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International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 290
CFD Analysis and Optimization of Heat Transfer Basket Element
Profiles of Ljungstrom Air Preheater (APH)
SRIKANTH1, Dr.M.C.NAVINDGI2
1Student of MTech (Thermal),Dept. of Mechanical Engineering, PDA College of Engineering, Kalaburagi,
Karnataka, India
2Professor, Dept. of Mechanical Engineering, PDA college of Engineering, Kalaburagi, Karnataka, India
---------------------------------------------------------------------***---------------------------------------------------------------------
Abstract - The Ljungstrom air preheater is one of the main
components in the coal fired power plant for the extraction of
the waste heat from the hot flue gases in order to increase the
plant efficiency. In this air preheater, element profiles are the
main component for heat exchange. At steady state, these
profiles are optimized and carried out CFD analysis on these
element profiles to check or to investigate the temperature
distribution between the hot flue gases and cold air at the low
effectiveness region of Ljungstrom Air preheater. The main
aim of this study is to find out the heat exchanging behavior of
element profiles and to find the outlet temperature ofboththe
air and flue gases in the low effectiveness region.
Key Words: CFD analysis, element profiles, solid works
1. INTRODUCTION
In most of the power plants, the Ljungstrom air preheater
(Fig.-1) is used to extract the waste heat from the hot flue
gases to preheat the cold air which is blown by the PA fans
and FD fans. The preheated air is utilized in the boiler
furnace for better combustion in order to increase the
combustion rate and increases the efficiency of the boiler
and thus it reduces the fuel consumption of the power plant.
This Ljungstrom air preheater is divided in to cold section
and hot section in which the hot flue gases will flow in the
hotter section and cold air will be flowing in cold section
and this air preheater consists of element profiles, rotor,
double seals, single seals, motorized motor to drivetheAPH,
speed controller, actuators etc,.
Fig.-1 Ljungstrom air preheater
The most important part of air preheater for the heat
exchange between both the fluids hot flue gases and cold air
is element profiles. When the air preheater is made to rotate
about 2-5 rpm by a rotor, the hot flue gaseswill flowoverthe
surface of these element profiles and is stored by these
profiles after some time the heated part will come in contact
with the cold air flow, thus the heat from the element
profiles is extracted by the cold air and this preheated air is
passed to the boiler furnace for complete combustion of the
powdered coal and thus it increases the thermal efficiency
and overall efficiency. These element profile materials are
made up of steel and steel alloys. In this study we used
corten steel as a material in which it is anti corrosive and
anti erosive and can withstand higher temperatures. Hence,
these material properties are suitable for experiment.
Assuming these profiles to be at steady state and at low
effectiveness region of Ljungstrom Air preheater (Fig.-2).
Fig.-2 Low effectiveness region of Ljungstrom Air
preheater
The CFD analysis is carried out by using the material
properties and air preheater data collected from the RTPS
210 MW power plant as boundary conditionsandappliedon
these element profiles and analyzed the results using Ansys
18.1 version.
2. HEAT TRANSFER ELEMENT PROFILES
The different heat transfer element profilesisthemain parts
of the ljungstrom air preheater and are as follows.
2.1 Notched Corrugated
This profile has lower thermal efficiency even though it is
used in all the coal fired based thermal powerplants(Fig.-3).
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 291
Fig.-3 Notched corrugated
2.4 Double undulated
This profile is inclined and notched geometry and used
mainly at intermediate and hot side portion of air preheater
basket matrix (Fig.-4).
Fig.-4 Double Undulated
2.5 Advanced Clear Element
This profile element profile helps in easycleaningofplugged
as by using soot blowers and this gives better performance
than the other profiles at low effectiveness region of air
preheater (Fig.-5).
Fig.-5 Advanced Clear Element
2.2 Notched Flat
This profile has lower pressure drop and has more thermal
efficiency. This type of profiles is used in lower plugging
applications such as oil and gas power plants. Since, it is
difficult to clean the plugged ash from the profile (Fig.-6).
Fig.-6 Notched Flat
2.1 Corrugated Undulated
This profile is used in the natural gas fired power plants and
these profiles is used for flue gases produced when fired
with natural gas (Fig.-7)
Fig-7 Corrugated undulated
3. EXPERIMENT MEASUREMENTS
The different heat transfer element profiles were
examined by using the specification of power plant,
specification ofLjungstromairpreheater,averagereadingsof
air preheater (Table 1) and properties of fluegases(Table2).
