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Hindawi Publishing Corporation Active and Passive Electronic Components Volume 2011, Article ID 823654, 8 pages doi:10.1155/2011/823654 Research Article Application of Thermal Network Model to Transient Thermal Analysis of Power Electronic Package Substrate Masaru Ishizuka, 1 Tomoyuki Hatakeyama, 1 Yuichi Funawatashi, 1 and katsuhiro Koizumi 2 1 Department of Mechanics System Engineering, Toyama Prefectural University, Imizu 939-0398, Japan 2 COSEL CO. LTD., 1-6-43 Kamiakae-machi, Toyama 930-0816, Japan Correspondence should be addressed to Masaru Ishizuka, [email protected] Received 12 April 2011; Revised 4 August 2011; Accepted 6 September 2011 Academic Editor: P. Markondeya Raj Copyright © 2011 Masaru Ishizuka et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. In recent years, there is a growing demand to have smaller and lighter electronic circuits which have greater complexity, multifunctionality, and reliability. High-density multichip packaging technology has been used in order to meet these requirements. The higher the density scale is, the larger the power dissipation per unit area becomes. Therefore, in the designing process, it has become very important to carry out the thermal analysis. However, the heat transport model in multichip modules is very complex, and its treatment is tedious and time consuming. This paper describes an application of the thermal network method to the transient thermal analysis of multichip modules and proposes a simple model for the thermal analysis of multichip modules as a preliminary thermal design tool. On the basis of the result of transient thermal analysis, the validity of the thermal network method and the simple thermal analysis model is confirmed. 1. Introduction Laptop personal computers and cellular phones have become smaller and thinner in recent years, while their functions have become more sophisticated. As a result, the heat dis- sipation density and dissipation power per volume of these devices have significantly increased. Cooling design is the key to the prevention of heat problems. At the same time, there are growing demands for the acceleration of product development and reduction of costs. Computational fluid dynamics (CFDs) codes [1, 2] have proved their high potential as a tool of thermal design of electronic equipment. However, as the product development cycle is shortened, the CFD-based thermal design needs a new format that allows the packaging designer fast and ver- satile searches for better design options. The most serious factor that slows the CFD-based design is the geometric complexity created by packing various components in a tight space of the system box. Recently, in order to reduce the CFD workload, several approaches for the thermal design of electronic equipment have been reported. Nakayama et al. [35] proposed a methodology coined build-up approach (BUA) and have ap- plied it to the board- and box-level thermal analyses. Min- ichiello and Belady [6] proposed a thermal design method- ology and applied it to the design of a multi-processor enterprise server, the RP8400. Their methodology combines the well-known analytical and experimental thermal design tools, including heat transfer correlations, flow network modeling, and CFD techniques and experimental measure- ments. In a broader perspective, the issue of our interest is concerned with model reduction methodologies, and on this subject, several reports have been presented. Assumption of velocity profiles in computational elements reduces the nonlinear momentum equation to a linear equation, and such linearized models have been proposed by Moosmann et al. [7], D’Amore et al. [8], and Rudnyi et al. [9]. Molina and Clemente [10] reported on an automated technique for reducing actual systems to lumped-parameter thermal models. Ishizuka and Hayama [11] have also proposed a thermal analysis scheme, in which CFD analysis and thermal network

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  • Hindawi Publishing CorporationActive and Passive Electronic ComponentsVolume 2011, Article ID 823654, 8 pagesdoi:10.1155/2011/823654

    Research Article

    Application of Thermal Network Model to Transient ThermalAnalysis of Power Electronic Package Substrate

    Masaru Ishizuka,1 Tomoyuki Hatakeyama,1 Yuichi Funawatashi,1 and katsuhiro Koizumi2

    1 Department of Mechanics System Engineering, Toyama Prefectural University, Imizu 939-0398, Japan2 COSEL CO. LTD., 1-6-43 Kamiakae-machi, Toyama 930-0816, Japan

    Correspondence should be addressed to Masaru Ishizuka, [email protected]

    Received 12 April 2011; Revised 4 August 2011; Accepted 6 September 2011

    Academic Editor: P. Markondeya Raj

    Copyright © 2011 Masaru Ishizuka et al. This is an open access article distributed under the Creative Commons AttributionLicense, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properlycited.

