance of Different Nanofluids
Flows in a Helically Coiled Heat Exchanger ;M.A.
Khairul, R. Saidur, Altab Hossain, M.A. Alim, I.M.
Mahbubul; Advanced Materials Research Vol. 832
(2014) pp 160-165.
14] Thermal Analysis of a Helical Coil Heat Exchanger;
Amol Andhare, V M Kriplani, J P Modak; International
Journal of Innovative Research in Advanced
Engineering (IJIRAE) ISSN: 2349-2163 , Volume 1
Issue 12 (December 2014).
15] Heat Transfer Enhancement in Heat Exchanger by
using Nano Fluid: a Review ; N. N. Bhosale, D. B. Gade,
S. Y. Gonda, V. J. Sonawane, A. A. Keste; IOSR Journal of
Mechanical and Civil Engineering (IOSR-JMCE) e-ISSN:
2278-1684,p-ISSN: 2320-334X PP. 89-93.

IRJET-Experimental Study on Helical Tube Heat Exchanger by Varying Cross Section using Nano Particles

More Related Content

What's hot (20)

Similar to IRJET-Experimental Study on Helical Tube Heat Exchanger by Varying Cross Section using Nano Particles (20)

More from IRJET Journal (20)

Recently uploaded (20)

IRJET-Experimental Study on Helical Tube Heat Exchanger by Varying Cross Section using Nano Particles