The specifications were listed below in the following.
Plant specifications are as follows:
 Capacity - 180 MW Unit
 Turbine - 3000 rpm
 Frequency – 49.59-50 Hz
 Power factor - 0.7-0.8
 Ambient temperature - 350C
Specifications of air preheater are as follows:
 Type - Ljungstrom air preheater
 Rotor rotation - 3 rpm
 Rotor diameter – 5-10 m
 Heating plate height- 800 mm
 Heating plate thickness – 0.60 mm
 Plate material - Corten steel
Table1: Average readings of Air preheater
Medium Inlet
temp.
Inlet
Pressure
Outlet
temp.
Outlet
pressure
Air 310K 2.054
kPa
560 K 1.735 kPa
Flue gas 574 K -0.5432
kPa
490 K -1.544
kPa
Table 2: Properties of Flue gases
Sr. No. Property Value
1. Density 0.623 kg/ m3
2. Specific heat (constant
pressure)
1.1796 kj/kgK
3. Thermal conductivity 0.04064 W/mK
4. Viscosity 0.023 Pas
5. Enthalpy 280.35 kj/kg
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 292
4. CFD ANALYSIS
The geometry of different element profiles was drawn and
modeling is done in solid works and these models were
imported in Ansys 18.1 fluent software and automatic
meshing is used, setup, steady state, energy equation, k- ε
turbulence model, boundary conditionsasmentioned below
CFD analysis is carried out by using the collected data from
210MW RTPS power plant as boundary conditions is listed
below in following (Table 3).
Table 3: Boundary conditions
Medium Inlet
temp.
Inlet
Pressure
Outlet
temp.
Outlet
pressure
Air 310K 2.0545
kPa
- 1.734 kPa
Flue gas 574 K -0.5431
kPa
- -1.5444
kPa
4. RESULTS AND DISCUSSIONS
A both experimental and analytical result shows that
there is a decrease in the flue gas outlet temperature [Chart.-
1] and increase in the air temperature [Chart.-2] which is
shown as below.
Chart.-1: Flue outlet
In this above, Chart.-1. It clearly shows that the
temperatures of different profiles at the low efficient region
of Ljungstrom Air-preheater. In these profiles from the CFD
analysisandoptimizedprofileNotchedCorrugated(NC)gives
lower flue outlet temperature than the otherprofiles.But,we
found that the Notched Corrugated (NC) outlet temperature
is slightly higher than the RTPS air preheater.
Chart.-2: Air outlet temperature vs Element profiles
In this above, Chart.-2. It clearly shows that the
temperatures of different profiles at the low efficient region
of Ljungstrom Air-preheater. In these profiles from the CFD
analysisandoptimizedprofileNotchedCorrugated(NC)gives
slightly lesser than Advanced Clear Element (ACE) profile.
But, on comparison with the Flue outlet temperature NC is
lesser than AdvancedClearElement(ACE)profile.Hence,this
Notched Corrugated (NC) profile is higher than RTPS air
preheater and this profile can be used in the low efficient
region forbetter efficiency orto improve the efficiency ofthe
air preheater and it also helps in easy cleansing of the
deposited ash.
Note: For easy comparison observe the first three bar
columns in chart.-1 and last three bar columns in chart.-2.
4.1 TEMPERATURE CONTOURS OF DIFFERENT PROFILE
The temperaturecontours ofdifferent profilesareshown
below from Fig.-8-12. These temperature contours shows
how the temperature variation takes place in the optimized
profiles of air preheater. The blue color shows the cold inlet
and red color shows the Flue inlet temperatures. The color
variation indicatesthetemperaturedistributionfromhotflue
gases to the cold air.
Fig-8: Temp. Contour for NC
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 293
Fig-9 Temp. Contour for DU
Fig-10 Temp. Contour for ACE
Fig-11: Temp. Contour for NF
Fig-12: Temp. Contour for CU
5. CONCLUSIONS
In this research work, “CFD analysis of Basket Element
profiles at Low Effectiveness Region of Ljungstrom Air
Preheater”.
1. Heat exchange andtemperaturedistributionofLjungstrom
air preheater mainly depends on the element profile.
2. From the CFD analysis and optimized profile Notched
Corrugated (NC) gives lowerflue outlet temperaturethan
the other profiles. But, we found that the Notched
Corrugated(NC)outlettemperatureisslightlyhigherthan
the average flue outlet temperatureofRTPSairpreheater.
