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Nice Thomachan et al. Int. Journal of Engineering Research and Application www.ijera.com
Vol. 3, Issue 5, Sep-Oct 2013, pp.24-26
www.ijera.com 24 | P a g e
CFD Studies on Multi Lead Rifled [MLR] Boiler Tubes
Dr T C Mohankumar*, Nice Thomachan**
*(Professor, Department of Mechanical Engg MES College of Engg Kuttipuram, Kerala)
** (PG Scholar, MES College of Engineering, Kuttippuram, Kerala, University of Calicut)
ABSTRACT
This paper reports the merits of multi lead rifled [MLR] tubes in vertical water tube boiler using CFD tool. Heat
transfer enhancement of MLR tubes was mainly taken in to consideration. Performance of multi lead rifled tube
was studied by varying its influencing geometrical parameter like number of rifling, height of rifling, length of
pitch of rifling for a particular length. The heat transfer analysis was done at operating conditions of an actual
coal fired water tube boiler situated at Apollo Tyres LTD, Chalakudy, India for saturated process steam
production. The results showed that the heat transfer increased when compared with existing inner plane wall
water tubes.
Keywords - CFD, Coal fired water tube boiler, Geometrical parameters, Multi Lead Rifled [MLR] tube, Operating
conditions
I. INTRODUCTION
The increasing cost of energy in the past
years aroused the need for using more efficient energy
systems. This in turn encouraged researches in the
field of augmenting heat transfer in heat exchangers.
Several techniques were recognized for the study of
heat transfer enhancement; out of which, rifling is
found to be a powerful heat transfer enhancing tool. In
this study three main geometrical parameters of rifled
tubes are taken in to consideration. The three
parameters are number of rifling, height of rifling, and
length of pitch of rifling.
The influence of geometrical parameters are
depend upon the operating conditions means operating
pressure, temperature ,mass flow rate etc .So
optimization of the geometry used for a particular
operating condition is an important criteria for
improving heat transfer. In this study the heat transfer
of multi lead rifled boiler tube was analyzed with the
real operating conditions of a coal fired boiler which is
situated at Apollo Tyres LTD , Chalakudy,India,
where the steam produced at saturated condition for
the processing of vulcanization of rubber of
automobile tyres. In the real condition the boiler water
tubes are plane walled .So the optimized rifled
geometry performance was compared with the
performance of inner plane walled tube.The analysis
of the tube flow was done using Ansys 14 and
geometry and was modeled using Solid Works 2012
,meshing was done using Gmabit 2.4.6.Material
properties of steel and water was copied from the data
base of Ansys Fluent software.
II. PROBLEM SETUP AND MODELING
In this 3 dimensional CFD study a tube of
5.08 cm outer diameter with a thickness of 0.35 cm is
considered and the analysis was done for a length of
150 cm .Multi rifling is provided with three varying
parameters number of rifling, height of rifling, length
of pitch of rifling. Figure 1 shows the MLR tube
geometry. The boiler tube material is considered as
steel. The commercial CFD software employs a
control volume based technique to convert the
governing equations which are solved numerically
using the implicit method. In the segregated
formulation the governing equations are solved
sequentially, as it is segregated from one another.
Figure 1 Geometry
A 3D tube geometry with multi lead rifling is
considered. The mesh was created using GAMBIT
2.4.6.The tube geometry details and operating
conditions are given below. Mesh generation plays an
important role in obtaining accurate results. A
quadrilateral mesh was created uniformly throughout
RESEARCH ARTICLE OPEN ACCESS
Nice Thomachan et al. Int. Journal of Engineering Research and Application www.ijera.com
Vol. 3, Issue 5, Sep-Oct 2013, pp.24-26
www.ijera.com 25 | P a g e
the area and analyzed using FLUENT, ANSYS 14.5
package.
Number of rifling : 8
Height of rifling : 0.11cm
Length of pitch : 25.4 cm
Fig 2 Meshed Geometry
III. SIMULATION OF THERMAL
FLOW
3.1 COMPUTATIONAL DOMAIN WITH
BOUNDARY CONDITION
The flow and thermal variables are defined
by the following boundary conditions.
