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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1193
CONVECTIVE HEAT TRANSFER ANALYSIS IN A HELICAL COIL
1M.E. Scholar, Department of Mechanical Engineering, Maharashtra Institute of Technology, Aurangabad India
2Professor, Department of Mechanical Engineering, Maharashtra Institute of Technology, Aurangabad India
-----------------------------------------------------------------------***-------------------------------------------------------------------------
Abstract- Twisted pipes are classified on the base of curve
as constant curve and variable curve pipes. The former are
called as “helices” i.e. spiral coil & the ultimate as ‘ spirals ”.
When a fluid flows in a helically curled tube centrifugal
forces causes secondary fluid stir, which gives rise to
increase heat transfer rate. At veritably short distances from
the launch of heat transfer zone, the thermal boundary
subcaste is too thin to be affected by the secondary inflow
field, which reaches its maximum intensity at some distance
down from the tube wall. thus, near the tube inlet the rate of
heat transfer measure in a curled tube to that in a straight
tube varies only as NDe1/6 and Coil tube offers little
advantage over a straight tube. The present work involves
fabrication of a setup for spiral coil of ID8.04 mm & OD9.70
mm and 3800 mm length. The coil consists of a tank of ID
305 mm with a bath result like water. The face temperature
of spiral coil at different positions, bath temperature are
measured on digital temperature archivist. The water bay
and outlet temperature are measured by thermometer. The
work involves analysis of heat transfer between bath result
and water flowing through the spiral coil. The convective
heat transfer will be anatomized for with and without
agitation. The ideal of this discussion work is to gain a better
and further quantitative sapience into the heat transfer
process that occurs when a fluid flows in a spiral coils tube.
Keywords--Heat Transfer1, Helical coil2, copper Coil
3
1. INTRODUCTION
Spiral coils are compact in size and provides distinct
benefit like advanced film measure, more effective
application of available pressure drop, which results in
effective and less precious design. spiral coil permits
running of high temperature and extreme temperature
differentials without high convinced stresses or expensive
expansion joints. spiral coil offers advantages over straight
tubes due to their conciseness and increased heat transfer
measure. The increased heat transfer portions are a
consequence of the curve of the coil, which induces
centrifugal forces to act on the moving fluid, performing in
secondary inflow. A Flow through Helical Coil When a fluid
flows through a straight tube the haste is maximum at the
tube centre, zero at the tube wall and symmetrically
distributed about the axis. still when a fluid flows through
a twisted tube, the primary haste profile shown in Fig -1.1
is distorted by the addition of secondary inflow pattern.
The secondary inflow is generated by the centrifugal
action and acts in the Aeroplan
vertical to the primary inflow. Since the haste is maximum
at the tube centre the fluid at the centre is subordinated to
maximum centrifugal action, which pushes the fluid
towards external wall. The fluid at the external wall moves
inward along the tube wall to replace the fluid ejected
outwards. This results in the conformation of two
maelstroms symmetrically about a vertical aeroplane
through the tube center.
Fig-1 Basic Geometry of Helical Coil
1.2.1 Heat Transfer in Helical coil: - The heat and
mass transfer are advanced in a twisted pipe than in an
original straight tube at the same inflow rate, due to
actuality of superimposed secondary inflow (5).
Flow in twisted path is a complex miracle because of the
presence of centrifugal forces acting on rudiments of liquid
flowing through similar pipes. To balance this centrifugal
force, a pressure grade across the pipe is formed. The
pressure is maximum at external wall and minimum at the
inner wall. This results in a secondary inflow, in which the
fluid near the top and nethermost moves inward and the
fluid in the middle moves outward. The secondary inflow
is the cause of high heat transfer rates and disunion losses
in a pipe.
Dr A.T. Autee
1Mr. Ankush J. Kakode, 2
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1194
operation of Helical Coil- Helical coils are considerably
employed for heat transfer operation in the process and
power diligence.
Some of the operations are listed as
1. spiral coils are used for transferring heat in a chemical
reactor and agitated vessel because heat transfer portions
are advanced in spiral coils. This is especially important
when chemical reactors having high heat of response are
carried out and the heat generated( or consumed) has to
be transferred fleetly to maintain the temperature of the
response. Also because of spiral coils have a compact
configuration further heat transfer face can be handed per
units of space than by use of straight tube.
2. Due to conciseness, it's used for brume generation in
marine and artificial operation.
3. The actuality of tone- convinced acceleration field in
spiral coil makes spiral coil most desirable for heat
transfer and fluid inflow operation in the absence of a
graveness field, similar as for spaceships in external space.
