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Copyright © 2009 Year IEEE. Reprinted from 2009 Electronic Components and<br />

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<strong>3D</strong> <strong>Packaging</strong> <strong>with</strong> <strong>Through</strong> <strong>Silicon</strong> <strong>Via</strong> (<strong>TSV</strong>) for Electrical and Fluidic Interconnections<br />

Navas Khan*,Li Hong Yu*, Tan Siow Pin*, Soon Wee Ho*, Nandar Su*, Wai Yin Hnin*, Vaidyanathan Kripesh*,<br />

Pinjala*, John H. Lau*^, Toh Kok Chuan**<br />

* <strong>Institute</strong> <strong>of</strong> Microelectronics, A*STAR (Agency for Science, Technology and Research), 11 Science Park Road,<br />

Science Park II, Singapore 117585; Email: oknavas@ime.a-star.edu.sg<br />

** School <strong>of</strong> Mechanical and Aerospace Engineering, Nanyang Technological University,<br />

50 Nanyang Avenue, Singapore 639798<br />

^Now <strong>with</strong> Hong Kong University <strong>of</strong> Science & Technology<br />

Abstract<br />

In this paper a liquid cooling solution has been reported<br />

for 3-D package in PoP format. The high heat dissipating<br />

chip is mounted on a silicon carrier, which has copper<br />

through-silicon via for electrical interconnection and throughsilicon<br />

hollow via for fluidic circulation. Heat enhancement<br />

structures have been embedded in the chip carrier. Cooling<br />

liquid, de-ionized water is circulated through the chip carrier<br />

and heat from the chip is extracted. The fluidic channels are<br />

isolated from electrical traces using hermetic sealing. The<br />

research work has demonstrated 100 W <strong>of</strong> heat dissipation<br />

from one stack and total <strong>of</strong> 200 W from two stacks <strong>of</strong> the<br />

package. The fluidic interconnections and sealing techniques<br />

have been discussed.<br />

Introduction<br />

System in a Package (SiP) combines semiconductors,<br />

passives and interconnects in one package, enabling higher<br />

system integration. Three-dimensional (3-D) packaging is the<br />

preferred technology for many SiP design because <strong>of</strong> the<br />

advantages <strong>of</strong> smaller size, shorter signal routing, and<br />

reduced wiring density at the second level. 3-D packaging is<br />

achieved by different techniques viz. die level stacking,<br />

package level stacking, and wafer level stacking. However,<br />

current 3-D package applications are limited to die and<br />

package level stacking for lower power applications such as<br />

memory devices, base band, and logic devices. On the other<br />

hand, the high packaging efficiency <strong>of</strong> <strong>3D</strong> stacking leads to<br />

the concentration many heat producing elements in a small<br />

volume, resulting in very high flux.[1] The power density <strong>of</strong> a<br />

single chip packaging is incessantly increasing and is<br />

expected to be higher than 100 W/cm 2 for high performance<br />

systems, such as defense systems. [2] Moreover, the space<br />

between the stacked modules is much less than 1mm, which<br />

reduces the physical space available for coolant. Thus, an<br />

integrated cooling solution is required for such application.<br />

Air-cooling is simple, low cost, and reliable cooling<br />

solution. However, the low thermal conductivity and low<br />

density <strong>of</strong> the air make it less attractive as a coolant for high<br />

heat flux 3-D packages. Liquid cooling using micro-channels<br />

is a suitable option for such application. An assessment <strong>of</strong><br />

cooling schemes available for such high heat flux<br />

applications was done <strong>with</strong> phase change cooling (Boiling)<br />

able to handle heat fluxes above 100W/cm 2 .[3] However, its<br />

application is <strong>of</strong>ten hindered by its unpredictable nature.<br />

