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Optimization of Energy Pile Conductance
using Finite Element and Fractional Factorial
Design of Experiment
Dr. Khaled Ahmed
Mechanical & Industrial Engineering Department,
Qatar University,
Doha, Qatar.
Dr. Mohammed Al-Khawaja
Mechanical & Industrial Engineering Department,
Qatar University,
Doha, Qatar.
Dr. Muhannad Suleiman
Civil and Environmental Engineering,
Lehigh University,
Bethlehem, PA, USA.
2017 International Joint Conference on Civil and Mechanical Engineering
JCCME 2017
Outline
2
Dr. Khaled Ahmed
 Introduction
οƒ˜ Review
οƒ˜ Problem Statement
οƒ˜ Objectives
 Finite Element Model
 Controlling Factors
 Design of Experiment
 Results & Discussion
 Conclusions
Introduction
3
Dr. Khaled Ahmed
 Review
 Cooling Buildings with AC is increasing
Introduction
4
Dr. Khaled Ahmed
 Review
 GSHP, Ground Source Heat Pump
Introduction
5
Dr. Khaled Ahmed
 Review
 Wellbores
Introduction
6
Dr. Khaled Ahmed
 Review
 Energy Piles work as heat
exchangers
Introduction
7
Dr. Khaled Ahmed
 Review
 Energy Piles has three materials and 5 geometrical factors.
1 U-tube 2 U-tubes 3 U-tubes
Introduction
8
Dr. Khaled Ahmed
 Problem Statement
 Energy Piles has many controlling factors ( >> 5).
 Interaction between these factors is missed.
 Optimization based on all possible factors is missed.
 Proper design of experiment is required.
Introduction
9
Dr. Khaled Ahmed
 Objectives
 Use well verified finite element model.
 Define wide range of possible controlling factors.
 Define design of experiment considering all factors.
 Predict a statistical correlation between factors.
 Predict statistically the optimum controlling factors.
Finite Element Model
10
Dr. Khaled Ahmed
 Geometrical Model
 Symmetrical Pattern
Finite Element Model
11
Dr. Khaled Ahmed
 Energy Balance using Galerkin Method
 Boundary Conditions
 Post Analysis
𝐡 𝑇
𝐾 𝐡 𝑑𝐴
𝐴
+ β„Ž 𝑁𝑠 𝑇
𝑁𝑠
𝑑𝑆
𝑆
𝑇 = π‘žπ‘ 
𝑁𝑠 𝑇
𝑑𝑆
𝑆
+ β„Žπ‘‡π‘“ 𝑁𝑠 𝑇
𝑑𝑆
𝑆
𝛛𝐓
𝛛𝐒
= 𝟎
π‘»π€βˆ’π = πŸπŸ“ 𝐨
𝐂
βˆ’πŠπ¬
𝛛𝐓
𝛛𝐒
= 𝐇 𝐓𝐬 βˆ’ π“πŸ
π‘ͺ𝐩,𝐅𝐄 =
ππ€βˆ’π
𝐓𝐭 βˆ’ π“π‚βˆ’πƒ
FE Model Verification
12
Dr. Khaled Ahmed
 Mesh Density Sensitivity.
𝑅𝑝 =
1
4πœ‹πΎπ‘
ln
𝑑𝑝
4
4π‘‘π‘œπ‘†3
𝑑𝑝
8
𝑑𝑝
8
βˆ’ 𝑆8
πΎπ‘βˆ’πΎπ‘ 
𝐾𝑝+𝐾𝑠
+
1
2π‘›πœ‹
1
2𝐾𝑑
ln
π‘‘π‘œ
𝑑𝑖
+
1
𝑑𝑖𝐻 𝑑
Controlling Factors
13
Dr. Khaled Ahmed
 Geometrical Factors
 n: Number of U-tubes
 dp [m]: Pile diameter.
 di [m]: Tube inner diameter
 t [m]: Tube thickness
 S [m]: Tubes spacing.
 Physical Factors
 Kp [W/m.K]: Pile thermal conductivity.
