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Reticom Solutions
Measure, Monitor, Manage
2455 Wyandotte St West , Windsor, ON, Canada N9B0C1
Tel: (226) 344-7809 Fax: (519) 253-3000
www.reticom.ca mkarami@reticom.ca
COMPUTATIONAL FLUID DYNAMICS
ENGINEERING SERVICES FOR CFD PROJECTS
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
INDUSTRIES
 Oil & Gas
 Power Plant
 Automotive
 Aerospace
 Renewable Energy
 Environmental
 Electronic Cooling
 Ventilation
 Biomedical
 Manufacturing
2
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
CFD AREAS
 Turbulence Modeling
 Large Eddy Simulations
 Heat Exchangers
 Combustion & Reacting Flows
 Multiphase Flows
 Compressible Flows
 Moving Mesh Applications
 Turbomachinery
 Mathematical Model Development
 User-Defined Functions (UDFs)
 Geometry Optimization
 Mesh Generation
 Advanced Post Processing
 Reverse Engineering
 Flow-Solid Interaction
 Aeroacoustics & Noise
3
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
PROJECT SAMPLES
 Duct burner design (for 20 different plants)
 Design of stand-alone HRSG (working with both gas turbine AND
fresh air)
 Burner modification for under-operation plants (7 different cases)
 High-fidelity heat transfer analysis
 Investigation of burner element performance (R&D and Reverse
Engineering)
 Conjugate heat transfer of boiler tubes
 Analysis of FAC (FlowAccelerated Corrosion) risk using CFD
simulations
 Flow distribution in headers and tubes
 Ventilation of urban traffic tunnels
 Temperature rise in human head due to cellphone
4
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DUCT BURNER DESIGN
 Duct burner is installed at inlet duct of HRSG to increase the
temperature of flue gas before entering the heat exchangers.
 Challenges and Issues
 Flame stability
 Preventing reverse-flame
 Proper flame direction
 Protecting burner from hot gases
 Protecting boiler tubes from hot spots
 Limiting pressure loss if flue gas side
 Flow & temperature uniformity at the cross sections of heat
exchangers
5
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DUCT BURNER DESIGN
 SAMPLE-1
 Gas turbine:SiemensV9.2
 Burner capacity: 10 MW
 # Burner Rows: 1
6
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DUCT BURNER DESIGN
 SAMPLE-2
 Gas turbine:SiemensV9.2
 Burner capacity: 30 MW
 # Burner Rows: 2
7
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DUCT BURNER DESIGN
 SAMPLE-3
 Gas turbine:SiemensV9.2
 Burner capacity: 42 MW
 # Burner Rows: 3
8
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DUCT BURNER DESIGN
 SAMPLE-4
 Gas turbine:GE 9E
 Burner capacity: 40 MW
 # Burner Rows: 3
9
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DUCT BURNER DESIGN
 SAMPLE-5
 Gas turbine:AnsaldoV94.2
 Burner capacity: 110 MW
 # Burner Rows: 9
 Challenges
 Heavy duty burner
 Limited space for boiler
 Need to shorten inlet duct
 Uniform temperature distribution
after burner is critical.
10
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DESIGN OF STAND-ALONE HRSG
 Stand-alone HRSG is a special type of steam generator that
can produce steam either with turbine exhaust gas (TEG) or
fresh air.The design of burner and flow guide vanes is critical
due to complexity of geometry.
 Challenges and Issues (in addition to those of ordinary duct
burners)
 90-degree turning in flow direction
 Burner configuration should be robust and reliable for both TEG
and fresh air flows.