Hence, single phase cooling using micro-channels is applied<br />

in this work. Different cooling liquid for the single phase<br />

cooling was considered, and DI water had been identified due<br />

to its better thermal properties (i.e. higher thermal<br />

conductivity).<br />

Many researchers have explored the advantages <strong>of</strong> using<br />

liquid cooling to tackle high heat flux problem [4-6]. But<br />

many challenges have not been addressed for the integration<br />

<strong>of</strong> liquid cooling in 3-D package such as embedding microchannels<br />

in the chip carrier, 3-D fluidic interconnection and<br />

fluidic sealing. In this work, a novel integrated liquid cooling<br />

technique for 3-D <strong>Silicon</strong> modules is developed. The cooling<br />

solution enables extraction <strong>of</strong> heat from the chip mounted on<br />

a silicon chip carrier and provides fluidic interconnects<br />

between two chip carriers stacked vertically. The cooling<br />

solution is designed such that no external fluidic<br />

interconnections are required to assemble the package on the<br />

mother board. Other components such as pump, heat<br />

exchanger have been assembled along <strong>with</strong> the 3-D package.<br />

Integrated cooling solution design<br />

The <strong>3D</strong> package consists <strong>of</strong> two carriers assembled one<br />

over other <strong>with</strong> silicon interposer. Each carrier is mounted<br />

<strong>with</strong> 10mm x10mm chip <strong>with</strong> heating and temperature<br />

sensing elements. Heat transfer enhancement structure is<br />

designed as a part <strong>of</strong> the carrier to extract the heat generated<br />

by chip. The stacked module is then attached to a printed<br />

circuit board using 300µm solder balls. The footprint <strong>of</strong> the<br />

<strong>3D</strong> package is 15mm by 15mm <strong>with</strong> a height <strong>of</strong> 2.8mm. The<br />

liquid cooling solution consists <strong>of</strong> the following components<br />

in addition to the package: (1) A mini-pump (2) an adapter<br />

for flow distribution and (3) a heat exchanger. A schematic <strong>of</strong><br />

the cooling solution is shown Fig. 1. Electrical and fluidic<br />

connectivity between carriers is achieved by <strong>TSV</strong>. In this<br />

arrangement, heat from the chip is transferred to the carrier,<br />

and it is transported to the heat exchanger to be rejected to the<br />

ambient.<br />

Heat Exchanger<br />

Chip 1<br />

Carrier 1<br />

Interposer<br />

<strong>TSV</strong><br />

Fluid out<br />

Mini Pump<br />

PCB<br />

Fluid in<br />

Mechanical<br />

connector<br />

Gasket<br />

Adaptor<br />

Chip 2<br />

Carrier 2<br />

Solder ball<br />

Fig. 1 Scheme <strong>of</strong> the integrated liquid cooling system for <strong>3D</strong><br />

stacked module (non-scaled)<br />

978-1-4244-4476-2/09/$25.00 ©2009 IEEE 1153 2009 Electronic Components and Technology Conference


Thermal design <strong>of</strong> the chip carrier and <strong>3D</strong> module has<br />

been done using commercial CFD package ICEPAK. Onedimensional<br />

thermal resistance network model was used as a<br />

first order estimate <strong>of</strong> various thermal resistances in the<br />

package and their contribution to the overall thermal<br />

resistance. Chip interconnection thermal resistance is<br />

calculated based on area-averaged conductivity <strong>of</strong> solder<br />

balls and underfilling material. The one dimensional model<br />

predicted a junction temperature <strong>of</strong> 98°C based on an inlet<br />

temperature <strong>of</strong> 50°C. The resistance <strong>of</strong> the chip interconnect<br />

is 57% <strong>of</strong> the overall thermal resistance, remaining 43% is<br />

chip carrier thermal resistance. Hence, we investigated<br />

enhancement techniques to improve the heat transfer and<br />

reduce the R interconnects and R carrier .<br />

Liquid<br />

Inlet<br />

Fig. 2 One dimensional thermal resistance model<br />

S<br />

gen,thermal<br />

Chip<br />

Carrier <strong>with</strong> micro-channel<br />

2<br />

Q <br />

<br />

R<br />

T<br />

ref <br />

*<br />

S S<br />

heat sin k<br />

gen,thermal<br />

* S<br />

Liquid<br />

Outlet<br />

S<br />

gen,dP<br />

gen,dP<br />

<br />

R Interconnection<br />

R Carrier<br />

dP * G<br />

T<br />

ref<br />

respective entropy generation. The trend in Fig 3 showed that<br />

optimum microchannel spacing is found to be in the region <strong>of</strong><br />

