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Thermal Design and Optimization of Heat Sinks

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1 Thermal Design and Optimization of Heat Sinks
J. Richard Culham

2 Outline Modelling Approach Validation Optimization Future Work Summary
Background Modelling Approach Validation Optimization Future Work Summary

3 40 Watts! What’s the big deal?
Pentium III  0.25 micron CMOS technology  9.5 million transistors  MHz Light Bulb Silicon Package  Power: 40 W  Area: 120 cm  Flux: 0.33 W/cm  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 2 2 80 x

4 Component Failure Rate
Intel Design Specification: T = 75 C Pentium 233 MHz @ 7.9 W no heat sink o o FC: C j (2 m/s) NC: C o Pentium 233 MHz @ 7.9 W with heat sink NC: C o Si - SiO 2 o FC: C Normalized Failure Rate (2 m/s) GaN - SiC Junction Temperature ( C) o

5  a new generation of chips is released every 18 - 24 months
Moore’s Law (1965)  each new chip contains roughly twice as much capacity as its predecessor  a new generation of chips is released every months 1975 1980 1985 1990 1995 2000 Micro 2000 From: 10M 500 Pentium III (transistors) (mips)  in 26 years, the population of transistors per chip has increased by 3,200 times Pentium 1M 25 80486 80386 100K 1.0 80286 8086 10K 0.1 8080 4004 0.01

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  immersion cooling (boiling)  impingement cooling
Heat sink (air) Heat source (junction) 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 Natural convection Isothermal Steady state
Plate fin heat sink Natural convection Isothermal Steady state Working fluid is air i.e. Pr = 0.71

11 dimensions & temperature
Modelling Procedure bp t g Exterior surfaces N f fins : top, bottom, ends & tip base plate: top, bottom, ends and back b L L Interior surfaces H t Given: fins : side walls channel base dimensions & temperature Find: Nu vs. Ra b b

12 Exterior Surfaces Diffusion lower Rayleigh numbers
thick boundary layers Boundary layer higher Rayleigh numbers thin boundary layers

13 Interior Surfaces Channel flow
Elenbaas model with adjustment for end wall combined flow : developing fully developed Control surfaces open surfaces with energy migration

14 Comprehensive Model diffusion channel flow external boundary
layer flow

15 Model Validation Limiting Cases 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) Heat Sinks

16 Modelling Domain Nu Ra b Aspect ratio b Plate spacing b Boundary layer
limit Aspect ratio Nu b Plate spacing b fully-developed limit Ra b

17 + = + + + Nu Nu Nu Nu g Ra Nu -1/2 -2 -2 4 3 1 2 b
L x W x H (mm) Chamberlain (1983) x 43.2 x 43.2 Stretton (1984) x Model 43.2 W L H g Ra b Nu -1/2 -2 + -2 Nu = + 4 3 Nu + + Nu 1 Nu 2 CUBE PRISM FLAT PLATE   PLATES HEAT SINK

18 Which is the Right Tool?  design is known a priori
Analysis Tool Design Tool vs.  design is known a priori  used to calculate the performance of a given design, i.e. Nu vs. Ra  cannot guarantee an optimized design  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
Why use Entropy Generation Minimization?  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

20 Entropy Balance (local)
conservation of mass + 1st law of thermodynamics + Gibb’s Equation heat transfer viscous dissipation

21 Entropy Balance (external & internal)
Passage geometry A T w m irreversibilities due to: wall-fluid ∆T fluid friction dx Extended surface T B T w Q B Q A irreversibilities due to base-wall ∆T

22 Total Entropy Generation
System • fins • base plate Extended surface • fin • channel flow differential control volume component level elemental level differential level dx dz dy where: base heat flow rate base - stream temp. difference ambient temperature - specified drag force - fan curve total fin resistance - buoyancy induced

23 Example: Heat Sink Optimization
Step 1: Determine problem constraints i) power input, Q ii) maximum chip temperature, Tmax iii) geometry , H, L, W W L Board spacing  H

24 Example: Heat Sink Optimization
Step 2: Set maximum heat sink volume i) package foot print = L x W ii) maximum height - board spacing minus package height L W H Board spacing  H

25 Example: Heat Sink Optimization
Step 3: Optimize heat sink i) number of fins ii) fin thickness iii) fin spacing iv) base plate thickness L W H Board spacing  H

26 Entropy Generation (W/K)
Single Parameter EGM H = L = W = 50 mm Fin thickness = 1 mm Base plate thickness = 1.25 mm Q = 50 W Find: number of fins Entropy Generation (W/K) 14 Number of Fins

27 Multi-Parameter Minimization Procedure
Newton-Raphson Method with Multiple Equations and Unknowns where: iterate until

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

30 The End


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