 Different design criteria for bothTEG and fresh-air firing
 More restricted limitation for gas-side pressure drop
 High capacity burner required for fresh air mode
11
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DESIGN OF STAND-ALONE HRSG
 Gas turbine:Zorya UGT-25000
 Burner capacity in TEG mode: 4 MW
 Burner capacity in Fresh air mode: 44 MW
 # Burner Rows: 4
 HRSG application: Desalination
12
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DESIGN OF STAND-ALONE HRSG
 Challenges
 Providing uniform flow over burners for both modes:
TEG mode and fresh air mode
13
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DESIGN OF STAND-ALONE HRSG
 Challenges
 Providing uniform flow over burners for both modes:
TEG mode and fresh air mode
SideView
TopView
14
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
DESIGN OF STAND-ALONE HRSG
 Challenges
 Providing uniform temperature over superheater tubes
 Appropriate flame direction
15
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
BURNER MODIFICATION FOR UNDER-OPERATION PLANTS
 SAMPLE-1
 Detection and removing huge recirculation zone
around the highest row of a 4-row burner
Recirculation Zone
16
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
BURNER MODIFICATION FOR UNDER-OPERATION PLANTS
 SAMPLE-1
 Detection and removing huge recirculation zone
around the highest row of a 4-row burner
Reverse Flame Region
17
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
BURNER MODIFICATION FOR UNDER-OPERATION PLANTS
Before
Modification
After
Modification
Hot spot on burner
Recirculation Zone
 SAMPLE-2
 Detection and removing
partial reverse-flame region
on the top of burner
18
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
BURNER MODIFICATION FOR UNDER-OPERATION PLANTS
Before
Modification
After
Modification
 SAMPLE-3
 Detection and removing partial reverse-flame
region on the top of burner
 Modification of flow direction by easily-done
suggestion
19
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
HIGH-FIDELITY HEAT TRANSFER ANALYSIS
 An INOVATIVE approach to implement heat exchanger
concept in CFD solver to reach the EXACT distribution of
temperature for metal and water/steam with reasonable
computational cost
 Reduction of design risk
 Reduction of unnecessary margins
 Better estimation of metal temperature
 Detecting and removing local hot-spots
 Accuracy in computing thermal stresses
20
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
HIGH-FIDELITY HEAT TRANSFER ANALYSIS
 It is impossible to model all finned tubes of
heat exchangers in CFD simulation due to
the limitations in computational sources. By
applying high-fidelity approach, the
distribution of temperature for fin and tubes
will be estimated accurately.
 Useful to study heat transfer behavior of
flow with high degree of non-uniformity in
velocity and temperature
 Applicable to estimate the thermal
performance of furnaces with complex tube
arrangement
Temperature Distribution of
Flue Gas at the Cross
Section
21
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
HIGH-FIDELITY HEAT TRANSFER ANALYSIS
FinTipTemperatureTube MetalTemperatureSteamTemperature
22
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
INVESTIGATION OF BURNER ELEMENT PERFORMANCE
 An R&D project to evaluate different burners in
variety of operating conditions and estimate their
performance according to following terms:
 Flame Stability
 Burner capacity
 Aerodynamics
 Flame shape & length
 Protection of burner material
against flame temperature
23
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
INVESTIGATION OF BURNER ELEMENT PERFORMANCE
24
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
INVESTIGATION OF BURNER ELEMENT PERFORMANCE
 Aerodynamics of bluff-body
configurations
 Temperature distribution on
burner metal
 Flame stability
 Mixing performance
25
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
INVESTIGATION OF BURNER ELEMENT PERFORMANCE
 Flame shape
 Flame length
 Temperature distribution
downstream the burner
26
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
CONJUGATE HEAT TRANSFER OF BOILER TUBES
 Combination of conduction/convection heat
transfer
 Transient heat transfer in tubes & headers
 Stress analysis of pressure parts
27
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
ANALYSIS OF FAC RISK USING CFD SIMULATIONS
 Investigation of FAC (Flow Accelerated Corrosion)
risk in tubes regarding the water chemistry,
temperature and flow
 Calculation of fluid velocity in all branches for all
operating conditions to be sure about meeting the
criteria
 Performing CFD to find out possible regions which
are locally susceptible to FAC
28
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
FLOW DISTRIBUTION IN HEADERS AND TUBES
 CFD simulation of water/steam distribution in
boiler headers and tubes
 Consideration of variable heat absorption in
different tubes
 Modification of tube arrangement to reach
required flow homogeneity
29
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
VENTILATION OF URBAN TRAFFIC TUNNELS
30
 CFD simulation of pollutant
dispersion in urban traffic
tunnel
 Design and Optimization of
ventilation system