80 microns and 110microns for the microchannel depth<br />

investigated. Microchannel size <strong>of</strong> 100µm width and 350µm<br />

depth has been taken based on the balance between the<br />

thermal resistance and pressure drop.<br />

A common micro-channel arrangement reported in the<br />

literature is single inlet / outlet arrangement (S1). The flow<br />

enters from one end <strong>of</strong> the channels and flow through the<br />

entire length <strong>of</strong> the channels and is collected at the outlet.<br />

This is a parallel plate type <strong>of</strong> micro-channel heatsink which<br />

has some disadvantages. The pressure drop across a channel<br />

is high due to the long flow length. The heat transfer per unit<br />

length is also lower as the developed region is a substantial<br />

portion <strong>of</strong> the total flow length.<br />

The flow distribution across channels is governed by<br />

pressure differences between the supply and return plenum.<br />

The conversion <strong>of</strong> static and dynamic pressure changes the<br />

pressure pr<strong>of</strong>ile <strong>with</strong>in the plenum. Hence, it is desirable to<br />

distribute flow such that the heat transfer per unit area <strong>with</strong>in<br />

the channels is the same to minimize temperature variation.<br />

Therefore a split flow arrangement (dual-port) has been<br />

developed for this work. Schematic <strong>of</strong> the single port and<br />

dual -port design is as shown in Fig 4. There are two fluidic<br />

inlets and two outlets. This arrangement has the benefit <strong>of</strong><br />

reducing the flow length, <strong>with</strong> the thermal developing length<br />

being a substantial portion <strong>of</strong> the channel length. The mixed<br />

mean temperature (T m ) <strong>of</strong> the cooling liquid in the channels is<br />

lower and hence heat rejection occurs across a smaller<br />

temperature difference (T w -T m ). As frictional pressure drop is<br />

proportional to flow length (4fL/D h ), the shorter length will<br />

reduced the pressure drop significantly.<br />

Fig. 3 Micro-channel optimization<br />

A chip carrier has been designed <strong>with</strong> microchannels to<br />

remove the heat from the chip to the cooling liquid.<br />

Numerical analysis is performed to optimize the carrier<br />

thermal resistance. Parametric study on channel dimensions is<br />

performed to understand its impact on the carrier<br />

performance. Pressure drop and thermal resistance <strong>of</strong><br />

different channel spacing versus channel depth between<br />

250µm to 400µm have been analyzed. A constant flow rate <strong>of</strong><br />

water at 200ml/min is taken for the analysis. Microchannel<br />

geometry is optimized by considering viscous and thermal<br />

effects simultaneously [7]. The entropy generation due to<br />

hydraulic losses and heat transfer are combined as an<br />

optimization parameter S*, given by the product <strong>of</strong> the<br />

Fig. 4 Chip carrier design: (Left) Single port design, (Right)<br />

Dual-port design<br />

We evaluated two designs <strong>of</strong> the split flow arrangement<br />

such as, design 1 (D1) has a constant supply and return<br />

plenum width and design 2 (D2) has reducing width <strong>of</strong> supply<br />

plenum. Due to the symmetry in geometry and boundary<br />

conditions <strong>of</strong> the carrier design, a quarter-model was<br />

developed for the numerical analysis. The fin thickness <strong>of</strong><br />

50m, the channel width <strong>of</strong> 100m and channel depth <strong>of</strong><br />

350m is taken for the analysis. The supply plenum width<br />

is150m and the return plenum is 250m. The inlet<br />

temperature <strong>of</strong> the water is assumed to be 50ºC for all the<br />

analysis.<br />

Numerical simulation results have been compared among<br />

the three designs. Temperature distribution <strong>of</strong> the chip is<br />

