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Thermal Design and
Optimization of Heat Sinks
J. Richard Culham
Outline
 Background
 Modelling Approach
 Validation
 Optimization
 Future Work
 Summary
40 Watts! What’s the big deal?
Light Bulb
 Power: 40 W
 Area: 120 cm
 Flux: 0.33 W/cm
Pentium III
Silicon Package
 Power: 40 W
 Area: 1.5 cm
 Flux: 26.7 W/cm
 Rj-c: 0.94 C/W
 Rj-a: 6.8 C/W
(no heat sink)
 Rj-a: 2.5 C/W
(heat sink)
2 2
 0.25 micron CMOS technology
 9.5 million transistors
 450 - 550 MHz
2
2
80 x
Component Failure Rate
Junction Temperature ( C)
Normalized
Failure
Rate
o
FC: 58.2 C
NC: 96.1 C
(2 m/s)
o
o
o
Pentium 233 MHz
@ 7.9 W
no heat sink
FC: 99.5 C
NC: 136.4 C
o
Pentium 233 MHz
@ 7.9 W
with heat sink
(2 m/s)
Intel Design
Specification:
T = 75 C
j
o
GaN - SiC
Si - SiO2
Moore’s Law (1965)
1975 1980 1985 1990 1995 2000
10M
1M
100K
10K
(transistors)
500
25
1.0
0.1
0.01
(mips)
4004
8080
8086
80286
80386
80486
Pentium
Pentium III
Micro 2000
 each new chip contains roughly twice as much
capacity as its predecessor
 a new generation of chips is released every
18 - 24 months
From: www.intel.com
 in 26 years, the
population of
transistors per
chip has increased
by 3,200 times
IC Trends: Past, Present & Future
From: David L. Blackburn, NIST
Why Use Natural Convection?
 simplicity:
 low maintenance
 lower power consumption
 less space (notebook computers)
 less noise
 fail safe heat transfer condition
Thermal Resistance
Heat source
(junction)
Heat sink
(air)
contact
resistance
material
resistance
spreading
resistance
film
resistance
• increased heat transfer coefficient
 immersion cooling (boiling)
 impingement cooling
 forced air
 natural convection
• increased surface area
 spreaders
 heat sinks
Plate Fin H.S. Pin Fin H.S.
Radial Fin H.S. Specialty H.S.
Heat Sink Model
 Plate fin heat sink
 Natural convection
 Isothermal
 Steady state
 Working fluid is air i.e. Pr = 0.71
Modelling Procedure
Exterior surfaces
Interior surfaces
 fins : top, bottom,
ends & tip
 base plate: top,
bottom, ends
and back
 fins : side walls
 channel base
g
L
L
H t
b
bp
t
f
N
Given:
Find:
dimensions & temperature
Nu vs. Ra
b b
Exterior Surfaces
Boundary layer
Diffusion
 lower Rayleigh
numbers
 thick boundary
layers
 higher Rayleigh
numbers
 thin boundary
layers
Interior Surfaces
Control surfaces
Channel flow
 Elenbaas model
with adjustment
for end wall
 combined flow :
developing +
fully developed
 open surfaces
with energy
migration
Comprehensive Model
diffusion channel
flow
external
boundary
layer flow
Model Validation
 cuboids
 plate - Karagiozis (1991), Saunders (1936)
 cube - Chamberlain (1983), Stretton (1988)
 rectangular prism - Clemes (1990)
 parallel plates
 Elenbaas (1942), Aihara (1973), Kennard (1941)
 Karagiozis (1991)
 Van de Pol & Tierny (1978)
Limiting Cases
Heat Sinks
Modelling Domain
Plate spacing
Aspect ratio
fully-developed
limit
Boundary layer
limit
b
Rab
Nu
b
CUBE PRISM FLAT PLATE   PLATES HEAT SINK
+
Nu = Nu0 +Nu1
2
Nu + 4
3
Nu Nu
+
-2 -2
-1/2
L x W x H (mm)
Chamberlain (1983) 43.2 x 43.2 x 43.2
Stretton (1984) 38.1 x 38.1 38.1
Model
43.2
W
L
H
g
Rab
Nu
b
Which is the Right Tool?
 design is known a priori
 used to calculate the
performance of a given
design, i.e. Nu vs. Ra
 cannot guarantee an
optimized design
Analysis Tool Design Tool
vs.
 used to obtain an
optimized design for a
set of known constraints
i.e. given: • heat input
• max. temp.