4. spiral coils have lately being studied for possible
operation inbio-engineering. Weissman and Mockero’s
lately studied the use of spiral coils to compound mass
transfer in membrane blood- oxygenerators. Their study
demonstrated, both theoretically and experimentally that
by curling a membrane tube into a spiral coil, they could
mainly increase the mass transfer rate of oxygen and
carbon dioxide to and from the blood flowing inside the
tube.
5. spiral coils have been considerably used in the cryogenic
assiduity for the liquefaction of feasts. The single pressure
mixed refrigerant (SPMR) process for the liquefaction of
the natural gas is a current illustration. Recent emphasis
on the increased product of thawed natural gas will call for
an increased use of curled tube heat exchangers.
1.3 Scope of Work: -Helical coils are widely used in all
fields of engineering, so a thought is given to
experimentally suggest the values of heat transfer
coefficients, the various numbers associated with heat
transfer phenomenon and suggest a fluid which gives
maximum overall heat transfer coefficient.
The dissertation consists of selection and fabrication of
various components required for the experimental
analysis of flow inside a helical coil. The setup for the
analysis consists of copper helical coils of inner diameter
8.04 mm and length 3800 mm. The set up required a tank
or vessel of internal diameter as 30.5 cm to accommodate
the helical coil along with a heating element of 1500 watt.
The work involves the analysis of results obtained for fluid
like water. The work carried out for the both with and
without agitation condition for all fluids.
2. EXPERIMENTAL SETUP
2.1 Introduction: The convective analysis of helical coil,
requires the experimental set up to record various
temperature along the length of coil at different heat input
and at different mass flow rate. The setup requires
fabrication & selection of different component for the
analysis purpose.
2.2 Experimental setup :
Fig - 2.1 Shows the schematic arrangement of the various
components required for the experimentation.
1. Fill the cylindrical tank with water such that the
entire setup of helical coil immersed in liquid.
2. Adjust the heat supplied to setup by properly
adjusting dimmer. Heat input should be recorded
from the values of voltage and current.
3. Adjust the flow rate of water entering in helical
coil in a way to maintain constant flow rate after
enough heating of liquid.
4. Note down the various thermocouple reading with
the help of temperature indicator at steady state.
5. Carry out the experimentation for the various
values of heat input and by changing the mass
flow rate.
2.3 Component used: The list of components along with
material & specification for experimentation is given in
table no.3.1
Table 3.1 : Different component used for the experimental
setup.
Sr. No. Name of
component
Material Specification
1. Helical coil Copper ID 8.04 mm,
OD 9.70mm
& length
380cm
2. Cylindrical GI sheet ID 30.5 cm
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1195
tank Height 41 Cm
Wall
thickness 25
mm
3. Thermo
couple and
digital
temperature
indicator
-----
A digital
temperature
indicator
with 6 point
selector
switch and
thermo
couple wire
& junction.
4 Dimmer stat ----- 6 Amp
Dimmer stat
with a range
of 0-230 Volt
5 Stirrer
-----
¼ HP cooler
motor pump
of RPM 1360,
amp 0.36, 50
Hz and 45
watt.
6. Flow
measuring
Device
Glass A glass biker
of 1 liter
marking
7 Heating coil Copper 1500-watt
drum heating
coil
The various thermocouples mounted along the length of
coil are worked as per the distance specified and are
enlisted in table no.2.1
2.4 Criteria for selection of component:
2.4.1 Helical Coil: The material selection for the spiral coil
is similar that, it must have high thermal conductivity. At
the same time material should be easy to bend in the form
of spiral structure, so the material named for the spiral coil
which has both these parcels & it's fluently available. The
dimension of spiral coil like inner dia. & length are named
grounded on the vacuity of material and at the same time
to accommodate the number of thermocouples along the
length. To achieve proper heat transfer five turns of spiral
coils of bobby material is named grounded on length of coil
as shown iffig.3.2
Fig - 3.2 Helical coil
2.4.2 Cylindrical Tank: The criteria for selection of
spherical tank should be similar that, the spiral coil
arrangement, the heater and stirrer for agitation must
accommodate in it. Considering the proper sizes, height of
coil & the distance of spiral coil from the heater, a
spherical tank of dimensions30.5 cm inner periphery,
height41.0 cm with a consistence of 25 mm is named as
shown in fig3.3. The tank named is of material GI & is the
same used for water heater purpose in the home
operation.
2.4.3 Thermocouple and Digital Temperature
Indicator To record the colorful temperature of water
inside the coil at colorful distances 5 Cr- Al thermocouples
Fig - 3.3 Cylindrical tank
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1196
are named. To record the temperature, a digital
temperature index as shown in fig3.4., of least count0.10 c
and the range of 0- 5000 C is named.
2.4.4 Dimmerstat: A dimmerstat of range( 0- 1500 W) is
named to fulfill the demand of varying heat input to assay
the performance of heat transfer between water & colorful
result as shown in fig3.5..