 Ks [W/m.K]: Soil thermal conductivity.
 Kt [W/m.K]: Tube thermal conductivity.
 Operational Factors
 H [W/m2.K]: Convection heat transfer coefficient.
9
Factors
Controlling Factors
14
Dr. Khaled Ahmed
 Factors Range
n
dp
[m]
di
[m]
t
[m]
S
[m]
Kp
[W/m.K]
Ks
[W/m.K]
Kt
[W/m.K]
H
[W/m2.K]
-1 1 0.4 0.02 0.002 0.4 dp 1.0 0.5 0.5 10
0 2 0.7 0.03 0.003 0.6 dp 1.75 1 16 55
+1 3 1.0 0.04 0.004 0.8 dp 2.25 1.5 32 100
Design of Experiment
15
Dr. Khaled Ahmed
 Taguchi Design
 Minimum number of experiments.
 Works fine with small number of factors.
 Linear correlation.
 Box-Behnken Design
 Large number of experiments.
 Works fine with up to 7 factors.
 Quadratic correlation.
 Uniform Design
 Offer wide range of number of experiments
 Works fine with large number of factors.
 Quadratic correlation using step regression.
Taguchi
Box-Behnken
Uniform
Design of Experiment
16
Dr. Khaled Ahmed
 Uniform Design
 Choosing number of experiments
U
27
(3
9
)
U
36
(3
9
)
U
51
(3
9
)
Fang et a., Number-theoretic methods in statistics, CRC Press, 1993.
Design of Experiment
17
Dr. Khaled Ahmed
 Uniform Design Tables
Fang et a., Number-theoretic methods in statistics, CRC Press, 1993.
n dp di t S Kp Ks Kt H
Conductance
1/Rp
1 1 1 1 1 1 0 -1 -1 1 7.84
2 0 1 -1 0 1 -1 0 1 1 2.27
3 1 -1 1 1 -1 0 1 0 0 4.64
4 0 -1 1 -1 0 1 -1 -1 -1 3.05
5 -1 0 0 1 1 -1 1 0 1 1.86
6 -1 1 0 1 0 -1 1 1 0 1.38
7 1 0 0 -1 -1 1 1 -1 1 5.17
8 0 0 0 0 0 0 0 0 0 3.22
9 0 0 0 1 1 -1 -1 -1 0 2.93
10 0 1 -1 -1 0 1 1 0 1 2.70
11 0 1 0 1 -1 1 -1 0 -1 1.90
12 0 1 1 0 -1 -1 1 -1 1 2.86
13 1 1 0 1 1 1 0 1 0 5.37
14 0 0 0 0 0 0 0 0 0 3.22
15 -1 0 0 1 -1 0 0 -1 -1 0.96
16 -1 -1 1 0 1 1 1 0 1 3.67
17 1 1 1 0 0 1 0 0 0 6.42
18 0 0 1 1 1 1 1 0 -1 3.10
19 0 -1 0 0 0 0 0 -1 1 4.23
20 1 -1 0 0 -1 -1 -1 0 1 3.12
21 1 0 1 -1 0 -1 0 0 1 5.26
22 -1 0 -1 0 -1 1 1 1 0 1.00
23 1 0 -1 -1 1 1 -1 0 0 3.05
24 -1 0 -1 -1 0 -1 -1 -1 1 1.10
25 -1 1 1 0 1 -1 -1 0 -1 1.25
26 -1 0 1 1 0 1 -1 1 1 3.31
27 -1 1 -1 0 1 1 0 -1 -1 0.55
Results & Discussion
18
Dr. Khaled Ahmed
 Signal to Noise Ratio
𝑆 𝑁 = βˆ’10 log10
1
π‘š
𝑖=1
π‘š
𝑅𝑝,𝑖
2
Results & Discussion
19
Dr. Khaled Ahmed
 Cubic Regression
π‘Œ
= π‘Ž0 +
π‘˜=1
9
π‘Žπ‘˜π‘₯π‘˜
+
𝑖=1
9
𝑗=𝑖
9
𝑏𝑖𝑗π‘₯𝑖π‘₯𝑗
+
𝑖=1
9
𝑗=𝑖
9
π‘˜=𝑗
9
π‘π‘–π‘—π‘˜π‘₯𝑖π‘₯𝑗π‘₯π‘˜
Results & Discussion
20
Dr. Khaled Ahmed
 Maximum Conductance
U27(39) U36(39) U51(39) Optimum
Number of Tubes ( n ) +1 +1 0 +1
Pile Diameter ( dp ) -1 +1 -1 -1
Tube Inner Diameter ( di ) +1 0 0 +1
Tube Thickness ( t ) -1 -1 -1 0
Distance between Tubes ( S ) +1 +1 +1 +1
Pile Thermal Conductivity ( Kp ) +1 +1 +1 +1
Ground Thermal Conductivity ( Ks ) -1 0 -1 0
Tube thermal Conductivity ( Kt ) 0 0 +1 +1
Heat Transfer Coefficient ( H ) 0 +1 +1 +1
Energy Pile Thermal Conductance ( Cp ) 24.4 21.33 17.75 34.52