Working pressure : 22 kg/cm2
Inlet water Temperature : 450K
Outer wall Temperature : 1000K
Mass flow rate : 0.034 kg/sec
Saturation temperature : 490K
The solution convergence is obtained by
monitoring the continuity, momentum, energy,
turbulence and species equations separately Figure 4
shows the profile of temperature distribution of water
inside the tube. The temperature of the flue gas is 1000
K and heat transfer takes place to the water inside the
tubes. The temperature of the water inside the tube
reaches approximately 550 K. The temperature
distribution in the boiler tube is affected by many
variables such as mass flow rate of steam, steam
temperature, feed water temperature and pressure.
Therefore, effect of these variables is also considered
by running a limited number of simulations By using
the CFD simulation the result will contains the
enhanced heat transfer due to the increased wetted
perimeter of the boiler tube and some other effects due
to rifling. The main heat transfer enhancement in
actual case is due to the increased heat transfer area
and the enhanced contact of water to the tube wall.
During flow boiling wet steam generated will flow
through the water tube, may be in some region steam
may in contact with the tube wall, heat absorption
capacity of steam is poor when compared with water,
so sufficient tube cooling may not take place at that
region . In MLR tubes there will be a swirling flow
and that centrifugal force will separate steam and
water, denser water will be taken away to the wall
region by keeping less dense steam at the center
region. This effect of MLR boiler tube will make the
heat transfer more efficient than ordinary plane boiler
tube.
IV. RESULTS AND DISCUSSIONS
Enhancement in the heat transfer in boiler
furnace will reflect in the performance of the boiler. A
small increase in the heat transfer of the tube will
make huge change in the overall performance of the
boiler. The boiler which is studied having 332 vertical
tubes arranged from its bed coil to the top of the boiler
(steam drum) each tube having a height of 11.58
meters .Sample length is analyzed in the software and
the resultant temperature, enthalpy contours and plots
are shown below
Fig 3: Contours of Enthalpy
Fig 4: Contours of Temperature
Nice Thomachan et al. Int. Journal of Engineering Research and Application www.ijera.com
Vol. 3, Issue 5, Sep-Oct 2013, pp.24-26
www.ijera.com 26 | P a g e
Fig 5: Temperature V/S Time step
Fig 6: Enthalpy V/S Flow Time
Fig 7: Pressure V/S Time step
The figures shown above are the results that gained
after simulation of the geometry using the prescribed
inputs and flow conditions. Variation of temperature,
enthalpy, and pressure are shown above.
V. CONCLUSION
The model was created using Solid Works
2012 and meshed with Gambit, and the flow analysis
is done with Ansys 14. The results showing that the
heat transfer is increased. The enthalpy and
temperature increase with flow is advancing when
compare with normal boiler tube. So the
implementation of Optimized Multi Lead Rifled boiler
tube in this boiler is advisable. The study show that the
improvement in furnace heat transfer can be achieved
by changing the internal plane surface to a multi lead
rifled tube
VI. ACKNOLEDGEMENTS
The authors wish to acknowledge Apollo
Tyres Pvt Ltd, Chalakudy, Thrissur, Kerala, India for
their support and help given in the successful
completion of this project work. And Mr.C.G Vinod,
Manager of the firm for his great support.