Fig - 3.5 Dimmerstat
2.4.5 Stirrer: For proper mixing of various solution & to
increase the turbuance a stirrer is required. In this setup, a
¼ HP cooler motor pump of 1360 rpm is used as stirrer.
2.4.6 Flow Measuring Device: To measure the quantity of
water flowing through the helical coil, a 1 lit glass
measuring jar is used.
2.4.7 Heating Coil: A 1500-watt drum heating coil is used
to heat the bath solution in the tank.
Fig - 3.6 Photograph of Experimental Setup
2.5 Testing procedure: The convective heat transfer
analysis of spiral coil is principally heat transfer between
the bath liquid & fluid flowing through spiral coil i.e. water.
The bath liquid used for the analysis purpose are water. To
find out the colorful parameters needed for the analysis
certain procedure must be espoused. So a testing
procedure is designed and the same as followed during
this trial.
To avoid any leakages, originally a leak test of the
experimental setup is assured at outside inflow rate of
fluid. The testing procedure is listed as follows.
1. Fill the spherical tank with proper liquid(viz. watersuch
that the entire setup of spiral coil immersed in liquid.
2. Acclimate the heat supplied to setup by duly conforming
dimmer. Heat input should be recorded from the values of
voltage and current.
3. Acclimate the inflow rate of water entering in spiral coil
in a way to maintain constant inflow rate after enough
heating of liquid.
4. Note down the colorful thermocouple reading with the
help of temperature index at steady state.
5. Carry out the trial for the colorful values of heat input
and by changing the mass inflow rate.
1. Instruments Used for Performance
The colorful instruments used for testing purpose are as
follows
1. Ammeter (0 – 10 A)
2. Voltmeter (0- 230 V)
3. Thermocouple
Dimmer stat
Dimmer
Voltmeter Ammeter
Temp
Indicator
Agitator
Water inlet
Water outlet
Thermometer
Measuring jar
G.I. Vessel
Dimmer stat
Dimmer
Voltmeter Ammeter
Temp
Indicator
Agitator
Water inlet
Water outlet
Thermometer
Measuring jar
G.I. Vessel
Fig - 3.4 Digital temperature indicator
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1197
4. Measuring jar and stop watch( due to attainability of
Rotameter)
5. Tachometer
3. RESULTS AND DISCUSSION
The measure readings recorded in table 3.3 - 3.8 are used
for calculation of heat transfer coefficient, over all heat
transfer coefficient, the convective analysis governed with
various non dimensional numbers and Nusselt number
correlation. Depending upon the flow conditions the
analysis requires numbers like Re number, Nusselt
number, Pr number, De number..
3.2 Calculation:
3.2.1 Calculation for Deciding Type of Flow : In helical
coil flow of fluid is a function of Reynold number and
Prandtl number.
For deciding laminar and turbulent flow following
equation are used (3),
For laminar flow
For turbulent flow,
Sample calculation for water at head input 0.6 kw and
mass flow rate of 5.75 gm/sec,
Pr = 4.92 > 1 & Re= 0.621 > 0.4
 Flow is turbulent
3.2.2 Calculation for Heat Transfer Coefficient:
Heat transfer coefficient in helical coil is calculated by
using equation are used (3), Sample calculation for water
at heat input Qi = 0.6 kw and mass flow rate of 5.75
gm/sec,
From equation 4.5,
Pr = 4.92 Re = 1170
di = 8.04 mm De = 259
Nu = 13.74
Nu =
Where, k = 0.626 W/m2 0k = Thermal conductivity which is
taken from thermo physical properties of water at 34.50c
(22)
 hi = 1.069 Kw/m2 0k
3.2.3 Calculation for Over All Heat Transfer
Coefficient :
The overall heat transfer coefficient is calculated by using
the relation stated as per (3) by equation
Where,
U – Overall heat transfer coefficient
Q – Heat flow rate
A – Area of the helical coil at outside
Tb – Bath temperature
Tm – Mean temperature of the helical coil
Sample calculation for water at head input 0.6 kw and
mass flow rate of 5.75 gm/sec,
Appendix A-D shows the calculated values of Re number,
Nu number, hi, and U for water for without agitation and
with agitation at a different concentration.
4 CONCLUSION
To analyses the convective heat transfer miracle in a spiral
coil fluids like water is used during the trial. Water is used
as a fluid flowing through spiral coil whereas fluid stated
above are allowed to compass the entire spiral coil.
Grounded on the trial the number of parameters is studied.
On the base of below results and discussion following
conclusion are drawn.