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
VENTILATION OF URBAN TRAFFIC TUNNELS
 Evaluation of different ventilation system
design to reach the maximum efficiency
31
RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca
TEMPERATURE RISE IN HUMAN HEAD DUE TO CELLPHONE
 Simulation of cell-phone electromagnetic waves effects on the
temperature rise in brain
 Evaluation of SAR in human head
 Engaging Pennes’ bioheat transfer equation to calculate the
temperature distribution inside human head due to the electromagnetic
waves of cellphone
32
RETICOM SOLUTIONS www.reticom.ca info@reticom.ca
Reticom Solutions
Measure, Monitor, Manage
2455 Wyandotte St West , Windsor, ON, Canada N9B0C1
Tel: (226) 344-7809 Fax: (519) 253-3000

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CFD Engineering Services

  • 1. Reticom Solutions Measure, Monitor, Manage 2455 Wyandotte St West , Windsor, ON, Canada N9B0C1 Tel: (226) 344-7809 Fax: (519) 253-3000 www.reticom.ca mkarami@reticom.ca COMPUTATIONAL FLUID DYNAMICS ENGINEERING SERVICES FOR CFD PROJECTS
  • 2. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca INDUSTRIES  Oil & Gas  Power Plant  Automotive  Aerospace  Renewable Energy  Environmental  Electronic Cooling  Ventilation  Biomedical  Manufacturing 2
  • 3. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca CFD AREAS  Turbulence Modeling  Large Eddy Simulations  Heat Exchangers  Combustion & Reacting Flows  Multiphase Flows  Compressible Flows  Moving Mesh Applications  Turbomachinery  Mathematical Model Development  User-Defined Functions (UDFs)  Geometry Optimization  Mesh Generation  Advanced Post Processing  Reverse Engineering  Flow-Solid Interaction  Aeroacoustics & Noise 3
  • 4. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca PROJECT SAMPLES  Duct burner design (for 20 different plants)  Design of stand-alone HRSG (working with both gas turbine AND fresh air)  Burner modification for under-operation plants (7 different cases)  High-fidelity heat transfer analysis  Investigation of burner element performance (R&D and Reverse Engineering)  Conjugate heat transfer of boiler tubes  Analysis of FAC (FlowAccelerated Corrosion) risk using CFD simulations  Flow distribution in headers and tubes  Ventilation of urban traffic tunnels  Temperature rise in human head due to cellphone 4
  • 5. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DUCT BURNER DESIGN  Duct burner is installed at inlet duct of HRSG to increase the temperature of flue gas before entering the heat exchangers.  Challenges and Issues  Flame stability  Preventing reverse-flame  Proper flame direction  Protecting burner from hot gases  Protecting boiler tubes from hot spots  Limiting pressure loss if flue gas side  Flow & temperature uniformity at the cross sections of heat exchangers 5
  • 6. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DUCT BURNER DESIGN  SAMPLE-1  Gas turbine:SiemensV9.2  Burner capacity: 10 MW  # Burner Rows: 1 6
  • 7. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DUCT BURNER DESIGN  SAMPLE-2  Gas turbine:SiemensV9.2  Burner capacity: 30 MW  # Burner Rows: 2 7
  • 8. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DUCT BURNER DESIGN  SAMPLE-3  Gas turbine:SiemensV9.2  Burner capacity: 42 MW  # Burner Rows: 3 8
  • 9. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DUCT BURNER DESIGN  SAMPLE-4  Gas turbine:GE 9E  Burner capacity: 40 MW  # Burner Rows: 3 9
  • 10. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DUCT BURNER DESIGN  SAMPLE-5  Gas turbine:AnsaldoV94.2  Burner capacity: 110 MW  # Burner Rows: 9  Challenges  Heavy duty burner  Limited space for boiler  Need to shorten inlet duct  Uniform temperature distribution after burner is critical. 10
  • 11. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DESIGN OF STAND-ALONE HRSG  Stand-alone HRSG is a special type of steam generator that can produce steam either with turbine exhaust gas (TEG) or fresh air.The design of burner and flow guide vanes is critical due to complexity of geometry.  Challenges and Issues (in addition to those of ordinary duct burners)  90-degree turning in flow direction  Burner configuration should be robust and reliable for both TEG and fresh air flows.  Different design criteria for bothTEG and fresh-air firing  More restricted limitation for gas-side pressure drop  High capacity burner required for fresh air mode 11
  • 12. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DESIGN OF STAND-ALONE HRSG  Gas turbine:Zorya UGT-25000  Burner capacity in TEG mode: 4 MW  Burner capacity in Fresh air mode: 44 MW  # Burner Rows: 4  HRSG application: Desalination 12
  • 13. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DESIGN OF STAND-ALONE HRSG  Challenges  Providing uniform flow over burners for both modes: TEG mode and fresh air mode 13
  • 14. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DESIGN OF STAND-ALONE HRSG  Challenges  Providing uniform flow over burners for both modes: TEG mode and fresh air mode SideView TopView 14
  • 15. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca DESIGN OF STAND-ALONE HRSG  Challenges  Providing uniform temperature over superheater tubes  Appropriate flame direction 15