    In recent years, there is a growing demand to have smaller and lighter electronic circuits which have greater complexity,multifunctionality, and reliability. High-density multichip packaging technology has been used in order to meet theserequirements. The higher the density scale is, the larger the power dissipation per unit area becomes. Therefore, in the designingprocess, it has become very important to carry out the thermal analysis. However, the heat transport model in multichip modulesis very complex, and its treatment is tedious and time consuming. This paper describes an application of the thermal networkmethod to the transient thermal analysis of multichip modules and proposes a simple model for the thermal analysis of multichipmodules as a preliminary thermal design tool. On the basis of the result of transient thermal analysis, the validity of the thermalnetwork method and the simple thermal analysis model is confirmed.

    1. Introduction

    Laptop personal computers and cellular phones have becomesmaller and thinner in recent years, while their functionshave become more sophisticated. As a result, the heat dis-sipation density and dissipation power per volume of thesedevices have significantly increased. Cooling design is thekey to the prevention of heat problems. At the same time,there are growing demands for the acceleration of productdevelopment and reduction of costs.

    Computational fluid dynamics (CFDs) codes [1, 2] haveproved their high potential as a tool of thermal design ofelectronic equipment. However, as the product developmentcycle is shortened, the CFD-based thermal design needs anew format that allows the packaging designer fast and ver-satile searches for better design options. The most seriousfactor that slows the CFD-based design is the geometriccomplexity created by packing various components in a tightspace of the system box.

    Recently, in order to reduce the CFD workload, severalapproaches for the thermal design of electronic equipmenthave been reported. Nakayama et al. [3–5] proposed a

    methodology coined build-up approach (BUA) and have ap-plied it to the board- and box-level thermal analyses. Min-ichiello and Belady [6] proposed a thermal design method-ology and applied it to the design of a multi-processorenterprise server, the RP8400. Their methodology combinesthe well-known analytical and experimental thermal designtools, including heat transfer correlations, flow networkmodeling, and CFD techniques and experimental measure-ments.

    In a broader perspective, the issue of our interest isconcerned with model reduction methodologies, and on thissubject, several reports have been presented. Assumptionof velocity profiles in computational elements reduces thenonlinear momentum equation to a linear equation, andsuch linearized models have been proposed by Moosmannet al. [7], D’Amore et al. [8], and Rudnyi et al. [9]. Molinaand Clemente [10] reported on an automated techniquefor reducing actual systems to lumped-parameter thermalmodels.

    Ishizuka and Hayama [11] have also proposed a thermalanalysis scheme, in which CFD analysis and thermal network

  • 2 Active and Passive Electronic Components

    method are coupled. In this scheme, the essential factorsaffecting thermal fluid phenomena in electronic equipmentare first clarified using CFD analysis, then, using the CFDresults obtained under suitable boundary conditions, mainheat flow passages are identified. At the end of the model-reduction process, a thermal network model is developed.The thermal network model facilitates the design parametersurvey for choosing a set of optimum parameters withoutresorting to time-consuming CFD analysis. Ishizuka et al.have proposed some simplified models such as heat diffusionmodel in [12], thermal convection model in [13], phasechanging process model in [14, 15], and 3D model in [15]to simulate various thermal behaviors in electronic devices.From those results, it is found that if we would understandthe heat phenomenon in a system, some temperature valuesfor the system could be predictable by using a simplifiedmodel for a thermal network method.

    The present study focuses on the derivation of a simplernetwork model to predict the transient temperature distri-bution of the package substrate covered by the cap, wherethe package consists of high-power transistor chips, otherIC chips, resistor chips, and capacitor chips. The analysiswas carried out to simulate the results of the transienttemperature rise on the surface of a substrate, taking intoconsideration natural convection and radiation, in the heattransfer mode for a cap-attached circuit substrate in additionto the thermal conduction. The alumina substrate has acircuit composed of various chips centering around fourpower transistor chips (hereinafter called power transistors).The heat transfer modes for packages are very complicated.The validity of the proposed thermal network model isdemonstrated on the basis of a comparison between calcu-lated values and measured values.