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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072
© 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1198
REFERENCES
[1] C.F.C. Rogers and Y.R. Mayhew “Heat Transfer and
Pressure Loss in Helically Coiled Tubes With
Turbulent Flow”, Int. Journal of Heat Mass Transfer,
Vol – 7 PP 1207- 1216, 1964.
[2] Venugopal Kabair and N.R. Kuloor “Heat Transfer to
Newtonian Fluids in Coiled Pipe in a Laminar Flow”,
Inst. Journal Heat and Mass Transfer Vol – 9, PP 69-
75, 1966
[3] Yasuo Mori and Wataru Nakayama “Study of Forced
Convective Heat Transfer in Curved Pipes”, Inst.
Journal Heat Mmass transfer Vol – 10 PP 681 – 695,
1967.
[4] R. A. Seban and E.F. Mcloughlin “Heat Transfer In
Tube Coils With Laminar And Turbulent Flow” Inst.
J. Heat mass transfer Vol – 6 pp 387-395, 1963.
[5] A. N. Dravid, K. A. Smith, E. W. Merill and P. L. T.
Brain “Effect Of Secondary Fluid On Laminar Flow
Heat Transfer In A Helically Coiled Tubes” Al.
Chemical Engine Journal Vol 17, No 5 pp 1114- 1122
sept. 1971.
[6] C.E. Kalb and J. D. Seadar, “Heat And Mass Transfer
Phenomina For Vis Cous Flow In Curved Circular
Tubes” Inst. J. Heat Mass transfer Vol 15, pp 801-
817, 1972.
[7] S. Raja Sekaran, V. G. Kabair and N. R. Kuloor,
“Secondary Flow Of Non – Newtanian Fluids In
Helical Coils” Indian Journal of Technology, vol 4,
Feb – 1966.
[8] G.S. Arvind, Y. Aran, R. Sunder and S. Subrahmaniyan
“Natural Convective Heat Transfer in Helically
Coiled Heat Exchange” Vol 84, sept. 2003, I.E. (I)
Journal
[9] V.V. Sitram Murthy and R. C. Sastrey “Laminar
Convective Heat Transfer And Viscous And Non
Newtonian Liquids In Helically Coiled Tube” Indian
Chemical Engineer Section A, Vol 42, No. 1. Jan –
March 2000
[10] A. Ramasubramanian and S.K. Pandey “Agitation
And Heat Transfer Studies In Suspension
Transaction Of ASME, Vol 117, Feb 1995.
[11] R.K. Prabhudesai and Shah “ Heat Transfer Though
Helical Coils” traction of I.I. Ch.E. Vol. XII, 1959-60.
[12] S. Manafzadeh, H.A. Simon and JCF chow “Heat
Transfer Enhancement In Coiled Tubes” letters in
heat and mass transfer, Vol – 9 PP 479-435, 1982.
[13] S.N. Gupta and P. Mishra “Isothermal Laminar Flow
of Non Newtonian Fluids Though Helical Coils”
Indian Journal of technology, Vol 13, June 1975 PP
245-250.
[14] Venugopal Kabair and N.R. Kuloor “Comparision Of
Performance Of Helical And Spiral Coil Heat
Exchange” and “Secondary Flow Of Non Newtonan
Fluids In Helical Coils” Indian Journal of technology,
Vol 4 Feb 1966.
[15] D.G. Prabhajan, G.S. Paghavan and T.J. Renie
“Comparison of Heat Transfer Rates Between A
Straight Tube Heat Exchange And Helically Coiled
Heat Exchange”
[16] E. De maerteleire “Heat Transfer to A Helical Coil In
Mechanically Agitauted Gas Ligit Dispersaion”
chemical engg. Science Vol 33 PP 107-1113. 1978
[17] Shashi Krishna Pandey “Heat Transfer Studies For
Agitated Liquits” CEW Vol XIII No. 9 Page 47-50,
sept 1978.
[18] Wang Kai and Yu shengyao, “Heat Transfer And
Power Consumption Of Non – Newtanian Fluids In
Agitated Vessels”, Chemical engineering science, Vol
44, No 1, PP 33-40, 1989.
[19] S. Rajasekharan, V.G. Kubair and N. R. Kuloor “Heat
Transfer To Non Newtonian Fluids In Coiled Pipes In
Laminar Flow” Int. Journal of heat and mass transfer
Vol 13 PP 1583-1594, 1970.
[20] A.V. Kirpikov, “Heat Transfer In Helically Coiled
Pipes,” Trudi moskov, first ktim, Moshinojtrojenija
12, 43-56 (1957)
[21] James R. Lines ‘Hellically Coiler Heat Exchanges
Offer Advantages Petroleum Enginner, April 1952.
[22] S. Domkundwar, “Heat Transfer Data Book”
Dhampat Rai publication New Delhi.