REFERENCES
[1] D.K. McDonald et.al, Vertical Tube, Variable
Pressure Furnace for Super Critical Steam
Boilers, POWER-GEN International 2001
December 11-13, 2001
[2] Stephen J. Goidich et.al. Innovation in
Supercritical Boiler Technology, PowerGen
International Orlando, Florida, USA
December 2 – 4, 2008
[3] Sara Rainieri et.al. Experimental
Investigation of Heat Transfer and Pressure
Drop Augmentation for Laminar Flow in
Spirally Enhanced Tubes
[4] Shaji Kumar K.R et.al,, An Investigation on
Tube Temperature Distribution in a Water
Tube Boiler, IOSR Journal of Mechanical
and Civil Engineering ISSN: 2278-1684
Volume 2, Issue 3 (Sep-Oct. 2012), PP 45-50
[5] Lixin Cheng. et,al, Flow Boiling Heat
Transfer In Spirally Internally Ribbed Tube
,Heat And Mass Transfer 37(2001) 229-236
Springer-Verlag 2001
[6] J.Blazek," Computational Fluid Dynamics:
Principles and Applications", Elsevier
Science Ltd,2001,1-39
[7] Ajay N. Ingale, CFD Analysis Of Super
Heater In View Of Boiler tube Leakage
,International Journal of Engineering and
Innovative Technology (IJEIT) Volume 1,
Issue 3, March 2012, ISSN 2277-3754, page
29-31

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  • 1. Nice Thomachan et al. Int. Journal of Engineering Research and Application www.ijera.com Vol. 3, Issue 5, Sep-Oct 2013, pp.24-26 www.ijera.com 24 | P a g e CFD Studies on Multi Lead Rifled [MLR] Boiler Tubes Dr T C Mohankumar*, Nice Thomachan** *(Professor, Department of Mechanical Engg MES College of Engg Kuttipuram, Kerala) ** (PG Scholar, MES College of Engineering, Kuttippuram, Kerala, University of Calicut) ABSTRACT This paper reports the merits of multi lead rifled [MLR] tubes in vertical water tube boiler using CFD tool. Heat transfer enhancement of MLR tubes was mainly taken in to consideration. Performance of multi lead rifled tube was studied by varying its influencing geometrical parameter like number of rifling, height of rifling, length of pitch of rifling for a particular length. The heat transfer analysis was done at operating conditions of an actual coal fired water tube boiler situated at Apollo Tyres LTD, Chalakudy, India for saturated process steam production. The results showed that the heat transfer increased when compared with existing inner plane wall water tubes. Keywords - CFD, Coal fired water tube boiler, Geometrical parameters, Multi Lead Rifled [MLR] tube, Operating conditions I. INTRODUCTION The increasing cost of energy in the past years aroused the need for using more efficient energy systems. This in turn encouraged researches in the field of augmenting heat transfer in heat exchangers. Several techniques were recognized for the study of heat transfer enhancement; out of which, rifling is found to be a powerful heat transfer enhancing tool. In this study three main geometrical parameters of rifled tubes are taken in to consideration. The three parameters are number of rifling, height of rifling, and length of pitch of rifling. The influence of geometrical parameters are depend upon the operating conditions means operating pressure, temperature ,mass flow rate etc .So optimization of the geometry used for a particular operating condition is an important criteria for improving heat transfer. In this study the heat transfer of multi lead rifled boiler tube was analyzed with the real operating conditions of a coal fired boiler which is situated at Apollo Tyres LTD , Chalakudy,India, where the steam produced at saturated condition for the processing of vulcanization of rubber of automobile tyres. In the real condition the boiler water tubes are plane walled .So the optimized rifled geometry performance was compared with the performance of inner plane walled tube.The analysis of the tube flow was done using Ansys 14 and geometry and was modeled using Solid Works 2012 ,meshing was done using Gmabit 2.4.6.Material properties of steel and water was copied from the data base of Ansys Fluent software. II. PROBLEM SETUP AND MODELING In this 3 dimensional CFD study a tube of 5.08 cm outer diameter with a thickness of 0.35 cm is considered and the analysis was done for a length of 150 cm .Multi rifling is provided with three varying parameters number of rifling, height of rifling, length of pitch of rifling. Figure 1 shows the MLR tube geometry. The boiler tube material is considered as steel. The commercial CFD software employs a control volume based technique to convert the governing equations which are solved numerically using the implicit method. In the segregated formulation the governing equations are solved sequentially, as it is segregated from one another. Figure 1 Geometry A 3D tube geometry with multi lead rifling is considered. The mesh was created using GAMBIT 2.4.6.The tube geometry details and operating conditions are given below. Mesh generation plays an important role in obtaining accurate results. A quadrilateral mesh was created uniformly throughout RESEARCH ARTICLE OPEN ACCESS