3. From the CFD analysis and optimized profiles, air outlet
temperature of Notched Corrugated (NC) gives slightly
lesser temperature than Advanced Clear Element (ACE)
profile. But, on comparison with the Flue outlet
temperature Notched Corrugated (NC) is lesser than
Advanced Clear Element (ACE) profile. Hence, this
Notched Corrugated (NC) profile is higher than RTPS air
preheater.
In future, this study can be applied for different materials
and at different region of air preheater in order to increase
the efficiency of the air preheater.
REFERENCES
[1] T. Museet, the Ljungstrom Air Preheater 192, ASME
History, 1995.
[2] I. Warren, Ljungstrom heat exchangers for waste heat
recovery, Heat Recovery Syst.CHE2(3)(1982)257-271.
[3] Armin Heidari-Kaydan, Ebrahim Hajidavalloo, Three-
dimensional simulation of rotary air preheater in steam
power Plant, Applied Thermal Engineering 73 (2014)
399-407.
[4] Jonathan Dallaire a, Louis Gosselin a, Alexandre K. da
Silva, Conceptual optimizationofarotaryheatexchanger
with a porous core, International Journal of Thermal
Sciences 49 (2010) 454–462. 5.
[5] Sreedhar VullojuȦ,E.ManojKumarȦ,M.SureshKumarȦ
and K.Krishna Reddy Ḃ, Analysis of Performance of
Ljungstrom Air Preheater Elements, International
Journal of Current Engineering and Technology. 6.
[6] Sepehr Sanaye , Saeid Jafari, Hadi Ghaebi, Optimum
operational conditions of a rotary regenerator using
genetic algorithm, Energy and Buildings 40 (2008)
1637–1642. 7.
[7] Sandira ELJŠAN, Nikola STOŠIĆ, Ahmed KOVAČEVIĆ,
Indira BULJUBAŠIC Improvement of EnergyEfficiencyof
Coal- fired Steam Boilers by Optimizing Working
Parameters of Regenerative Air Preheaters, Researches
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 294
and Applications in Mechanical Engineering (RAME)
Volume 2 Issue 1, March 2013.
BIOGRAPHIES
SRIKANTH,MTech(Thermal Power
Engineering), Dept. of Mechanical
Engineering, PDA College of
Engineering, Kalaburagi-585102,
Karnataka, India.
Dr. M.C. NAVINDGI, Professor,
Dept. of Mechanical Engineering,
PDA College of Engineering,
Kalaburagi-585102, Karnataka,
India.

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IRJET- CFD Analysis and Optimization of Heat Transfer Basket Element Profiles of Ljungstrom Air Preheater (APH)

  • 1. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 290 CFD Analysis and Optimization of Heat Transfer Basket Element Profiles of Ljungstrom Air Preheater (APH) SRIKANTH1, Dr.M.C.NAVINDGI2 1Student of MTech (Thermal),Dept. of Mechanical Engineering, PDA College of Engineering, Kalaburagi, Karnataka, India 2Professor, Dept. of Mechanical Engineering, PDA college of Engineering, Kalaburagi, Karnataka, India ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract - The Ljungstrom air preheater is one of the main components in the coal fired power plant for the extraction of the waste heat from the hot flue gases in order to increase the plant efficiency. In this air preheater, element profiles are the main component for heat exchange. At steady state, these profiles are optimized and carried out CFD analysis on these element profiles to check or to investigate the temperature distribution between the hot flue gases and cold air at the low effectiveness region of Ljungstrom Air preheater. The main aim of this study is to find out the heat exchanging behavior of element profiles and to find the outlet temperature ofboththe air and flue gases in the low effectiveness region. Key Words: CFD analysis, element profiles, solid works 1. INTRODUCTION In most of the power plants, the Ljungstrom air preheater (Fig.-1) is used to extract the waste heat from the hot flue gases to preheat the cold air which is blown by the PA fans and FD fans. The preheated air is utilized in the boiler furnace for better combustion in order to increase the combustion rate and increases the efficiency of the boiler and thus it reduces the fuel consumption of the power plant. This Ljungstrom air preheater is divided in to cold section and hot section in which the hot flue gases will flow in the hotter section and cold air will be flowing in cold section and this air preheater consists of element profiles, rotor, double seals, single seals, motorized motor to drivetheAPH, speed controller, actuators etc,. Fig.-1 Ljungstrom air preheater The most important part of air preheater for the heat exchange between both the fluids hot flue gases and cold air is element profiles. When the air preheater is made to rotate about 2-5 rpm by a rotor, the hot flue gaseswill flowoverthe surface of these element profiles and is stored by these profiles after some time the heated part will come in contact with the cold air flow, thus the heat from the element profiles is extracted by the cold air and this preheated air is passed to the boiler furnace for complete combustion of the powdered coal and thus it increases the thermal efficiency and overall efficiency. These element profile materials are made up of steel and steel alloys. In this study we used corten steel as a material in which it is anti corrosive and anti erosive and can withstand higher temperatures. Hence, these material properties are suitable for experiment. Assuming these profiles to be at steady state and at low effectiveness region of Ljungstrom Air preheater (Fig.-2). Fig.-2 Low effectiveness region of Ljungstrom Air preheater The CFD analysis is carried out by using the material properties and air preheater data collected from the RTPS 210 MW power plant as boundary conditionsandappliedon these element profiles and analyzed the results using Ansys 18.1 version. 2. HEAT TRANSFER ELEMENT PROFILES The different heat transfer element profilesisthemain parts of the ljungstrom air preheater and are as follows. 2.1 Notched Corrugated This profile has lower thermal efficiency even though it is used in all the coal fired based thermal powerplants(Fig.-3).