[23] B.T. Najaguna, “Thermal Science Data Book”, Tata
MaGraw-Hill Co. Ltd. , New Delhi.

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CONVECTIVE HEAT TRANSFER ANALYSIS IN A HELICAL COIL

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1193 CONVECTIVE HEAT TRANSFER ANALYSIS IN A HELICAL COIL 1M.E. Scholar, Department of Mechanical Engineering, Maharashtra Institute of Technology, Aurangabad India 2Professor, Department of Mechanical Engineering, Maharashtra Institute of Technology, Aurangabad India -----------------------------------------------------------------------***------------------------------------------------------------------------- Abstract- Twisted pipes are classified on the base of curve as constant curve and variable curve pipes. The former are called as “helices” i.e. spiral coil & the ultimate as ‘ spirals ”. When a fluid flows in a helically curled tube centrifugal forces causes secondary fluid stir, which gives rise to increase heat transfer rate. At veritably short distances from the launch of heat transfer zone, the thermal boundary subcaste is too thin to be affected by the secondary inflow field, which reaches its maximum intensity at some distance down from the tube wall. thus, near the tube inlet the rate of heat transfer measure in a curled tube to that in a straight tube varies only as NDe1/6 and Coil tube offers little advantage over a straight tube. The present work involves fabrication of a setup for spiral coil of ID8.04 mm & OD9.70 mm and 3800 mm length. The coil consists of a tank of ID 305 mm with a bath result like water. The face temperature of spiral coil at different positions, bath temperature are measured on digital temperature archivist. The water bay and outlet temperature are measured by thermometer. The work involves analysis of heat transfer between bath result and water flowing through the spiral coil. The convective heat transfer will be anatomized for with and without agitation. The ideal of this discussion work is to gain a better and further quantitative sapience into the heat transfer process that occurs when a fluid flows in a spiral coils tube. Keywords--Heat Transfer1, Helical coil2, copper Coil 3 1. INTRODUCTION Spiral coils are compact in size and provides distinct benefit like advanced film measure, more effective application of available pressure drop, which results in effective and less precious design. spiral coil permits running of high temperature and extreme temperature differentials without high convinced stresses or expensive expansion joints. spiral coil offers advantages over straight tubes due to their conciseness and increased heat transfer measure. The increased heat transfer portions are a consequence of the curve of the coil, which induces centrifugal forces to act on the moving fluid, performing in secondary inflow. A Flow through Helical Coil When a fluid flows through a straight tube the haste is maximum at the tube centre, zero at the tube wall and symmetrically distributed about the axis. still when a fluid flows through a twisted tube, the primary haste profile shown in Fig -1.1 is distorted by the addition of secondary inflow pattern. The secondary inflow is generated by the centrifugal action and acts in the Aeroplan vertical to the primary inflow. Since the haste is maximum at the tube centre the fluid at the centre is subordinated to maximum centrifugal action, which pushes the fluid towards external wall. The fluid at the external wall moves inward along the tube wall to replace the fluid ejected outwards. This results in the conformation of two maelstroms symmetrically about a vertical aeroplane through the tube center. Fig-1 Basic Geometry of Helical Coil 1.2.1 Heat Transfer in Helical coil: - The heat and mass transfer are advanced in a twisted pipe than in an original straight tube at the same inflow rate, due to actuality of superimposed secondary inflow (5). Flow in twisted path is a complex miracle because of the presence of centrifugal forces acting on rudiments of liquid flowing through similar pipes. To balance this centrifugal force, a pressure grade across the pipe is formed. The pressure is maximum at external wall and minimum at the inner wall. This results in a secondary inflow, in which the fluid near the top and nethermost moves inward and the fluid in the middle moves outward. The secondary inflow is the cause of high heat transfer rates and disunion losses in a pipe. Dr A.T. Autee 1Mr. Ankush J. Kakode, 2