1154 2009 Electronic Components and Technology Conference


shown in Fig. 5. Table 1 showed the pressure drop across the<br />

carrier and the die temperature pr<strong>of</strong>ile. Comparing between<br />

the single port and the dual-port design, it is very clear that<br />

the dual-port designs has lower thermal resistance and<br />

reduced pressure drop. As the pump size is proportional to<br />

pressure drop, a smaller pump can be selected for the cooling<br />

design. Comparing D1 and D2, D2 has the lower thermal<br />

resistance (peak chip temperature) and small temperature<br />

variation. Thermal performance improvement is due to the<br />

uniform heat picked up in each channel. Flow distribution in<br />

each channel has been analyzed for the three designs. For S1,<br />

the flow distribution is better, but the long channel length<br />

leads to high temperature gradient. Design D1 has nonuniform<br />

flow distribution among the channels, which reduced<br />

the microchannel effectiveness. For D2, the flow distribution<br />

is uniform, except for the first 3 channels. Hence, we have<br />

selected design D2 for the fabrication and characterization.<br />

Fig. 5 Temperature contours on chip at 100ml/min: (Left) S1,<br />

(Top Right) D1, (Bottom Right) D2<br />

bonding, electrical interconnection through the carrier is<br />

made by <strong>TSV</strong> <strong>with</strong> on wall metallization.<br />

The chip carrier fabrication process begins <strong>with</strong> an 8”,<br />

725µm thick wafer (Fig. 6a). A 3µm thick silicon dioxide<br />

(SiO 2 ) layer is deposited on the wafer by plasma enhanced<br />

chemical vapor deposition (PECVD) and the <strong>TSV</strong>/ microchannels<br />

are patterned (Fig. 6b). This is followed by a 2µm<br />

thick photoresist coating and patterning for the via (Fig. 6c).<br />

As the depth <strong>of</strong> the <strong>TSV</strong> and micro-channels are different, the<br />

<strong>TSV</strong> is etched to 230µm deep, then the photoresist mask is<br />

stripped (Fig. 6d). Then <strong>TSV</strong> and micro-channels are etched<br />

using SiO 2 mask further to the depth <strong>of</strong> 170µm (Fig. 6e). The<br />

SiO 2 layer is then stripped by BOE (Fig. 6f). The backside <strong>of</strong><br />

the wafer is then grinded to 400µm thickness to expose the<br />

vias (Fig. 6g). A 1µm thick SiO 2 is then deposited on the<br />

channel side and back side <strong>of</strong> the wafer (Fig. 6h). Under<br />

Bump Metallization (UBM) is deposited and patterned on the<br />

channel side and back side <strong>of</strong> the wafer (Fig. 6i & 6j). 1µm<br />

thick SiO 2 is deposited on the back side and patterned for the<br />

carrier passivation layer (6k). The fluidic ports are then laser<br />

drilled (Fig. 6l). The Au/Sn solder is then deposited on the<br />

channel side and patterned (Fig.6m). The carrier fabrication<br />

process is completed by bonding two such wafers together at<br />

350°C for 15 minutes <strong>with</strong> a compressive strength <strong>of</strong> 4.7MPa<br />

(Fig. 6n). The UBM material used is Ti/Cu/Ni/Au <strong>with</strong><br />

thickness <strong>of</strong> 0.1μm, 1μm, 0.5μm and 0.1μm, respectively.<br />

The electrical <strong>TSV</strong> are connected by sputtering the UBM<br />

layer from front and back side <strong>of</strong> the wafer. AuSn-solder<br />

system is selected as the bonding material <strong>of</strong> the wafers.<br />

Generally 80wt%Au - 20wt%Sn solder is widely used<br />

because <strong>of</strong> its advantages, such as high reliability, high<br />

strength, high corrosion resistance, no thermal fatigue and<br />

allows soldering in flux-less processes. A sealing ring <strong>of</strong><br />