  • 2. Nice Thomachan et al. Int. Journal of Engineering Research and Application www.ijera.com Vol. 3, Issue 5, Sep-Oct 2013, pp.24-26 www.ijera.com 25 | P a g e the area and analyzed using FLUENT, ANSYS 14.5 package. Number of rifling : 8 Height of rifling : 0.11cm Length of pitch : 25.4 cm Fig 2 Meshed Geometry III. SIMULATION OF THERMAL FLOW 3.1 COMPUTATIONAL DOMAIN WITH BOUNDARY CONDITION The flow and thermal variables are defined by the following boundary conditions. Working pressure : 22 kg/cm2 Inlet water Temperature : 450K Outer wall Temperature : 1000K Mass flow rate : 0.034 kg/sec Saturation temperature : 490K The solution convergence is obtained by monitoring the continuity, momentum, energy, turbulence and species equations separately Figure 4 shows the profile of temperature distribution of water inside the tube. The temperature of the flue gas is 1000 K and heat transfer takes place to the water inside the tubes. The temperature of the water inside the tube reaches approximately 550 K. The temperature distribution in the boiler tube is affected by many variables such as mass flow rate of steam, steam temperature, feed water temperature and pressure. Therefore, effect of these variables is also considered by running a limited number of simulations By using the CFD simulation the result will contains the enhanced heat transfer due to the increased wetted perimeter of the boiler tube and some other effects due to rifling. The main heat transfer enhancement in actual case is due to the increased heat transfer area and the enhanced contact of water to the tube wall. During flow boiling wet steam generated will flow through the water tube, may be in some region steam may in contact with the tube wall, heat absorption capacity of steam is poor when compared with water, so sufficient tube cooling may not take place at that region . In MLR tubes there will be a swirling flow and that centrifugal force will separate steam and water, denser water will be taken away to the wall region by keeping less dense steam at the center region. This effect of MLR boiler tube will make the heat transfer more efficient than ordinary plane boiler tube. IV. RESULTS AND DISCUSSIONS Enhancement in the heat transfer in boiler furnace will reflect in the performance of the boiler. A small increase in the heat transfer of the tube will make huge change in the overall performance of the boiler. The boiler which is studied having 332 vertical tubes arranged from its bed coil to the top of the boiler (steam drum) each tube having a height of 11.58 meters .Sample length is analyzed in the software and the resultant temperature, enthalpy contours and plots are shown below Fig 3: Contours of Enthalpy Fig 4: Contours of Temperature
  • 3. Nice Thomachan et al. Int. Journal of Engineering Research and Application www.ijera.com Vol. 3, Issue 5, Sep-Oct 2013, pp.24-26 www.ijera.com 26 | P a g e Fig 5: Temperature V/S Time step Fig 6: Enthalpy V/S Flow Time Fig 7: Pressure V/S Time step The figures shown above are the results that gained after simulation of the geometry using the prescribed inputs and flow conditions. Variation of temperature, enthalpy, and pressure are shown above. V. CONCLUSION The model was created using Solid Works 2012 and meshed with Gambit, and the flow analysis is done with Ansys 14. The results showing that the heat transfer is increased. The enthalpy and temperature increase with flow is advancing when compare with normal boiler tube. So the implementation of Optimized Multi Lead Rifled boiler tube in this boiler is advisable. The study show that the improvement in furnace heat transfer can be achieved by changing the internal plane surface to a multi lead rifled tube VI. ACKNOLEDGEMENTS The authors wish to acknowledge Apollo Tyres Pvt Ltd, Chalakudy, Thrissur, Kerala, India for their support and help given in the successful completion of this project work. And Mr.C.G Vinod, Manager of the firm for his great support. REFERENCES [1] D.K. McDonald et.al, Vertical Tube, Variable Pressure Furnace for Super Critical Steam Boilers, POWER-GEN International 2001 December 11-13, 2001 [2] Stephen J. Goidich et.al. Innovation in Supercritical Boiler Technology, PowerGen International Orlando, Florida, USA December 2 – 4, 2008 [3] Sara Rainieri et.al. Experimental Investigation of Heat Transfer and Pressure Drop Augmentation for Laminar Flow in Spirally Enhanced Tubes [4] Shaji Kumar K.R et.al,, An Investigation on Tube Temperature Distribution in a Water Tube Boiler, IOSR Journal of Mechanical and Civil Engineering ISSN: 2278-1684 Volume 2, Issue 3 (Sep-Oct. 2012), PP 45-50 [5] Lixin Cheng. et,al, Flow Boiling Heat Transfer In Spirally Internally Ribbed Tube ,Heat And Mass Transfer 37(2001) 229-236 Springer-Verlag 2001 [6] J.Blazek," Computational Fluid Dynamics: Principles and Applications", Elsevier Science Ltd,2001,1-39 [7] Ajay N. Ingale, CFD Analysis Of Super Heater In View Of Boiler tube Leakage ,International Journal of Engineering and Innovative Technology (IJEIT) Volume 1, Issue 3, March 2012, ISSN 2277-3754, page 29-31