Vapor Cooling in Electronicsa

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    Outline Benefits Disadvantages History Basic operation Engineering Design

    Cold plate Refrigerants Capillary tube Condensation

    Product Reliability Current applications:

    Supercomputer and Mainframe Cooling Current researc:

    Microscale !CRS

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    Benefits "llo#s cooling to belo# ambient temperatures$ increasing

    performance$ reliability$ and allo#ing operation in igertemperatures%

    Hig COP &around ' to ()%

    "bility to remove very large eat loads% *idely available+ compressor and fan only moving parts$

    stable$ and reliable% &moran$ ',,-)% .o# mass flo# rate of refrigerant needed% "bility to transport eat a#ay from its source%

    COP up to ( times greater tan termoelectric coolers ormore%

    &peeples$ ',,-)

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    BenefitsSub ambient temperature operation allo#sCMOS &complementary/symmetry0metal/o1ide semiconductor) transistors to s#itc on

    and off faster &peeples$ ',,-)%CMOS circuits are a ma2or class ofintegrated circuit and includemicroprocessors$ microcontrollers$ and oter

    digital logic circuits &*i3ipedia$ ttp:00en%#i3ipedia%org0#i3i0CMOS) %

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    Benefits 4e follo#ing pysical parameters favor lo# temperature

    operation: carrier mobility$ andjunction leakage% "ltoug at lo# temperatures tere is an increase in te

    failure rates due to ot carriers$ overall failure rates

    decrease at lo#er temps due to te overall increasedcaracteristics mentioned previously &Moran$',,-)% Definitions:

    Carrier mobility/ velocity of carge carriers in a solid material #it an electric field

    applied to it&*i3ipedia$ ttp:00en%#i3ipedia%org0#i3i0Electron5mobility)%

    Hot carriers/ ig energy carriers &Moran$',,-)% 6unction lea3age/undesirable conductive pats in certain components$ for

    instance$ in capacitors% "lso$ a pat#ay troug #ic electric discarge mayslo#ly ta3e place (IEEE Standard Dictionary of Electrical and Electronics Terms).

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    Benefits

    Muc li3e eat pipes$ vapor compressioncoolers use te ig eat of vapori7ations of te

    #or3ing li8uid to remove large amounts of eat% 4erefore$ lo# mass flo# rates re8uired%"dvantage over a cilled li8uid loop tat re8uires a muc

    iger mass flo# rate%

    Muc li3e eat pipes$ !CCs use te ig eat of vapori7ation

    of li8uids to transport large amounts of eat$ tus lo#amounts of li8uid are re8uired% Ho#ever$ in cilled li8uid loopcoolers$ te li8uid is eated but not necessarily evaporated%

    &Cengel and Boles$ ',,')

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    Disadvantages

    4e cost of employing te cooling system maybe -,/',9 of te cost of te entire system%

    .arge space and input po#er% 4e disadvantages of te cooling system as tobe #eiged #it te large advantages% " lot oftimes$ traditional metods of cooling li3e aircooling is not feasible so a !CC is re8uired%

    Ho#ever$ if te cooling re8uirements can besatisfied #it traditional tecni8ues$ tetraditional tecni8ue are te preferred coolingmetod &Moran$ ',,-)%

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    History 4e vapor compression refrigerator #as first

    proposed in -,; and a model #as constructed in-(,?s companies li3e "MD$ Sun

    Microsystems$ @BM$ and SAS 4ecnologies ad allused !apor Compression cooling%

    &Scmidt et al%$ ',,')

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    Basic Operation

    &Peeples$',,-)

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    Basic Operation Ideal cycle

    -/' 4e #or3ing refrigerant$ a saturated vapor$ is carriedtroug te suction tube to te compressor% 4ecompressor compresses te saturated vapor into asupereated vapor #ic is ten passed to te condenser%