  • 2. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 291 Fig.-3 Notched corrugated 2.4 Double undulated This profile is inclined and notched geometry and used mainly at intermediate and hot side portion of air preheater basket matrix (Fig.-4). Fig.-4 Double Undulated 2.5 Advanced Clear Element This profile element profile helps in easycleaningofplugged as by using soot blowers and this gives better performance than the other profiles at low effectiveness region of air preheater (Fig.-5). Fig.-5 Advanced Clear Element 2.2 Notched Flat This profile has lower pressure drop and has more thermal efficiency. This type of profiles is used in lower plugging applications such as oil and gas power plants. Since, it is difficult to clean the plugged ash from the profile (Fig.-6). Fig.-6 Notched Flat 2.1 Corrugated Undulated This profile is used in the natural gas fired power plants and these profiles is used for flue gases produced when fired with natural gas (Fig.-7) Fig-7 Corrugated undulated 3. EXPERIMENT MEASUREMENTS The different heat transfer element profiles were examined by using the specification of power plant, specification ofLjungstromairpreheater,averagereadingsof air preheater (Table 1) and properties of fluegases(Table2). The specifications were listed below in the following. Plant specifications are as follows:  Capacity - 180 MW Unit  Turbine - 3000 rpm  Frequency – 49.59-50 Hz  Power factor - 0.7-0.8  Ambient temperature - 350C Specifications of air preheater are as follows:  Type - Ljungstrom air preheater  Rotor rotation - 3 rpm  Rotor diameter – 5-10 m  Heating plate height- 800 mm  Heating plate thickness – 0.60 mm  Plate material - Corten steel Table1: Average readings of Air preheater Medium Inlet temp. Inlet Pressure Outlet temp. Outlet pressure Air 310K 2.054 kPa 560 K 1.735 kPa Flue gas 574 K -0.5432 kPa 490 K -1.544 kPa Table 2: Properties of Flue gases Sr. No. Property Value 1. Density 0.623 kg/ m3 2. Specific heat (constant pressure) 1.1796 kj/kgK 3. Thermal conductivity 0.04064 W/mK 4. Viscosity 0.023 Pas 5. Enthalpy 280.35 kj/kg
  • 3. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 292 4. CFD ANALYSIS The geometry of different element profiles was drawn and modeling is done in solid works and these models were imported in Ansys 18.1 fluent software and automatic meshing is used, setup, steady state, energy equation, k- ε turbulence model, boundary conditionsasmentioned below CFD analysis is carried out by using the collected data from 210MW RTPS power plant as boundary conditions is listed below in following (Table 3). Table 3: Boundary conditions Medium Inlet temp. Inlet Pressure Outlet temp. Outlet pressure Air 310K 2.0545 kPa - 1.734 kPa Flue gas 574 K -0.5431 kPa - -1.5444 kPa 4. RESULTS AND DISCUSSIONS A both experimental and analytical result shows that there is a decrease in the flue gas outlet temperature [Chart.- 1] and increase in the air temperature [Chart.-2] which is shown as below. Chart.-1: Flue outlet In this above, Chart.-1. It clearly shows that the temperatures of different profiles at the low efficient region of Ljungstrom Air-preheater. In these profiles from the CFD analysisandoptimizedprofileNotchedCorrugated(NC)gives lower flue outlet temperature than the otherprofiles.But,we found that the Notched Corrugated (NC) outlet temperature is slightly higher than the RTPS air preheater. Chart.-2: Air outlet temperature vs Element profiles In this above, Chart.