    2. Experiment

    2.1. Package Structure. Various kinds of chips such as IC,resistor, and capacitor, centered around four power transis-tors (square of 4.5 mm in size, 0.3 mm in thickness, eachhaving power dissipation of 8 W), are mounted and wire-bonded to form an electronic circuit on a 1.6 mm-thick and6 cm-square substrate formed from 92% alumina ceramic.The vicinity of the power transistors is illustrated in Figure 1.The power transistors, a heat source in this circuit, arearranged at 4 mm intervals.

    The power dissipation value contributed from otherchips may be neglected. Interconnections are provided with-in the substrate, forming a multilayer printed circuit board.This chip group is covered with a 5 cm-square, 2.8 mm-highand 0.25 mm-thick kovar cap, in which nitrogen gas (N2gas) is sealed. Figure 2 shows a cross-sectional view of thesubstrate. The power transistor chips were mounted on themolybdenum heat sink blocks, which were aligned on thecopper heat sink blocks with electroconductive epoxy. Theother IC chips, resistor chips and capacitor chips were alsomounted on the substrate top conductor metal die pads withelectroconductive epoxy. They were then wire-bonded with30 μm diameter gold wire.

    Condenser chip

    Resistor chips

    IC chips

    Power transistor chips

    (a)

    (b)

    Figure 1: (a)Power-transistor layout. (b)Power transistors (photo).

    2.2. Temperature Measurement. The module to be measuredwas held horizontally 10 cm above the surface of a desk andsupported at its edges by three thin glass epoxy sticks (3 mmin diameter) in a clean room with free airflow. Temperaturewas controlled to 298 K. A point equally distant from thefour power transistors was considered as the center (radiusr = 0), and two points were located on the back of thesubstrate (r = 0) and one on the front (r = 2.55 mm).A copper-constantan thermocouple (0.1 mm in diameter)for use in making the measurements was bonded by goodconductive epoxy material to each of the measuring points.As a measuring procedure, temperature rise values after theapplication of electric power from a DC power source tothe power transistors were recorded by means of an infraredcamera. The experiment was stopped when temperature T0at measuring point r = 0 on the back of the substrateexceeded 410 K.

    3. Analysis

    3.1. Heat Transfer Model for Multichip Modules. The pathsthrough which package heat transfer takes place was con-sidered as follows. The substrate bottom area and substratetop area, with the exception of the kovar cap area, include

  • Active and Passive Electronic Components 3

    IC chip

    Kavar cap (0.25 mm)

    Power transistor chipSilicon chip (0.3 mm)

    Gold wire

    Electroconductive epoxy (50 µm)

    Molybdenum block (0.45 mm)

    Copper block (0.2 mm)

    Silver-copper eutectic alloy (50 µm)

    isolation layer(total 75 µm)

    Nitrogen gas

    92% alumina ceramic substrate (1.5 mm)

    (value) indicates individual layer thickness

    Cofired ceramic paste

    Figure 2: Cross-sectional view of the substrate.

    Kovar shellThermal radiation

    Heat conduction

    Natural convection

    Chip

    Nitrogen gas

    Multilayer ceramic substrate

    h

    Thermal radiation

    Naturalconvection

    Thermalradiation

    Naturalconvection

    Thermal radiationHeatconduction

    Figure 3: Heat transfer form for package.

    heat transport by thermal radiation and natural convection.Inside the kovar cap, heat transport by heat conduction ofthe nitrogen gas and thermal radiation was considered. At thekovar cap top surface area, heat transport occurs by thermalradiation and natural convection. Furthermore, inside thesubstrate and the cap, heat transport occurs only by thermalconduction. These aspects are illustrated in Figure 3.

    Figure 3 indicates the paths by which heat transfer fromthe module takes place, where the following major heattransfer factors were considered:

    (1) thermal conduction inside the substrate,

    (2) natural convection and thermal radiation from thetop and bottom surfaces of the substrate to theatmosphere,

    (3) thermal conduction through N2 gas and thermalradiation from the substrate surfaces to the cap,

    (4) thermal conduction from the substrate to the capthrough the welded area between the substrate andthe cap (not shown in Figure 3).