    '/( 4e eat of te ot and ig pressure vapor is releasedinto te environment from te condenser% 4e #or3ing gasis transformed into a saturated li8uid%

    (/< 4e li8uid is pumped troug a capillary tube or atermal e1pansion valve into te evaporator$ dropping

    significantly in temperature% 4e #or3ing fluid is a saturatedmi1ture%

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    Basic Operation

    ' represents te actual

    position of te state% 's

    represents te position of

    te state if it #ereirreversible%

    @n te ideal case: -' isentropic &sconst)

    '( isobaric &Pconst) (< isentalpic &const)

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    Basic Operation 4e eat absorbed by te evaporator &in) released from te

    condenser &out)$ and actual and isentropic #or3 input by te

    compressor can be determined from te e8uations:

    4e efficiency of te compressor is given by:

    *ere is te entalpy at various states$ te subscripts s and a

    refer to isentropic and actual$ and # refers to #or3%

    12

    12

    hh

    hh

    w

    w s

    a

    s

    c

    ==

    )(

    )(

    )(

    )(

    12

    12

    23

    41

    hhmW

    hhmW

    hhmQ

    hhmQ

    aa

    ss

    out

    in

    =

    =

    =

    =

    &Cengel and Boles$ ',,')

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    Basic Operation

    Actual cycle 4e deviation of te ideal cycle to te actual cylce is

    due to irreversibilities+ mainly due to fluid friction/

    causing pressure drops and eat transfer to tesystem or te environment%

    @n te ideal cycle te state of te refrigerant isprecisely 3no#$ for e1ample$ at stage - te refrigerantis a saturated vapor% Ho#ever$ in actuality te state ofte refrigerant may not be precisely 3no#n and isusually a supereated vapor%

    &Cengel and Boles$ ',,')

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    Basic Operationote tat te pressure drops bet#een stages /-$ '/($

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    Basic Operation

    &Cengel and Boles$ ',,')

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    Basic Operation

    4e Coefficient of performance of te !CR is te ratio of eat into te

    evaporator to #or3 put into te compressor% Fenerally$ te COP is

    around ' to (%

    4e COP can be determined by finding te ratio of te entalpies

    bet#een te trottling valve and evaporator and bet#een te

    evaporator and te compressor%

    c

    e

    W

    QCOP

    =

    12

    41

    hh

    hhCOP

    =

    &Cengel and Boles$ ',,')

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    Basic Operation 4e most efficient refrigeration cycle is tat of a Carnot

    refrigerator%

    4e coefficient of performance of te Carnot refrigerator

    gives te ma1imum performance bet#een t#o ot and and

    cold temperatures% 4is value can be compared to te actual COP to

    determine o# close to ideal te refrigerator is operating%

    ote tat te Carnot cycle is a reversible cycle% Reversible

    cycles are cycles tat do not generate any entropy due tofriction$ eat transfer$ etc% Gor a reversible cycle:

    L

    H

    reversL

    H

    T

    T

    Q

    Q=

    &Cengel and Boles$ ',,')

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    Basic Operation

    4e coefficient of performance for a Carnot cycle is:

    ote: te COP increases as te ratio of 4H04.decreases%

    4erefore$ #e #ant 4Hand 4.to be as close as possible%

    sually$ 4.is specified and 4Hcan be altered% 4e

    reason for 4H0 4. affecting COP is tat for a given 4.tegreater te 4Hte greater te amount of #or3 input$

    decreasing COP%

    1/

    1

    1/

    1

    =

    =

    LHLH

    CarnotTTQQ

    COP

    &Cengel and Boles$ ',,')

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    Basic Operation

    4e area enclosed in te 4S diagramgenerally describes te net eat transfer

    and te #or3 of te system% Gorrefrigeration$ #or3 input lo#ers te COPfor a given eat re2ection+ terefore$altering te states of te cycle to get a

    smaller enclosed area #ill increaseperformance%

    &Cengel and Boles$ ',,')