-2. It clearly shows that the temperatures of different profiles at the low efficient region of Ljungstrom Air-preheater. In these profiles from the CFD analysisandoptimizedprofileNotchedCorrugated(NC)gives slightly lesser than Advanced Clear Element (ACE) profile. But, on comparison with the Flue outlet temperature NC is lesser than AdvancedClearElement(ACE)profile.Hence,this Notched Corrugated (NC) profile is higher than RTPS air preheater and this profile can be used in the low efficient region forbetter efficiency orto improve the efficiency ofthe air preheater and it also helps in easy cleansing of the deposited ash. Note: For easy comparison observe the first three bar columns in chart.-1 and last three bar columns in chart.-2. 4.1 TEMPERATURE CONTOURS OF DIFFERENT PROFILE The temperaturecontours ofdifferent profilesareshown below from Fig.-8-12. These temperature contours shows how the temperature variation takes place in the optimized profiles of air preheater. The blue color shows the cold inlet and red color shows the Flue inlet temperatures. The color variation indicatesthetemperaturedistributionfromhotflue gases to the cold air. Fig-8: Temp. Contour for NC
  • 4. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 293 Fig-9 Temp. Contour for DU Fig-10 Temp. Contour for ACE Fig-11: Temp. Contour for NF Fig-12: Temp. Contour for CU 5. CONCLUSIONS In this research work, “CFD analysis of Basket Element profiles at Low Effectiveness Region of Ljungstrom Air Preheater”. 1. Heat exchange andtemperaturedistributionofLjungstrom air preheater mainly depends on the element profile. 2. From the CFD analysis and optimized profile Notched Corrugated (NC) gives lowerflue outlet temperaturethan the other profiles. But, we found that the Notched Corrugated(NC)outlettemperatureisslightlyhigherthan the average flue outlet temperatureofRTPSairpreheater. 3. From the CFD analysis and optimized profiles, air outlet temperature of Notched Corrugated (NC) gives slightly lesser temperature than Advanced Clear Element (ACE) profile. But, on comparison with the Flue outlet temperature Notched Corrugated (NC) is lesser than Advanced Clear Element (ACE) profile. Hence, this Notched Corrugated (NC) profile is higher than RTPS air preheater. In future, this study can be applied for different materials and at different region of air preheater in order to increase the efficiency of the air preheater. REFERENCES [1] T. Museet, the Ljungstrom Air Preheater 192, ASME History, 1995. [2] I. Warren, Ljungstrom heat exchangers for waste heat recovery, Heat Recovery Syst.CHE2(3)(1982)257-271. [3] Armin Heidari-Kaydan, Ebrahim Hajidavalloo, Three- dimensional simulation of rotary air preheater in steam power Plant, Applied Thermal Engineering 73 (2014) 399-407. [4] Jonathan Dallaire a, Louis Gosselin a, Alexandre K. da Silva, Conceptual optimizationofarotaryheatexchanger with a porous core, International Journal of Thermal Sciences 49 (2010) 454–462. 5. [5] Sreedhar VullojuȦ,E.ManojKumarȦ,M.SureshKumarȦ and K.Krishna Reddy Ḃ, Analysis of Performance of Ljungstrom Air Preheater Elements, International Journal of Current Engineering and Technology. 6. [6] Sepehr Sanaye , Saeid Jafari, Hadi Ghaebi, Optimum operational conditions of a rotary regenerator using genetic algorithm, Energy and Buildings 40 (2008) 1637–1642. 7. [7] Sandira ELJŠAN, Nikola STOŠIĆ, Ahmed KOVAČEVIĆ, Indira BULJUBAŠIC Improvement of EnergyEfficiencyof Coal- fired Steam Boilers by Optimizing Working Parameters of Regenerative Air Preheaters, Researches
  • 5. International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 294 and Applications in Mechanical Engineering (RAME) Volume 2 Issue 1, March 2013. BIOGRAPHIES SRIKANTH,MTech(Thermal Power Engineering), Dept. of Mechanical Engineering, PDA College of Engineering, Kalaburagi-585102, Karnataka, India. Dr. M.C. NAVINDGI, Professor, Dept. of Mechanical Engineering, PDA College of Engineering, Kalaburagi-585102, Karnataka, India.