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1194 operation of Helical Coil- Helical coils are considerably employed for heat transfer operation in the process and power diligence. Some of the operations are listed as 1. spiral coils are used for transferring heat in a chemical reactor and agitated vessel because heat transfer portions are advanced in spiral coils. This is especially important when chemical reactors having high heat of response are carried out and the heat generated( or consumed) has to be transferred fleetly to maintain the temperature of the response. Also because of spiral coils have a compact configuration further heat transfer face can be handed per units of space than by use of straight tube. 2. Due to conciseness, it's used for brume generation in marine and artificial operation. 3. The actuality of tone- convinced acceleration field in spiral coil makes spiral coil most desirable for heat transfer and fluid inflow operation in the absence of a graveness field, similar as for spaceships in external space. 4. spiral coils have lately being studied for possible operation inbio-engineering. Weissman and Mockero’s lately studied the use of spiral coils to compound mass transfer in membrane blood- oxygenerators. Their study demonstrated, both theoretically and experimentally that by curling a membrane tube into a spiral coil, they could mainly increase the mass transfer rate of oxygen and carbon dioxide to and from the blood flowing inside the tube. 5. spiral coils have been considerably used in the cryogenic assiduity for the liquefaction of feasts. The single pressure mixed refrigerant (SPMR) process for the liquefaction of the natural gas is a current illustration. Recent emphasis on the increased product of thawed natural gas will call for an increased use of curled tube heat exchangers. 1.3 Scope of Work: -Helical coils are widely used in all fields of engineering, so a thought is given to experimentally suggest the values of heat transfer coefficients, the various numbers associated with heat transfer phenomenon and suggest a fluid which gives maximum overall heat transfer coefficient. The dissertation consists of selection and fabrication of various components required for the experimental analysis of flow inside a helical coil. The setup for the analysis consists of copper helical coils of inner diameter 8.04 mm and length 3800 mm. The set up required a tank or vessel of internal diameter as 30.5 cm to accommodate the helical coil along with a heating element of 1500 watt. The work involves the analysis of results obtained for fluid like water. The work carried out for the both with and without agitation condition for all fluids. 2. EXPERIMENTAL SETUP 2.1 Introduction: The convective analysis of helical coil, requires the experimental set up to record various temperature along the length of coil at different heat input and at different mass flow rate. The setup requires fabrication & selection of different component for the analysis purpose. 2.2 Experimental setup : Fig - 2.1 Shows the schematic arrangement of the various components required for the experimentation. 1. Fill the cylindrical tank with water such that the entire setup of helical coil immersed in liquid. 2. Adjust the heat supplied to setup by properly adjusting dimmer. Heat input should be recorded from the values of voltage and current. 3. Adjust the flow rate of water entering in helical coil in a way to maintain constant flow rate after enough heating of liquid. 4. Note down the various thermocouple reading with the help of temperature indicator at steady state. 5. Carry out the experimentation for the various values of heat input and by changing the mass flow rate. 2.3 Component used: The list of components along with material & specification for experimentation is given in table no.3.1 Table 3.1 : Different component used for the experimental setup. Sr. No. Name of component Material Specification 1. Helical coil Copper ID 8.04 mm, OD 9.70mm & length 380cm 2. Cylindrical GI sheet ID 30.5 cm
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1195 tank Height 41 Cm Wall thickness 25 mm 3. Thermo couple and digital temperature indicator ----- A digital temperature indicator with 6 point selector switch and thermo couple wire & junction. 4 Dimmer stat ----- 6 Amp Dimmer stat with a range of 0-230 Volt 5 Stirrer ----- ¼ HP cooler motor pump of RPM 1360, amp 0.36, 50 Hz and 45 watt. 6. Flow measuring Device Glass A glass biker of 1 liter marking 7 Heating coil Copper 1500-watt drum heating coil The various thermocouples mounted along the length of coil are worked as per the distance specified and are enlisted in table no.2.1 2.4 Criteria for selection of component: 2.4.1 Helical Coil: The material selection for the spiral coil is similar that, it must have high thermal conductivity. At the same time material should be easy to bend in the form of spiral structure, so the material named for the spiral coil which has both these parcels & it's fluently available. The dimension of spiral coil like inner dia. & length are named grounded on the vacuity of material and at the same time to accommodate the number of thermocouples along the length. To achieve proper heat transfer five turns of spiral coils of bobby material is named grounded on length of coil as shown iffig.3.2 Fig - 3.2 Helical coil 2.4.2 Cylindrical Tank: The criteria for selection of spherical tank should be similar that, the spiral coil arrangement, the heater and stirrer for agitation must accommodate in it. Considering the proper sizes, height of coil & the distance of spiral coil from the heater, a spherical tank of dimensions30.5 cm inner periphery, height41.0 cm with a consistence of 25 mm is named as shown in fig3.3. The tank named is of material GI & is the same used for water heater purpose in the home operation. 