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    Engineering Foals

    4e design of a cost/effective and efficient !CCinvolves te follo#ing considerations:

    Cold surfaces can not be allo#ed to collectcondensate from te air%4e most suitable refrigerant for te given

    application$ as #ell as te tubing to supply andremove te refrigerant$ must be cosen%

    Compressor and condenser design%4e cold plate must efficiently lift eat from te device

    to be cooled%

    &Peeples$',,-)

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    Cold Plate0Evaporator

    4e cold plate &evaporator) is a eat e1cangedevice #ic transfers eat from te eat sourceto te #or3ing fluid%

    Cold plate design must assure efficient eattransfer from te device being cooled to terefrigerant inside te cold plate%

    4e cold plate must be fabricated from tin andtermally conductive material to minimi7e termalresistance #ile maintaining structural stability%

    4e mating surface bet#een te cold plate andte eated body must be flat and smoot tominimi7e contact resistance%

    &Peeples$',,-)

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    Refrigerant Gluids

    4e refrigerant?s pysical properties determineits evaporating temperature at a specifiedoperating temperature$ as #ell as$ its capacity totransport eat%

    4e #ell 3no#n refrigerants R/-(

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    Refrigerant Gluids

    *en ma3ing a decision as to #ic refrigerant to use andunder #at pressures to operate te !CR$ consideration ofte refrigerant?s temperature of vapori7ation and condensationsould be considered% @f te temperature of te refrigerant

    doesn?t reac te vapori7ation point &at te operatingpressure) te !CR #ill not #or3 properly% 4o ensure a propereat transfer rate a ; to -, degree Celsius temperaturedifference sould be maintained bet#een te evaporator andte condenser #it te refrigerant%

    4e ne1t slide so#s te P/4 curves of R/

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    Refrigerant Gluid Saturation

    Pressure and 4emperature

    &Peeples$',,-)

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    Capillary 4ube

    4e capillary tube as te function of transporting te#or3ing li8uid from te condenser to te evaporator%

    4e small diameter and long lengt of te tube produces

    a large pressure drop% Refrigerants cosen ave a large 6oule/4omson

    coefficient$ #ic tells us o# muc te temperaturedrops as te pressure drops at constant entalpy%

    Since pressure drops create performance losses carefuldesign must be ta3en so tat te tube lengts anddiameters are minimal%

    &Heydari$ ',,')

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    Condensation

    Condensation$ muc li3e in 4EC$ is a

    problem because te surfaces of te !CR

    may be lo#er tan te de# point% Since #ater is a7ardous to electronic

    assemblies$ condensation must be

    minimi7ed by insulating surfaces from airin spot/cooling applications% &Peeples$',,-)

    More on sealants later on in te slides%

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    Product Reliability

    Electro/mecanical

    systems generally ave

    product life cycles called

    Ibattub curvesJ% 4e curve as tree

    distinct regions @nfant mortality/ rate of

    failure decreases #it time ormal use/rate of failure

    relatively constant

    *ear out/ rate of failure

    increases #it time% &Peeples$',,-)

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    @mproving Performance

    @n some applications te eat re2ection demands&efficiency or amount) are iger tan #at canbe andled by a vapor compression cyclerunning on a regular cycle% @n tese cases$modifications of te cycle must occur%

    .i3e previously mentioned$ modifying te 4H04.to get tem as as lo# as possible #ill increaseperformance but larger modifications may needto be made%

    &Cengel and Boles$ ',,')

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    @mproving Performance

    "n e1ample is a cascade cycle$ #ic performs terefrigeration process in t#o cycles tat are inseries% 4is is useful in situations &industrial)$ #ere

    tere is a large temperature difference bet#een teot and cold side for one cycle to be practical%

    @f te fluid used in te cascade system is te same$te eat e1canger can be replaced by a mi1ing

    camber$ 3no#n as a flas camber #ic asbetter eat transfer caracteristics%

    &Cengel and Boles$ ',,')