Results & Discussion
21
Dr. Khaled Ahmed
 Verification & Comparison
Maximum expected
34.52
Conclusions
22
Dr. Khaled Ahmed
 Defined the optimum condition with the least
number of experiments using uniform design
 Three uniform designs have been tested;
U27(39), U36(39), and U51(39).
 U36(39) has shown acceptable level of error with
significantly low number of experiments….
Conclusions
23
Dr. Khaled Ahmed
 The maximum energy pile steady state thermal
conductance is achieved with;
 the highest number of U-tubes, (n++).
 largest tube diameter, (di++).
 largest distance between tubes, (S++).
 highest pile thermal conductivity and (Kp++).
 highest heat transfer coefficient (H++).
THANKS
ACKNOWLEDGEMENTS
This publication was made possible by grant No. NPRP
7-725-2-270 from the Qatar National Research Fund (a
member of Qatar Foundation). The statements made
herein are solely the responsibility of the authors.

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Presentation_IMECE_20121.pptx

  • 1. Optimization of Energy Pile Conductance using Finite Element and Fractional Factorial Design of Experiment Dr. Khaled Ahmed Mechanical & Industrial Engineering Department, Qatar University, Doha, Qatar. Dr. Mohammed Al-Khawaja Mechanical & Industrial Engineering Department, Qatar University, Doha, Qatar. Dr. Muhannad Suleiman Civil and Environmental Engineering, Lehigh University, Bethlehem, PA, USA. 2017 International Joint Conference on Civil and Mechanical Engineering JCCME 2017
  • 2. Outline 2 Dr. Khaled Ahmed  Introduction οƒ˜ Review οƒ˜ Problem Statement οƒ˜ Objectives  Finite Element Model  Controlling Factors  Design of Experiment  Results & Discussion  Conclusions
  • 3. Introduction 3 Dr. Khaled Ahmed  Review  Cooling Buildings with AC is increasing
  • 4. Introduction 4 Dr. Khaled Ahmed  Review  GSHP, Ground Source Heat Pump
  • 5. Introduction 5 Dr. Khaled Ahmed  Review  Wellbores
  • 6. Introduction 6 Dr. Khaled Ahmed  Review  Energy Piles work as heat exchangers
  • 7. Introduction 7 Dr. Khaled Ahmed  Review  Energy Piles has three materials and 5 geometrical factors. 1 U-tube 2 U-tubes 3 U-tubes
  • 8. Introduction 8 Dr. Khaled Ahmed  Problem Statement  Energy Piles has many controlling factors ( >> 5).  Interaction between these factors is missed.  Optimization based on all possible factors is missed.  Proper design of experiment is required.
  • 9. Introduction 9 Dr. Khaled Ahmed  Objectives  Use well verified finite element model.  Define wide range of possible controlling factors.  Define design of experiment considering all factors.  Predict a statistical correlation between factors.  Predict statistically the optimum controlling factors.