300um width around the micro-channels and fluidic ports has<br />

been designed to isolate the electrical <strong>TSV</strong> from the cooling<br />

liquid.<br />

Table 1: Thermal simulation results<br />

Flowrate<br />

(ml/min)<br />

100<br />

200<br />

Design<br />

Pressure<br />

drop<br />

(mbar)<br />

Maximum<br />

Temperature<br />

(°C)<br />

Temper<br />

ature<br />

variation<br />

(°C)<br />

S1 158.1 98.7 22.5<br />

D1 55.45 97.2 8.6<br />

D2 76.7 93.4 9.4<br />

S1 398.7 92.1 18.5<br />

D1 169.7 91.8 9.6<br />

D2 253.1 87.2 7.8<br />

Chip Carrier Fabrication<br />

The bottom carrier (CR1) and top carrier (CR2) has<br />

mostly the same construction except that CR1 has pads for<br />

PCB. The chip carrier has copper <strong>TSV</strong> for electrical<br />

interconnection and hollow <strong>TSV</strong> for fluidic circulation. <strong>TSV</strong><br />

are designed along the periphery <strong>of</strong> the carrier at a pitch <strong>of</strong><br />

500 μm. Totally there are 144 <strong>TSV</strong> for electrically<br />

interconnection and four hollow via for fluidic ports. After<br />

Fig. 6 Process steps involved in carrier fabrication<br />

1155 2009 Electronic Components and Technology Conference


The bonded carrier should have good bonding strength to<br />

<strong>with</strong>stand the dicing force and liquid pressure. The bonded<br />

carrier is sheared using DAGE-SERIES-4000-T, the shear<br />

strength value measured for 20 different samples ranged from<br />

17.8 MPa to 35.1 MPa, and an average value <strong>of</strong> 27.2 MPa<br />

and a standard deviation <strong>of</strong> 2.2 are obtained. The shear<br />

failure mode is silicon crack, the bonded interface is intact.<br />

Mini- Pump<br />

Heat Exchanger<br />

Flexible Tube<br />

Adaptor<br />

PCB<br />

Fig. 9 Photograph <strong>of</strong> integrated cooling solution<br />

Fig. 7 Cross section <strong>of</strong> the carrier <strong>with</strong> embedded microchannels<br />

<strong>3D</strong> Package Assembly<br />

The bonded carrier wafer is diced to 15mm x 15mm size<br />

using mechanical dicing tool. The assembly processes<br />

involves pick and place <strong>of</strong> the chip on the carrier and<br />

reflowed. Then solder balls <strong>of</strong> 300µm diameters are placed<br />

on the carrier 1 and reflowed. Two types <strong>of</strong> solder are used in<br />

the assembly namely SnAgCu reflowed at 255°C for 30s<br />

(pr<strong>of</strong>ile 1) and SnPb Solder reflowed at 220°C for 30s<br />

(pr<strong>of</strong>ile 2). The underfill is dispensed after the chip<br />

attachment <strong>with</strong> the carrier and carrier to the PCB.<br />

Flip-Chip<br />

Carrier 2<br />

Cooling solution performance characterization<br />

A schematic diagram <strong>of</strong> the experimental setup for<br />

hydraulic characterization is shown in Fig. 10. A variablespeed<br />

gear pump was used to provide the pressure head. A<br />

filter <strong>with</strong> 10 µm mesh filter element was used after the pump<br />

to remove particles suspended in the liquid. A flow meter<br />

was connected in the closed loop to measure the flow rates.<br />

The flow meter was calibrated in-house to achieve a<br />

measurement error <strong>with</strong>in 2%. The pressure drop across the<br />

<strong>3D</strong> package section was measured <strong>with</strong> a piezo-resistive<br />

pressure transducer. The uncertainty at the full range was<br />

estimated to be <strong>with</strong>in 0.2%.<br />

Pump<br />

Heat Exchanger<br />

Solder<br />

Interposer<br />

Carrier 1<br />

Filter<br />

PCB<br />

Fig. 8: Schematic <strong>of</strong> the <strong>3D</strong> package assembly<br />

Solder ball<br />

Flow Meter<br />

Pressure Gauge<br />

The fluidic interconnection at difference interfaces is one<br />

<strong>of</strong> the biggest challenges in this work. As the size <strong>of</strong> <strong>3D</strong><br />

package becomes smaller, the available area on the periphery<br />

<strong>of</strong> the package for the fluidic interface also becomes smaller.<br />