    3.2. Thermal Network Model. The existence of the cap isconsidered to have an influence on the temperature distri-

    bution; therefore, the effect of the cap should be taken intoconsideration. However, since considering the cap resultsin a complicated three-dimensional analytical model, thereis no advantage in adopting the thermal network method.Therefore, the analytical model is formed on the basis ofthe following assumptions to reduce the model’s dimensionsfrom three to one.

    (1) The temperature of the center of the cap surface isthe same as that of the substrate area where the cap iswelded.

    (2) The 4 power transistors are regarded as one nodalpoint.

    (3) The heat dissipated by the power transistors flows outin the radial direction.

    These assumptions will make the analytical model one di-mensional (axial symmetry).

    The substrate was divided, as shown in Figure 4, cen-tering on the power transistor (r = 0). It is assumedthat there is no temperature difference between individualdivided partitions and that the partitions are numbered0, 1, 2, . . . ,n, respectively, from the center. In this study, n wastaken as 6. Representing the heat resistance and the thermalcapacitance for each partition by R and C, respectively, thethermal network model for the heat transfer is formed, whereheat flux Q0 is generated by the power transistors, as shownin Figure 5. The total of the heat flux Q0 was assumed toflow out toward the region 1 in the substrate. Since the areaof the region 0 including the power transistor chips weresmaller than those of the other regions, the heat transfer forthe central region 0 was neglected. In Figure 5, in the caseof the first partition where the temperature is represented byT1, heat flow Q1 flows out toward external region 2 throughheat resistance R3 due to the thermal conduction. Some ofthe heat is stored in the thermal capacitance C1, or dissipateddirectly or indirectly through cap, out of the substrate bynatural convection and thermal radiation through thermalresistance values such as R2 and R16. It is assumed that

  • 4 Active and Passive Electronic Components

    Q

    Substrate

    Cap

    T0

    T4

    T5

    T6

    r4 r6

    T : temperatureQ: heat flow rater: radius

    r

    r0

    Figure 4: Substrate partition.

    T1 T2 T3 T4 T5 T6 T7C1 C2 C3 C4 C5 C6 C7

    R1 R3 R5 R7 R9 R11 R13R15 R16 R17 R18

    R19 R20 R21 R22 R10R12 R14

    Ground

    Aluminasubstrate

    HeatsourceQ0

    Cap

    T0

    Ground

    Figure 5: Thermal network model (Model 1).

    C7 value is infinite. Note that although the actual moduleforms a regular square and the power transistors are arrangedquadrilaterally, these may be represented approximately bycircles, having diameters equal to the length of one side of therespective rectangle, as shown in Figure 4. On the basis of thepreviously mentioned assumptions, the center of the cap waslinked with the welded portion of the substrate without anythermal resistance.

    In addition, the cap thermal capacity was neglected,because it is infinitesimally small compared to that ofsubstrate. In addition, it is assumed, as described previously,that cap temperature is equal to substrate temperature inpartition 5.

    3.3. Evaluation of Thermal Resistance. The thermal conduc-tion partition model in the substrate is illustrated in Figure 6.It was assumed that a circular heat source, whose radius isr0 cm, exists at the center of a circular multilayer ceramicsubstrate, whose thickness is d cm, and the heat diffuses inthe radial direction. If the temperature at a point on radiusr1 is T1 and the temperature at a point of radius r2 is T2, theheat flow rate along the radial direction is given by

    Qcd = 2πdsλs ΔTln(r2/r1) , (1)

    r0r1

    r2

    rn

    0 1 2 dn

    Subs ra e

    Figure 6: Thermal conduction partition model in the substrate.

    where ΔT = T1 − T2, λs is the thermal conductivity of thesubstrate.

    Therefore, the thermal resistance, Rcd in region coveredby radius r1 and radius r2 is given by

    Rcd = ΔTQcd

    = ln(r2/r1)(2πds λs)

    . (2)

    The thermal resistance for nitrogen gas inside the kovarcap is given by

    RN = h(λNA) , (3)

    where λN is thermal conductivity, h is the substrate-to-capdistance, and A represents the thermal conduction area.