  • 10. Finite Element Model 10 Dr. Khaled Ahmed  Geometrical Model  Symmetrical Pattern
  • 11. Finite Element Model 11 Dr. Khaled Ahmed  Energy Balance using Galerkin Method  Boundary Conditions  Post Analysis 𝐡 𝑇 𝐾 𝐡 𝑑𝐴 𝐴 + β„Ž 𝑁𝑠 𝑇 𝑁𝑠 𝑑𝑆 𝑆 𝑇 = π‘žπ‘  𝑁𝑠 𝑇 𝑑𝑆 𝑆 + β„Žπ‘‡π‘“ 𝑁𝑠 𝑇 𝑑𝑆 𝑆 𝛛𝐓 𝛛𝐒 = 𝟎 π‘»π€βˆ’π = πŸπŸ“ 𝐨 𝐂 βˆ’πŠπ¬ 𝛛𝐓 𝛛𝐒 = 𝐇 𝐓𝐬 βˆ’ π“πŸ π‘ͺ𝐩,𝐅𝐄 = ππ€βˆ’π 𝐓𝐭 βˆ’ π“π‚βˆ’πƒ
  • 12. FE Model Verification 12 Dr. Khaled Ahmed  Mesh Density Sensitivity. 𝑅𝑝 = 1 4πœ‹πΎπ‘ ln 𝑑𝑝 4 4π‘‘π‘œπ‘†3 𝑑𝑝 8 𝑑𝑝 8 βˆ’ 𝑆8 πΎπ‘βˆ’πΎπ‘  𝐾𝑝+𝐾𝑠 + 1 2π‘›πœ‹ 1 2𝐾𝑑 ln π‘‘π‘œ 𝑑𝑖 + 1 𝑑𝑖𝐻 𝑑
  • 13. Controlling Factors 13 Dr. Khaled Ahmed  Geometrical Factors  n: Number of U-tubes  dp [m]: Pile diameter.  di [m]: Tube inner diameter  t [m]: Tube thickness  S [m]: Tubes spacing.  Physical Factors  Kp [W/m.K]: Pile thermal conductivity.  Ks [W/m.K]: Soil thermal conductivity.  Kt [W/m.K]: Tube thermal conductivity.  Operational Factors  H [W/m2.K]: Convection heat transfer coefficient. 9 Factors
  • 14. Controlling Factors 14 Dr. Khaled Ahmed  Factors Range n dp [m] di [m] t [m] S [m] Kp [W/m.K] Ks [W/m.K] Kt [W/m.K] H [W/m2.K] -1 1 0.4 0.02 0.002 0.4 dp 1.0 0.5 0.5 10 0 2 0.7 0.03 0.003 0.6 dp 1.75 1 16 55 +1 3 1.0 0.04 0.004 0.8 dp 2.25 1.5 32 100
  • 15. Design of Experiment 15 Dr. Khaled Ahmed  Taguchi Design  Minimum number of experiments.  Works fine with small number of factors.  Linear correlation.  Box-Behnken Design  Large number of experiments.  Works fine with up to 7 factors.  Quadratic correlation.  Uniform Design  Offer wide range of number of experiments  Works fine with large number of factors.  Quadratic correlation using step regression. Taguchi Box-Behnken Uniform
  • 16. Design of Experiment 16 Dr. Khaled Ahmed  Uniform Design  Choosing number of experiments U 27 (3 9 ) U 36 (3 9 ) U 51 (3 9 ) Fang et a., Number-theoretic methods in statistics, CRC Press, 1993.