An adaptor is designed to distribute the fluid between heat<br />

exchanger, mini pump and the carriers. Other purpose for the<br />

adaptor is split the flow into two inlet ports. A cavity <strong>of</strong><br />

1.5mm depth precisely machined on bottom side <strong>of</strong> the<br />

adaptor to align <strong>with</strong> the fluidic ports on the <strong>3D</strong> package. On<br />

the top side <strong>of</strong> the adaptor, one inlet port is fabricated to<br />

deliver the fluid from the mini pump to the package and one<br />

outflow port to convey the fluid from the package to the heat<br />

exchanger. The two ports are fixed <strong>with</strong> ¼” tap and flexible<br />

tube is used for the connection. The fluidic interface between<br />

the adapter and the package is sealed using rubber gasket.<br />

The integrated cooling solution is shown in Fig. 9.<br />

<strong>3D</strong> Package<br />

Fig. 10: Schematic <strong>of</strong> the test set-up<br />

As a first step, leakage testing is conducted by running<br />

the system at the maximum pressure condition (flow rate is<br />

400 ml/min) for 30 minutes. No leakage was observed during<br />

this period, which indicates that the sealing is good. Then the<br />

total pressure drop due to adaptor and <strong>3D</strong> package was<br />

measured. Then pressure drop due to the adaptor alone was<br />

measured by removing the <strong>3D</strong> package. The pressure drop in<br />

the <strong>3D</strong> package is obtained by subtracting the adaptor<br />

pressure drop from the measured total pressure drop. In<br />

addition, the pressure drop <strong>of</strong> the heat exchanger was<br />

measured separately by replacing the adaptor and <strong>3D</strong> package<br />

1156 2009 Electronic Components and Technology Conference


<strong>with</strong> the heat exchanger. The system pressure drop comprises<br />

<strong>of</strong> head losses from (a) <strong>3D</strong> package (b) Adapter and (c) Heat<br />

exchanger. Losses in tubes and fittings are small due to the<br />

lower velocities <strong>with</strong>in and ignored. The average pressure<br />

drop <strong>of</strong> five packages is plotted in Fig 11. The dual- port<br />

carrier design helps to lower the total pressure drop in the<br />

package, <strong>with</strong> less than 200mbar at 400ml/min in a two<br />

stacked package. A maximum <strong>of</strong> 400ml/min is required for<br />

the package cooling. A miniature pump based on this<br />

pressure head and flow requirements has been selected. The<br />

miniature pump is only 16mm height, which meets the<br />

package height requirements.<br />

Pressure drop (mbar)<br />

250<br />

200<br />

150<br />

100<br />

50<br />

Pressure Drop in <strong>3D</strong> Package<br />

0<br />

100 150 200 250 300 350 400 450<br />

Flowrate (ml/min)<br />

Fig. 11 Pressure drop characterization results<br />

Chip interconnection thermal resistance is measured and<br />

compared <strong>with</strong> the simulation result. A thermal test chip <strong>of</strong><br />

10mm by 10mm size is attached on a large silicon substrate<br />

(22mm by 22mm). The assembly is then mounted onto a cold<br />

plate and a thin layer <strong>of</strong> thermal interface material is applied<br />

in between them. On the test chip, the diode temperatures are<br />

measured are at the middle, left and right corner location. The<br />

cold plate surface and silicon substrate surface temperature<br />

are also measured using thermocouples. A numerical model<br />

has been developed similar to the experimental setup to<br />

obtain chip and silicon substrate average temperatures, then it<br />

is used for interconnect thermal resistance calculation. The<br />

TIM thickness in the experimental setup is unknown,<br />

therefore the numerical model is solved iteratively by<br />

comparing the cold plate temperature in the model <strong>with</strong><br />

thermocouple reading from the measurement.<br />

The experimental setup to determine thermal<br />

characteristic <strong>of</strong> the <strong>3D</strong> package is similar to the arrangement<br />