  • 16. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca BURNER MODIFICATION FOR UNDER-OPERATION PLANTS  SAMPLE-1  Detection and removing huge recirculation zone around the highest row of a 4-row burner Recirculation Zone 16
  • 17. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca BURNER MODIFICATION FOR UNDER-OPERATION PLANTS  SAMPLE-1  Detection and removing huge recirculation zone around the highest row of a 4-row burner Reverse Flame Region 17
  • 18. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca BURNER MODIFICATION FOR UNDER-OPERATION PLANTS Before Modification After Modification Hot spot on burner Recirculation Zone  SAMPLE-2  Detection and removing partial reverse-flame region on the top of burner 18
  • 19. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca BURNER MODIFICATION FOR UNDER-OPERATION PLANTS Before Modification After Modification  SAMPLE-3  Detection and removing partial reverse-flame region on the top of burner  Modification of flow direction by easily-done suggestion 19
  • 20. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca HIGH-FIDELITY HEAT TRANSFER ANALYSIS  An INOVATIVE approach to implement heat exchanger concept in CFD solver to reach the EXACT distribution of temperature for metal and water/steam with reasonable computational cost  Reduction of design risk  Reduction of unnecessary margins  Better estimation of metal temperature  Detecting and removing local hot-spots  Accuracy in computing thermal stresses 20
  • 21. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca HIGH-FIDELITY HEAT TRANSFER ANALYSIS  It is impossible to model all finned tubes of heat exchangers in CFD simulation due to the limitations in computational sources. By applying high-fidelity approach, the distribution of temperature for fin and tubes will be estimated accurately.  Useful to study heat transfer behavior of flow with high degree of non-uniformity in velocity and temperature  Applicable to estimate the thermal performance of furnaces with complex tube arrangement Temperature Distribution of Flue Gas at the Cross Section 21
  • 22. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca HIGH-FIDELITY HEAT TRANSFER ANALYSIS FinTipTemperatureTube MetalTemperatureSteamTemperature 22
  • 23. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca INVESTIGATION OF BURNER ELEMENT PERFORMANCE  An R&D project to evaluate different burners in variety of operating conditions and estimate their performance according to following terms:  Flame Stability  Burner capacity  Aerodynamics  Flame shape & length  Protection of burner material against flame temperature 23
  • 24. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca INVESTIGATION OF BURNER ELEMENT PERFORMANCE 24
  • 25. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca INVESTIGATION OF BURNER ELEMENT PERFORMANCE  Aerodynamics of bluff-body configurations  Temperature distribution on burner metal  Flame stability  Mixing performance 25
  • 26. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca INVESTIGATION OF BURNER ELEMENT PERFORMANCE  Flame shape  Flame length  Temperature distribution downstream the burner 26
  • 27. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca CONJUGATE HEAT TRANSFER OF BOILER TUBES  Combination of conduction/convection heat transfer  Transient heat transfer in tubes & headers  Stress analysis of pressure parts 27
  • 28. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca ANALYSIS OF FAC RISK USING CFD SIMULATIONS  Investigation of FAC (Flow Accelerated Corrosion) risk in tubes regarding the water chemistry, temperature and flow  Calculation of fluid velocity in all branches for all operating conditions to be sure about meeting the criteria  Performing CFD to find out possible regions which are locally susceptible to FAC 28
  • 29. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca FLOW DISTRIBUTION IN HEADERS AND TUBES  CFD simulation of water/steam distribution in boiler headers and tubes  Consideration of variable heat absorption in different tubes  Modification of tube arrangement to reach required flow homogeneity 29
  • 30. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca VENTILATION OF URBAN TRAFFIC TUNNELS 30  CFD simulation of pollutant dispersion in urban traffic tunnel  Design and Optimization of ventilation system
  • 31. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca VENTILATION OF URBAN TRAFFIC TUNNELS  Evaluation of different ventilation system design to reach the maximum efficiency 31
  • 32. RETICOM SOLUTIONS www.reticom.ca mkarami@reticom.ca TEMPERATURE RISE IN HUMAN HEAD DUE TO CELLPHONE  Simulation of cell-phone electromagnetic waves effects on the temperature rise in brain  Evaluation of SAR in human head  Engaging Pennes’ bioheat transfer equation to calculate the temperature distribution inside human head due to the electromagnetic waves of cellphone 32
  • 33. RETICOM SOLUTIONS www.reticom.ca info@reticom.ca Reticom Solutions Measure, Monitor, Manage 2455 Wyandotte St West , Windsor, ON, Canada N9B0C1 Tel: (226) 344-7809 Fax: (519) 253-3000