  • 17. Design of Experiment 17 Dr. Khaled Ahmed  Uniform Design Tables Fang et a., Number-theoretic methods in statistics, CRC Press, 1993. n dp di t S Kp Ks Kt H Conductance 1/Rp 1 1 1 1 1 1 0 -1 -1 1 7.84 2 0 1 -1 0 1 -1 0 1 1 2.27 3 1 -1 1 1 -1 0 1 0 0 4.64 4 0 -1 1 -1 0 1 -1 -1 -1 3.05 5 -1 0 0 1 1 -1 1 0 1 1.86 6 -1 1 0 1 0 -1 1 1 0 1.38 7 1 0 0 -1 -1 1 1 -1 1 5.17 8 0 0 0 0 0 0 0 0 0 3.22 9 0 0 0 1 1 -1 -1 -1 0 2.93 10 0 1 -1 -1 0 1 1 0 1 2.70 11 0 1 0 1 -1 1 -1 0 -1 1.90 12 0 1 1 0 -1 -1 1 -1 1 2.86 13 1 1 0 1 1 1 0 1 0 5.37 14 0 0 0 0 0 0 0 0 0 3.22 15 -1 0 0 1 -1 0 0 -1 -1 0.96 16 -1 -1 1 0 1 1 1 0 1 3.67 17 1 1 1 0 0 1 0 0 0 6.42 18 0 0 1 1 1 1 1 0 -1 3.10 19 0 -1 0 0 0 0 0 -1 1 4.23 20 1 -1 0 0 -1 -1 -1 0 1 3.12 21 1 0 1 -1 0 -1 0 0 1 5.26 22 -1 0 -1 0 -1 1 1 1 0 1.00 23 1 0 -1 -1 1 1 -1 0 0 3.05 24 -1 0 -1 -1 0 -1 -1 -1 1 1.10 25 -1 1 1 0 1 -1 -1 0 -1 1.25 26 -1 0 1 1 0 1 -1 1 1 3.31 27 -1 1 -1 0 1 1 0 -1 -1 0.55
  • 18. Results & Discussion 18 Dr. Khaled Ahmed  Signal to Noise Ratio 𝑆 𝑁 = βˆ’10 log10 1 π‘š 𝑖=1 π‘š 𝑅𝑝,𝑖 2
  • 19. Results & Discussion 19 Dr. Khaled Ahmed  Cubic Regression π‘Œ = π‘Ž0 + π‘˜=1 9 π‘Žπ‘˜π‘₯π‘˜ + 𝑖=1 9 𝑗=𝑖 9 𝑏𝑖𝑗π‘₯𝑖π‘₯𝑗 + 𝑖=1 9 𝑗=𝑖 9 π‘˜=𝑗 9 π‘π‘–π‘—π‘˜π‘₯𝑖π‘₯𝑗π‘₯π‘˜
  • 20. Results & Discussion 20 Dr. Khaled Ahmed  Maximum Conductance U27(39) U36(39) U51(39) Optimum Number of Tubes ( n ) +1 +1 0 +1 Pile Diameter ( dp ) -1 +1 -1 -1 Tube Inner Diameter ( di ) +1 0 0 +1 Tube Thickness ( t ) -1 -1 -1 0 Distance between Tubes ( S ) +1 +1 +1 +1 Pile Thermal Conductivity ( Kp ) +1 +1 +1 +1 Ground Thermal Conductivity ( Ks ) -1 0 -1 0 Tube thermal Conductivity ( Kt ) 0 0 +1 +1 Heat Transfer Coefficient ( H ) 0 +1 +1 +1 Energy Pile Thermal Conductance ( Cp ) 24.4 21.33 17.75 34.52
  • 21. Results & Discussion 21 Dr. Khaled Ahmed  Verification & Comparison Maximum expected 34.52
  • 22. Conclusions 22 Dr. Khaled Ahmed  Defined the optimum condition with the least number of experiments using uniform design  Three uniform designs have been tested; U27(39), U36(39), and U51(39).  U36(39) has shown acceptable level of error with significantly low number of experiments….
  • 23. Conclusions 23 Dr. Khaled Ahmed  The maximum energy pile steady state thermal conductance is achieved with;  the highest number of U-tubes, (n++).  largest tube diameter, (di++).  largest distance between tubes, (S++).  highest pile thermal conductivity and (Kp++).  highest heat transfer coefficient (H++).
  • 24. THANKS ACKNOWLEDGEMENTS This publication was made possible by grant No. NPRP 7-725-2-270 from the Qatar National Research Fund (a member of Qatar Foundation). The statements made herein are solely the responsibility of the authors.