    If there exists a temperature difference (ΔT) between theair and the substrate, the heat flow rate Qcv which passesthrough the area A of the substrate is given by

    Qcv = αcvAΔT. (4)In general, the heat transfer coefficient, αcv is related to

    the heat transfer phenomenon. If the flow is laminar and theheat transfer occurs through natural convection, the naturalconvection heat coefficient in the case of two-dimensionalflat plate is given considering that Gr·Pr value (Grashof andPrandtl number) in this study was the order of 105 as follows

    αcv = 2.8D(ΔT

    L

    )0.25, (5)

    where ΔT is the temperature rise with reference to ambienttemperature Ta; Ta = 298 K is selected as a referencetemperature and the value of D is determined by theorientation location of the flat plate, shown in Figure 7.Facing up it is equal to 0.54, while facing down it is 0.27. Lis the characteristic length which is determined by the flowpath of the cooling air on the hot surface of the material. Inthis divided doughnut-shaped plate, having inner and outerradius of r1 and r2, respectively, the assumed characteristiclength L is given by the ratio of area/perimeter of thedoughnut-region as follows:

    L = π(r22 − r21

    )2π(r1 + r2)

    = (r2 − r1)2

    (6)

    Then, thermal resistance Rcv is expressed as follows, where Arepresents the thermal radiation area:

    Rcv = 1(αcvA) . (7)

  • Active and Passive Electronic Components 5

    Flat pate

    Heat flow

    D = 0.56

    (a)

    Flat pate

    Heat flow

    Top surface is hotD = 0.52

    (b)

    Flat pate

    Heat flow

    Bottom surface is hot

    D = 0.26

    (c)

    Figure 7: Value D in natural heat transfer equation (5).

    In the exchange of thermal radiation energy between twomaterials which are not black bodies, the general thermalradiation equation is given by

    Qra = σFA(T41 − T42

    ), (8)

    where σ is Stefan-Boltzmann’s constant which is 5.67 ×10−8 W/m2 K4, A is the thermal radiation area, and T1 andT2 are absolute temperature, respectively. Furthermore, F isthe shape factor which is defined as

    F = 1(1/ε1 + (A1/A2)(1/ε2 − 1)) , (9)

    where ε1 and ε2 are emissivities for the materials. If one sideis the atmosphere, A2 becomes infinity; therefore, F becomesε1.

    From (8), thermal resistance Rra is expressed as follows:

    Rra = (T1 − T2)Qra

    = 1(σFA

    (T21 + T

    22

    )(T1 + T2)

    ) . (10)

    3.4. Calculation of Thermal Capacitance. The calculation ofthermal capacitance of each partition, for example, Ci is forthe ith partition, is expressed as follows, by defining thesubstrate density as ρ, specific heat at constant pressure ascp, and substrate thickness as d:

    Ci = cpπd(r2i − r2i−1

    ). (11)

    T0 R1 T1 T2R2

    Q1 Q2

    C1

    Figure 8: Heat flow at tee section.

    3.5. Equation Formulation. The thermal network methodis based on the similarity between the diffusion equationfor thermal engineering and that for electric engineering,and it is found that the analogous quantities are voltage-temperature and current-heat flow.

    Therefore, the transient analog method is formed on thebasis of a number of lumped RC tee sections, as shown inFigure 8, with subsequent employment of the node analysismethod. The following equations, which can be written asexamples, are based on heat flow conservation for a nodalpoint

    C1dT1dt

    = Q1 −Q2 at T1 point, (12)

    and for heat paths based on thermal resistance definition

    T0 − T1 = Q1R1 for R1,T1 − T2 = Q2R2 for R2,

    (13)

    where Q represents the heat flow value through thermalresistance and T represents the temperature value.

    3.6. Calculation Procedure. The above equations are nonlin-ear in nature, due to (7) and (10), and iterative calculationsare required. However, to simplify the method of calculatingparameters, temperature T , required for calculating (7) and(10), is approximated by a value calculated with τ = τi−Δτinstead of τ = τi, assuming that temperature change ΔT isvery small during the period Δτ when Δτ is very small; thatis, Δτ � RiCi. To solve these equations, the Runge-Kuttasecondary approximate method is used. The calculation flowchart is given below.

    (1) Set the applied power Q0.

    (2) Give the initial temperature value T0 for the initialtime τ0.