shown in Fig. 11. The filter, flow meter and pressure gauge<br />

have been removed from the closed loop. Single and two<br />

stack package have been tested. For the stacked module, the<br />

bottom and top chip is powered up from 40W to 100W. The<br />

water inlet and outlet temperatures are measured to quantify<br />

the energy balance. All the tests have been performed <strong>with</strong><br />

water flowing at 200ml/min for each stack. For thermal<br />

resistance calculation, arithmetic mean <strong>of</strong> the three diodes in<br />

the chip is used to represent the average chip temperature. Fig<br />

12 shows average temperature rise <strong>of</strong> the chip from the<br />

cooling water inlet temperature <strong>with</strong> heat load from 40W to<br />

100W. Fig 13 shows thermal resistance <strong>of</strong> the <strong>3D</strong> package.<br />

Temp rise (ºC)<br />

70<br />

65<br />

60<br />

55<br />

50<br />

45<br />

40<br />

35<br />

30<br />

25<br />

20<br />

15<br />

10<br />

5<br />

Average Chip Temperature Rise<br />

20 30 40 50 60 70 80 90 100 110<br />

Power (W)<br />

Fig. 12 Temperature rise <strong>of</strong> the chip verses power dissipation<br />

Thermal Resistance (ºC/W)<br />

0.8<br />

0.7<br />

0.6<br />

0.5<br />

0.4<br />

0.3<br />

0.2<br />

0.1<br />

0<br />

Thermal Resistance<br />

Fig. 13 Total thermal resistance <strong>of</strong> the <strong>3D</strong> package<br />

The <strong>3D</strong> package total thermal resistance based on test is<br />

0.577±6% °C/W. The thermal resistance is calculated based<br />

on average temperature rise on the chip from inlet liquid<br />

temperature. From the experimental results, higher<br />

temperature rise has been recorded on the chip compared to<br />

the modeling results. The overall thermal resistance measured<br />

by experiment is 0.577°C/W compared to 0.41°C/W by<br />

simulation. The overall thermal resistance is broken down<br />

into R interconnects and R carrier to understand the contribution <strong>of</strong><br />

each resistance to the total. R interconnects thermal resistance <strong>of</strong><br />

0.207°C/W is found experimentally compared to 0.229°C/W<br />

by simulation <strong>with</strong> an absolute error <strong>of</strong> 10%. The test chip<br />

used for the package thermal characterization contains only<br />

400 solder bumps. Therefore R interconnects is large, which can<br />

be reduced significantly by increasing number <strong>of</strong> solder<br />

bumps.<br />

Table 2: Comparison <strong>of</strong> thermal resistance<br />

Board 1<br />

Board 2<br />

20 30 40 50 60 70 80 90 100 110<br />

Power (W)<br />

Board 1<br />

Board 2<br />

Model Experiment Error (%)<br />

R th (°C/W) 0.410 0.577 44.3<br />

1157 2009 Electronic Components and Technology Conference


The experimental and simulation results <strong>of</strong><br />

hydraulic/thermal performances <strong>of</strong> the carriers are showing<br />

several discrepancies. The thermal resistance measured is<br />

0.377ºC/W compared to 0.21ºC/W by simulation, which is<br />

44% difference. Possible reason for the differences in<br />

modeling and experimental results can be attributed to flow<br />

imbalance in the lower and upper sack <strong>of</strong> the <strong>3D</strong> module due<br />

to bubbles trapping, other flow obstruction. The second<br />

reason can be attributed to flow allocation between the two<br />

inlet ports in carrier. There is also a possibility that more flow<br />

through one port compared to other due to air bubble<br />

clogging or flow obstruction by the sealing ring.<br />

Conclusions<br />

In this research work, a novel liquid cooling solution has<br />

been developed for <strong>3D</strong> package <strong>with</strong> integrated cooling<br />

components like heat exchanger, pump, electrical and fluidic<br />

connectivity. The liquid cooling solution is based on<br />

microchannel heat sink design. The dual-port microchannel<br />

arrangement maximized the heat transfer enhancement,<br />

minimized temperature variation in the chip and lowered the<br />

pressure drop. A chip carrier <strong>with</strong> embedded micro-channels<br />