2.4.3 Thermocouple and Digital Temperature Indicator To record the colorful temperature of water inside the coil at colorful distances 5 Cr- Al thermocouples Fig - 3.3 Cylindrical tank
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1196 are named. To record the temperature, a digital temperature index as shown in fig3.4., of least count0.10 c and the range of 0- 5000 C is named. 2.4.4 Dimmerstat: A dimmerstat of range( 0- 1500 W) is named to fulfill the demand of varying heat input to assay the performance of heat transfer between water & colorful result as shown in fig3.5.. Fig - 3.5 Dimmerstat 2.4.5 Stirrer: For proper mixing of various solution & to increase the turbuance a stirrer is required. In this setup, a ¼ HP cooler motor pump of 1360 rpm is used as stirrer. 2.4.6 Flow Measuring Device: To measure the quantity of water flowing through the helical coil, a 1 lit glass measuring jar is used. 2.4.7 Heating Coil: A 1500-watt drum heating coil is used to heat the bath solution in the tank. Fig - 3.6 Photograph of Experimental Setup 2.5 Testing procedure: The convective heat transfer analysis of spiral coil is principally heat transfer between the bath liquid & fluid flowing through spiral coil i.e. water. The bath liquid used for the analysis purpose are water. To find out the colorful parameters needed for the analysis certain procedure must be espoused. So a testing procedure is designed and the same as followed during this trial. To avoid any leakages, originally a leak test of the experimental setup is assured at outside inflow rate of fluid. The testing procedure is listed as follows. 1. Fill the spherical tank with proper liquid(viz. watersuch that the entire setup of spiral coil immersed in liquid. 2. Acclimate the heat supplied to setup by duly conforming dimmer. Heat input should be recorded from the values of voltage and current. 3. Acclimate the inflow rate of water entering in spiral coil in a way to maintain constant inflow rate after enough heating of liquid. 4. Note down the colorful thermocouple reading with the help of temperature index at steady state. 5. Carry out the trial for the colorful values of heat input and by changing the mass inflow rate. 1. Instruments Used for Performance The colorful instruments used for testing purpose are as follows 1. Ammeter (0 – 10 A) 2. Voltmeter (0- 230 V) 3. Thermocouple Dimmer stat Dimmer Voltmeter Ammeter Temp Indicator Agitator Water inlet Water outlet Thermometer Measuring jar G.I. Vessel Dimmer stat Dimmer Voltmeter Ammeter Temp Indicator Agitator Water inlet Water outlet Thermometer Measuring jar G.I. Vessel Fig - 3.4 Digital temperature indicator
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1197 4. Measuring jar and stop watch( due to attainability of Rotameter) 5. Tachometer 3. RESULTS AND DISCUSSION The measure readings recorded in table 3.3 - 3.8 are used for calculation of heat transfer coefficient, over all heat transfer coefficient, the convective analysis governed with various non dimensional numbers and Nusselt number correlation. Depending upon the flow conditions the analysis requires numbers like Re number, Nusselt number, Pr number, De number.. 3.2 Calculation: 3.2.1 Calculation for Deciding Type of Flow : In helical coil flow of fluid is a function of Reynold number and Prandtl number. For deciding laminar and turbulent flow following equation are used (3), For laminar flow For turbulent flow, Sample calculation for water at head input 0.6 kw and mass flow rate of 5.75 gm/sec, Pr = 4.92 > 1 & Re= 0.621 > 0.4  Flow is turbulent 3.2.2 Calculation for Heat Transfer Coefficient: Heat transfer coefficient in helical coil is calculated by using equation are used (3), Sample calculation for water at heat input Qi = 0.6 kw and mass flow rate of 5.75 gm/sec, From equation 4.5, Pr = 4.92 Re = 1170 di = 8.04 mm De = 259 Nu = 13.74 Nu = Where, k = 0.626 W/m2 0k = Thermal conductivity which is taken from thermo physical properties of water at 34.50c (22)  hi = 1.069 Kw/m2 0k 3.2.3 Calculation for Over All Heat Transfer Coefficient : The overall heat transfer coefficient is calculated by using the relation stated as per (3) by equation Where, U – Overall heat transfer coefficient Q – Heat flow rate A – Area of the helical coil at outside Tb – Bath temperature Tm – Mean temperature of the helical coil Sample calculation for water at head input 0.6 kw and mass flow rate of 5.75 gm/sec, Appendix A-D shows the calculated values of Re number, Nu number, hi, and U for water for without agitation and with agitation at a different concentration. 