    (3) Calculate the thermal resistance values R0 from (7)and (10) using the above temperature value T0 andthermal capacitance C.

    (4) Solve the linearized equation system to yield thetemperature for the new time level τ = τ0 + Δτ usingthe Runge-Kutta method.

    (5) Advance the time level τ by Δτ.

  • 6 Active and Passive Electronic Components

    (6) The newly predicted temperatures are assigned to theinitial temperature.

    (7) The procedure is repeated from step (5) for thesubsequent time level until τ = τmax.

    3.7. Numerical Example. As the calculation condition, thepower transistor region, the shapes of the cap, and thesubstrate are approximated as a circle of diameter 1.5 cm,5 cm, and 6 cm, respectively, as shown as Figure 4. It is alsoassumed that the substrate is partitioned into six sections(number of partitions n = 6), having radii of r0 =0.75 cm (central partition), r1 = 0.9 cm, r2 = 1.1 cm,r3 = 1.5 cm, r4 = 2.2 cm, r5 = 2.6 cm, and r6 =3.0 cm, respectively, where r represents the radius for eachcircle. Substrate characteristics are as follows. Thickness:ds = 1.5 mm, thermal conductivity: λs = 16.7 W/(mK),density: ρ = 3.6 × 103 kg/m3, and specific heat: cp = 879J/kg K. Other factors are emissivity: εN = 0.8, nitrogenthermal conductivity: λN = 0.0286 W/mK, the cap height:h = 2.75 mm, and the cap thermal conductivity: λcap =18.6 W/mK. However, in this study, the property valuesof the cap were not decided using the assumptions. Thecalculations were carried out using a time increment Δτ =1 ms, where the conductivity of the substrate was substitutedby the conductivity of alumina which was measured by thelaser-flash method, because the volume of alumina occupies98% or more of the total substrate volume.

    4. Results

    4.1. Comparison of Calculated Values and Measured Values.Figure 9 compares the measured and predicted values forthe case of T0, T3, T5, and Tcap. T0 is the temperature ofthe partition 0 as shown in Figure 4, near the center ofthe substrate bottom surface, T3 is the temperature of thepartition 3, near the midpoint between the edge of thesubstrate bottom surface and the center of the substratebottom surface, T5 is the temperature of the partition 5,near the edge of the substrate bottom surface, and Tcap isthe temperature near the center of the kovar cap. For T3 andT5, temperatures at two different points in the same regionwere averaged. Temperature differences between the twotemperatures were within 3%. Agreement between measuredand predicted values is very satisfactory. In order to preventthe damage of chip, the power supply switch was turned offin the case of temperature T0 reaching to a value of 410 K.

    Figure 9 also shows result using the results of calculatedtemperature T0 on the basis of another model in whichthermal diffusion is caused only by the substrate thermalconduction (Model 2 as shown in Figure 10). It can beobserved here that the temperature T0 predicted by themodel 2 is approximately 10% higher as compared to thatobtained using the present model (Model 1). The trends oftemperature rise for T0 is similar to that in the case of theModel 2. The difference in temperatures other than T0 waswithin the range of 5% to 8%. Here, since the heat sink effectdue to the thermal capacity of the substrate is much largeat only initial stage of the temperature rise, the results by

    0

    25

    50

    75

    100

    125

    150

    0 10 20 30 40 50 60

    Tem

    pera

    ture

    (◦C

    )

    Time (s)

    Calculated using model 1Calculated using model 2T0

    T3T5Tcap

    Figure 9: Comparison between calculated values and measuredvalues.

    Q0Q1 Q3 Q2n−3 Q2n−1

    T0 T1 T2 TnTn−1Tn−2

    C1 C2 CnCn−1Cn−2

    R1 R3 R2n−3 R2n−1

    Figure 10: Thermal network model (Model 2).

    model 2 considering only conduction was compared onceby model 1. Of course, time passing, the difference becomesmuch larger. Of course, time passing, the difference betweenthem becomes much larger.