and fluidic manifolds has been developed. The chip carrier<br />

has been tested up to a flowrate <strong>of</strong> 400 ml/min and good<br />

sealing <strong>of</strong> the fluidic path was achieved. <strong>3D</strong> package thermal<br />

performance had also been characterized; the chip is powered<br />

up to 100 W / chip. Overall thermal resistance <strong>of</strong> the chip<br />

carrier is 0.577°C/W compared to simulation result <strong>of</strong><br />

0.41°C/W. Some important results <strong>of</strong> the research work are<br />

summarized below:<br />

1. Unique design <strong>of</strong> a silicon carrier <strong>with</strong> embedded microchannels<br />

for heat transfer enhancement<br />

2. Chip carrier <strong>with</strong> tapered micro- fin structures for<br />

uniform flow distribution and small temperature<br />

variation <strong>with</strong>in the chip (< 10°C @ 100 Watts / cm 2<br />

heat flux)<br />

3. Dual-port fluidic design to minimize the system pressure<br />

drop (< 500 mbar @ 400ml/min)<br />

4. Chip carrier design <strong>with</strong> copper through-silicon via for<br />

electrical interconnection and through-silicon hollow via<br />

for the fluidic circulation<br />

5. Fluidic sealing design and hermetic joint using Au/Sn<br />

solder for high pressure flow requirements up to 0.8 Bar<br />

6. Micro-to-Macro fluidic interconnection method to<br />

connect 500um size holes in the module <strong>with</strong> 4mm hole<br />

in the pump<br />

7. Integrated liquid cooling design <strong>with</strong> miniature<br />

exchanger and pump mounted on the module giving<br />

overall module foot print <strong>of</strong> 50mm x 50mm<br />

Acknowledgments<br />

The authors acknowledge the financial grant from<br />

DARPA under agreement number HR0011-06-2-0007 for<br />

this project. The support from the process team and<br />

management team at <strong>Institute</strong> <strong>of</strong> Microelectronics is also<br />

greatly appreciated.<br />

References<br />

1. Wu, L., Wang, Yu-Po, Kee, S. C., Wallace, B., Hsiao, C.<br />

S., Yeh, C. K., Her, T. D., Lo, R., “The Advent <strong>of</strong> 3-D<br />

Package Age”, Proc 26 th IEEE/CPMT Int’l Electronic<br />

Manufacturing Technology Symposium, Santa Clara,<br />

2000, pp. 102-107.<br />

2. http://www.itrs.net/Links/2007ITRS/Home2007.htm<br />

3. Issam Mudawar, “Assessment <strong>of</strong> high-heat flux thermal<br />

management schemes,” IEEE Trans. On Components and<br />

<strong>Packaging</strong> Technologies, Vol 24, Issue 2, June 2001, pg<br />

122-141.<br />

4. J. Koo, S. Im, L, Jiang, and K. Goodson, “Integrated<br />

Microchannel Cooling for Three-Dimensional Electronic<br />

Circuit Architectures”, J. Heat Transfer, 2005, Vol. 127,<br />

49-58.<br />

5. X. Chen, K. Toh, and J. Chai, “Direct Liquid Cooling <strong>of</strong> a<br />

Stacked Multichip Module”, Proc. Electronics <strong>Packaging</strong><br />

Technology Conference, 2002, 380-384.<br />

6. R.H.W. Pijnenburg, R. Dekker, C.C.S. Nicole, A. Aubry,<br />

E.H.E.C. Eummelen,” Integrated micro-channel cooling<br />

in silicon,” Solid-State Device Research conference,<br />

2004.<br />

7. J.R. Culham, Y.S. Muzychka, “ Optimisation <strong>of</strong> Plate Fin<br />

Heat Sinks Using Entropy Generation Minimization”<br />

IEEE CPT Jun 01, Vol 2, Pg 159-165<br />

1158 2009 Electronic Components and Technology Conference

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