• max. outside
dimensions
find: the most efficient
design
Optimization Using EGM
 entropy production  amount of energy degraded
to a form unavailable for work
 lost work is an additional amount of heat that could
have been extracted
 degradation process is a function of thermodynamic
irreversibilities e.g. friction, heat transfer etc.
 minimizing the production of entropy, provides a
concurrent optimization of all design variables
Why use Entropy Generation Minimization?
Entropy Balance (local)
1st law of
thermodynamics
Gibb’s
Equation
heat transfer viscous dissipation
conservation
of mass + +
Entropy Balance (external & internal)
Extended surface
Passage geometry
dx
m

A
Tw irreversibilities
due to: wall-fluid ∆T fluid friction
A
Q
B
T
B Tw
Q
irreversibilities due to
base-wall ∆T
Total Entropy Generation
differential
level
elemental
level
component
level
dx
dy
dz
differential
control
volume
Extended surface
• fin
• channel flow
System
• fins
• base plate
where:
base heat flow rate
base - stream temp. difference
ambient temperature
drag force
total fin resistance
- specified
- fan curve
- buoyancy induced
Example: Heat Sink Optimization
Board spacing  H
L
W
Step 1: Determine problem constraints
i) power input, Q
ii) maximum chip temperature, Tmax
iii) geometry , H, L, W
Example: Heat Sink Optimization
Board spacing  H
L W
H
Step 2: Set maximum heat sink volume
i) package foot print = L x W
ii) maximum height - board spacing minus
package height
Example: Heat Sink Optimization
Board spacing  H
L W
H
Step 3: Optimize heat sink
i) number of fins
ii) fin thickness
iii) fin spacing
iv) base plate thickness
Single Parameter EGM
Number of Fins
Entropy
Generation
(W/K)
14
H = L = W = 50 mm
Fin thickness = 1 mm
Base plate thickness = 1.25 mm
Q = 50 W
Find: number of fins
Multi-Parameter Minimization Procedure
where:

iterate until
Newton-Raphson Method with Multiple Equations and Unknowns
Future Work
Goal: Develop a comprehensive model to
find the best heat sink design given
a limited set of design constraints
Physical Design Thermal Cost
Standards
• heat sink type
• material
• weight
• dimensions
• surface finish
• maximum volume
• boundary conditions
• max. allowable temp.
• orientation
• flow mechanism
• labour
• manufacturing
• material
• noise
• exposure to
touch
Summary
 Heat sink design requires both a
selection tool & an analysis tool
 Selection is based on:
 physical constraints - geometry, material, etc.
 thermal-fluid conditions - bc’s, properties, etc.
 miscellaneous conditions - cost, standards etc.
 Analysis is based on simulating a
prescribed design
The End

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13055193.ppt This is heat sink material.

  • 1. Thermal Design and Optimization of Heat Sinks J. Richard Culham
  • 2. Outline  Background  Modelling Approach  Validation  Optimization  Future Work  Summary
  • 3. 40 Watts! What’s the big deal? Light Bulb  Power: 40 W  Area: 120 cm  Flux: 0.33 W/cm Pentium III Silicon Package  Power: 40 W  Area: 1.5 cm  Flux: 26.7 W/cm  Rj-c: 0.94 C/W  Rj-a: 6.8 C/W (no heat sink)  Rj-a: 2.5 C/W (heat sink) 2 2  0.25 micron CMOS technology  9.5 million transistors  450 - 550 MHz 2 2 80 x
  • 4. Component Failure Rate Junction Temperature ( C) Normalized Failure Rate o FC: 58.2 C NC: 96.1 C (2 m/s) o o o Pentium 233 MHz @ 7.9 W no heat sink FC: 99.5 C NC: 136.4 C o Pentium 233 MHz @ 7.9 W with heat sink (2 m/s) Intel Design Specification: T = 75 C j o GaN - SiC Si - SiO2
  • 5. Moore’s Law (1965) 1975 1980 1985 1990 1995 2000 10M 1M 100K 10K (transistors) 500 25 1.0 0.1 0.01 (mips) 4004 8080 8086 80286 80386 80486 Pentium Pentium III Micro 2000  each new chip contains roughly twice as much capacity as its predecessor  a new generation of chips is released every 18 - 24 months From: www.intel.com  in 26 years, the population of transistors per chip has increased by 3,200 times
  • 6. IC Trends: Past, Present & Future From: David L. Blackburn, NIST
  • 7. Why Use Natural Convection?  simplicity:  low maintenance  lower power consumption  less space (notebook computers)  less noise  fail safe heat transfer condition
  • 8. Thermal Resistance Heat source (junction) Heat sink (air) contact resistance material resistance spreading resistance film resistance • increased heat transfer coefficient  immersion cooling (boiling)  impingement cooling  forced air  natural convection • increased surface area  spreaders  heat sinks
  • 9. Plate Fin H.S. Pin Fin H.S. Radial Fin H.S. Specialty H.S.