    5. Discussion

    In forming the heat transfer model for the present experi-ment condition, it was assumed that the thermal conductioninside the substrate plays a dominant role in contributingto the heat transfer of the package. The validity of thisassumption was verified by comparing the results obtainedby considering only thermal conduction and those obtainedby considering natural convection and thermal radiationas well as thermal conduction, as shown in Figure 9. Thetemperature difference between the results obtained by usingthe heat transfer model and those obtained by using themodel which considers only thermal conduction is at themost 10%. That is the reason that in the transient condition,the substrate capacitance works as a main heat sink, and inthe steady state condition, the atmosphere does. However,the results obtained by using the proposed heat transfermodel coincide closely with the results obtained by using

  • Active and Passive Electronic Components 7

    the model which considers only thermal conduction. Onthe basis of the recent trends that the power dissipationdensity values for future electronic elements will becomehigher or they will be used in a steady-state condition, this10% difference cannot be neglected. For the current powerdissipation density (where power dissipation density valuein this substrate is 32 watts for 36 cm2 area), this proposedmodel is considered to be useful as a simulation model forthermal design because of its simple and convenient form.It should also be noted that when a forced cooling methodis applied instead of natural convection, which was adoptedin this experiment, the effect of the proposed model shouldbe higher if (5) were replaced by the forced convection heattransfer coefficient. The difference between results obtainedby using the proposed model and by the other model wherethe natural convection and thermal radiation were neglectedwould be larger.

    6. Conclusion

    A thermal network model was applied to simulate a transienttemperature rise in small-size multichip modules. The heattransfer process by natural convection and thermal radiationwas also adopted in this model in addition to the thermaldiffusion by thermal conduction. The calculated results usingthis model gave a very reasonable estimation of the measuredsubstrate temperature values. Since substrate thermal design-ing becomes more important and great design accuracyis required, as chip power dissipation density becomeslarger, this model is considered sufficiently practical as anengineering model for simulating a transient temperaturerise in the substrate, because it is structurally simple and easyto use.

    Nomenclature

    A: Area, m2

    C: Thermal capacitance, J/Kcp: Specific heat, J/(kg K)D: Constant in the natural heat transfer

    equationd: Substrate thickness, mF: Shape factorh: Cap height, mL: Reference length, mQ: Heat flow rate, WR: Thermal resistance, K/WT : Temperature, KΔT : Temperature rise, K.

    Greek Symbols

    α: Heat transfer coefficient, W/m2 Kε: Emissivityλ: Thermal conductivity, W/m Kρ: Density, kg/m3

    σ : Stefan-Boltzmann constant = 5.67 × 10−8,W/(m2 K4)

    τ: Time, s.

    Subscription

    a: Atmospherecap: Capcd: Thermal conductioncv: Natural convectionra: Thermal radiationN: Nitrogen.

    References

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    new role of CFD simulation in thermal design of compactelectronic equipment: application of the build-up approach tothermal analysis of a benchmark model,” Journal of ElectronicPackaging, Transactions of the ASME, vol. 126, no. 4, pp. 440–448, 2004.

    [4] W. Nakayama, T. Nakajima, H. Koike, and R. Matsuki, “Heatconduction in printed circuit boards—part I; overview and thecase of a JEDEC test board,” in Proceedings of IPACK, ASMEInterPACK, Vancouver, BC, Canada, July 2007.

    [5] W. Nakayama, T. Nakajima, H. Koike, and R. Matsuki, “Heatconduction in printed circuit boards—part I; part ii; smallPCBs connected to large thermal mass at their edge,” in Pro-ceedings of IPACK, ASME InterPACK, Vancouver, BC, Canada,July 2007.

    [6] A. Minichiello and C. Belady, “Thermal design methodologyfor electronic systems,” in Proceedings of the Inter SocietyConference on Thermal Phenomena, San Diego Calif, USA,June 2002.

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    [8] D. D’Amore, L. Codecasa, and P. Maffezzoni, “An Arnoldibased thermal network reduction method for electro-thermalanalysis,” IEEE Transactions on Components and PackagingTechnologies, vol. 26, no. 1, pp. 186–192, 2003.

    [9] E. B. Rudnyi, T. Bechtold, and J. G. Korvink, “Automatic gen-eration of compact electrothermal models for semiconductordevices,” IEICE Transactions on Electronics, vol. 86C, pp. 459–465, 2003.

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