4 CONCLUSION To analyses the convective heat transfer miracle in a spiral coil fluids like water is used during the trial. Water is used as a fluid flowing through spiral coil whereas fluid stated above are allowed to compass the entire spiral coil. Grounded on the trial the number of parameters is studied. On the base of below results and discussion following conclusion are drawn. ) 1 . 4 ...( ) ( 35 . 2 1 ) ( 364 . 0 2 1 2 1             De De A Nu ) 2 . 4 ...( } ) Re( 061 . 0 1 { ) ( Re Pr 41 1 6 1 5 . 2 12 1 6 5 4 . 0         c i c i D d D d x x Nu k d h i i k Kw/m 505 . 0 ) T T ( A Q U 0 2 m b    ) 3 . 4 ...( ) ( m b T T A Q U  
  • 6. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 09 Issue: 08 | Aug 2022 www.irjet.net p-ISSN: 2395-0072 © 2022, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 1198 REFERENCES [1] C.F.C. Rogers and Y.R. Mayhew “Heat Transfer and Pressure Loss in Helically Coiled Tubes With Turbulent Flow”, Int. Journal of Heat Mass Transfer, Vol – 7 PP 1207- 1216, 1964. [2] Venugopal Kabair and N.R. Kuloor “Heat Transfer to Newtonian Fluids in Coiled Pipe in a Laminar Flow”, Inst. Journal Heat and Mass Transfer Vol – 9, PP 69- 75, 1966 [3] Yasuo Mori and Wataru Nakayama “Study of Forced Convective Heat Transfer in Curved Pipes”, Inst. Journal Heat Mmass transfer Vol – 10 PP 681 – 695, 1967. [4] R. A. Seban and E.F. Mcloughlin “Heat Transfer In Tube Coils With Laminar And Turbulent Flow” Inst. J. Heat mass transfer Vol – 6 pp 387-395, 1963. [5] A. N. Dravid, K. A. Smith, E. W. Merill and P. L. T. Brain “Effect Of Secondary Fluid On Laminar Flow Heat Transfer In A Helically Coiled Tubes” Al. Chemical Engine Journal Vol 17, No 5 pp 1114- 1122 sept. 1971. [6] C.E. Kalb and J. D. Seadar, “Heat And Mass Transfer Phenomina For Vis Cous Flow In Curved Circular Tubes” Inst. J. Heat Mass transfer Vol 15, pp 801- 817, 1972. [7] S. Raja Sekaran, V. G. Kabair and N. R. Kuloor, “Secondary Flow Of Non – Newtanian Fluids In Helical Coils” Indian Journal of Technology, vol 4, Feb – 1966. [8] G.S. Arvind, Y. Aran, R. Sunder and S. Subrahmaniyan “Natural Convective Heat Transfer in Helically Coiled Heat Exchange” Vol 84, sept. 2003, I.E. (I) Journal [9] V.V. Sitram Murthy and R. C. Sastrey “Laminar Convective Heat Transfer And Viscous And Non Newtonian Liquids In Helically Coiled Tube” Indian Chemical Engineer Section A, Vol 42, No. 1. Jan – March 2000 [10] A. Ramasubramanian and S.K. Pandey “Agitation And Heat Transfer Studies In Suspension Transaction Of ASME, Vol 117, Feb 1995. [11] R.K. Prabhudesai and Shah “ Heat Transfer Though Helical Coils” traction of I.I. Ch.E. Vol. XII, 1959-60. [12] S. Manafzadeh, H.A. Simon and JCF chow “Heat Transfer Enhancement In Coiled Tubes” letters in heat and mass transfer, Vol – 9 PP 479-435, 1982. [13] S.N. Gupta and P. Mishra “Isothermal Laminar Flow of Non Newtonian Fluids Though Helical Coils” Indian Journal of technology, Vol 13, June 1975 PP 245-250. [14] Venugopal Kabair and N.R. Kuloor “Comparision Of Performance Of Helical And Spiral Coil Heat Exchange” and “Secondary Flow Of Non Newtonan Fluids In Helical Coils” Indian Journal of technology, Vol 4 Feb 1966. [15] D.G. Prabhajan, G.S. Paghavan and T.J. Renie “Comparison of Heat Transfer Rates Between A Straight Tube Heat Exchange And Helically Coiled Heat Exchange” [16] E. De maerteleire “Heat Transfer to A Helical Coil In Mechanically Agitauted Gas Ligit Dispersaion” chemical engg. Science Vol 33 PP 107-1113. 1978 [17] Shashi Krishna Pandey “Heat Transfer Studies For Agitated Liquits” CEW Vol XIII No. 9 Page 47-50, sept 1978. [18] Wang Kai and Yu shengyao, “Heat Transfer And Power Consumption Of Non – Newtanian Fluids In Agitated Vessels”, Chemical engineering science, Vol 44, No 1, PP 33-40, 1989. [19] S. Rajasekharan, V.G. Kubair and N. R. Kuloor “Heat Transfer To Non Newtonian Fluids In Coiled Pipes In Laminar Flow” Int. Journal of heat and mass transfer Vol 13 PP 1583-1594, 1970. [20] A.V. Kirpikov, “Heat Transfer In Helically Coiled Pipes,” Trudi moskov, first ktim, Moshinojtrojenija 12, 43-56 (1957) [21] James R. Lines ‘Hellically Coiler Heat Exchanges Offer Advantages Petroleum Enginner, April 1952. [22] S. Domkundwar, “Heat Transfer Data Book” Dhampat Rai publication New Delhi. [23] B.T. Najaguna, “Thermal Science Data Book”, Tata MaGraw-Hill Co. Ltd. , New Delhi.