  • 10. Heat Sink Model  Plate fin heat sink  Natural convection  Isothermal  Steady state  Working fluid is air i.e. Pr = 0.71
  • 11. Modelling Procedure Exterior surfaces Interior surfaces  fins : top, bottom, ends & tip  base plate: top, bottom, ends and back  fins : side walls  channel base g L L H t b bp t f N Given: Find: dimensions & temperature Nu vs. Ra b b
  • 12. Exterior Surfaces Boundary layer Diffusion  lower Rayleigh numbers  thick boundary layers  higher Rayleigh numbers  thin boundary layers
  • 13. Interior Surfaces Control surfaces Channel flow  Elenbaas model with adjustment for end wall  combined flow : developing + fully developed  open surfaces with energy migration
  • 15. Model Validation  cuboids  plate - Karagiozis (1991), Saunders (1936)  cube - Chamberlain (1983), Stretton (1988)  rectangular prism - Clemes (1990)  parallel plates  Elenbaas (1942), Aihara (1973), Kennard (1941)  Karagiozis (1991)  Van de Pol & Tierny (1978) Limiting Cases Heat Sinks
  • 16. Modelling Domain Plate spacing Aspect ratio fully-developed limit Boundary layer limit b Rab Nu b
  • 17. CUBE PRISM FLAT PLATE   PLATES HEAT SINK + Nu = Nu0 +Nu1 2 Nu + 4 3 Nu Nu + -2 -2 -1/2 L x W x H (mm) Chamberlain (1983) 43.2 x 43.2 x 43.2 Stretton (1984) 38.1 x 38.1 38.1 Model 43.2 W L H g Rab Nu b
  • 18. Which is the Right Tool?  design is known a priori  used to calculate the performance of a given design, i.e. Nu vs. Ra  cannot guarantee an optimized design Analysis Tool Design Tool vs.  used to obtain an optimized design for a set of known constraints i.e. given: • heat input • max. temp. • max. outside dimensions find: the most efficient design
  • 19. Optimization Using EGM  entropy production  amount of energy degraded to a form unavailable for work  lost work is an additional amount of heat that could have been extracted  degradation process is a function of thermodynamic irreversibilities e.g. friction, heat transfer etc.  minimizing the production of entropy, provides a concurrent optimization of all design variables Why use Entropy Generation Minimization?
  • 20. Entropy Balance (local) 1st law of thermodynamics Gibb’s Equation heat transfer viscous dissipation conservation of mass + +
  • 21. Entropy Balance (external & internal) Extended surface Passage geometry dx m  A Tw irreversibilities due to: wall-fluid ∆T fluid friction A Q B T B Tw Q irreversibilities due to base-wall ∆T
  • 22. Total Entropy Generation differential level elemental level component level dx dy dz differential control volume Extended surface • fin • channel flow System • fins • base plate where: base heat flow rate base - stream temp. difference ambient temperature drag force total fin resistance - specified - fan curve - buoyancy induced
  • 23. Example: Heat Sink Optimization Board spacing  H L W Step 1: Determine problem constraints i) power input, Q ii) maximum chip temperature, Tmax iii) geometry , H, L, W
  • 24. Example: Heat Sink Optimization Board spacing  H L W H Step 2: Set maximum heat sink volume i) package foot print = L x W ii) maximum height - board spacing minus package height
  • 25. Example: Heat Sink Optimization Board spacing  H L W H Step 3: Optimize heat sink i) number of fins ii) fin thickness iii) fin spacing iv) base plate thickness
  • 26. Single Parameter EGM Number of Fins Entropy Generation (W/K) 14 H = L = W = 50 mm Fin thickness = 1 mm Base plate thickness = 1.25 mm Q = 50 W Find: number of fins
  • 27. Multi-Parameter Minimization Procedure where:  iterate until Newton-Raphson Method with Multiple Equations and Unknowns
  • 28. Future Work Goal: Develop a comprehensive model to find the best heat sink design given a limited set of design constraints Physical Design Thermal Cost Standards • heat sink type • material • weight • dimensions • surface finish • maximum volume • boundary conditions • max. allowable temp. • orientation • flow mechanism • labour • manufacturing • material • noise • exposure to touch
  • 29. Summary  Heat sink design requires both a selection tool & an analysis tool  Selection is based on:  physical constraints - geometry, material, etc.  thermal-fluid conditions - bc’s, properties, etc.  miscellaneous conditions - cost, standards etc.  Analysis is based on simulating a prescribed design