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    Cascade Refrigeration

    &Cengel and Boles$ ',,')

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    Refrigeration System #0 Glas

    Camber

    &Cengel and Boles$ ',,')

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    Supercomputer and Mainframe

    Cooling 4e e1tremely ig cooling demands of

    mainframes and supercomputers are ideal

    applications for !CRs because otercooling systems can not provide te

    necessary cooling capacity% "n e1ample of

    is @BM?s F< mainframe &so#n on te ne1tslide)

    &Scmidt et al%$',,')

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    Supercomputer and Mainframe

    Cooling

    &Scmidt et al%$',,')

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    Supercomputer and Mainframe

    Cooling 4e bul3 po#er assembly at te top

    provides ';, volts dc to te mainframe%

    Belo# te bul3 po#er is te centralelectronic comple1 #ere te MCM

    &multicip module) is located% 4e MCM

    ousing te -' processors%

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    Supercomputer and Mainframe

    Cooling Belo# te MCM are blo#ers tat provide air cooling for

    all of te components in te processors e1cept for teprocessor module$ #ic is cooled by refrigeration%

    Belo# te blo#ers are t#o modular refrigeration units&MRs/te !CR) #ic provide cooling via teevaporator mounted on te processor module%

    @n te bottom of te mainframe are te input0 output&@0O)connections and t#o blo#ers% 4e blo#ers coolte @0O connections$ as #ell as$ provide te cooling forte condenser of te MRs%

    &Scmidt et al%$',,')

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    Multicip Module &MCM)

    4e mainframe?s processing unit$ MCM$ is

    constructed as follo#s%

    ote te evaporator above te cips%

    &Scmidt et al%$',,')

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    Modular Refrigeration nit

    &MR) 4e MR &!CR)

    ouses all terefrigeration

    components e1cept teevaporator% 4e MRcontains te: Condenser

    4ermostatic e1pansionvalve

    DC rotary compressor

    &Scmidt et al%$',,')

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    Condensation Protection

    4o avoid moisture condensation onte MCM ard#are$ all te coolingard#are including te evaporator

    copper cold plate is contained inan airtigt metal enclosure #itone open face%

    'K, grams of silica gel desiccant is

    3ept tere to absorb any moisturelea3ing into te enclosure%

    &Scmidt et al%$',,')

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    Condensation Protection

    4e figure on te previous slide also so#s a flat boardtat replaced te planar board in order to test teeffectiveness of various sealants in 3eeping moisture outof te evaporator cavity%

    4e results so# tat te

    Butyl L- rubber sealant

    displayed te best

    sealant caracteristics$

    allo#ing te least amount

    of umidity to enter%

    &Scmidt et al%$',,')

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    Microscale !CRs

    4o utili7e !CRs in laptops$ personal computers$ oroter cooling applications of small si7e$ te !CRsi7e must be reduced to fit #itin a small enclosure%

    4e ne1t section discusses progression in tis area% Since miniature !CRs ave ig eat loads totransfer a#ay$ te condenser and evaporator mustbe designed suc tat tey transfer enoug eat tosatisfy te eat removal demands%

    4e most difficult part in designing a miniature !CRis te compressor%

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    Microscale Evaporators

    Cirac et al% &',,;) suggest using an evaporator #it

    microcannels troug te center as an option to

    miniaturi7e te evaporator% 4e microcannels transfer

    large amounts of eat reducing te evaporator si7eneeded to transfer te eat load from te eat source%

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    Microscale Condenser

    Ciriac et al% also describe a condenser #it

    microcannels troug te center% " eat sin3

    surrounds te outside of te condenser #ile a fan

    blo#s air over te eat sin3%

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    Refrigerant Gluids

    Heydari &',,') performed asimulation #it a miniature !CR#ic included a miniaturecompressor to cool a computersystem%

    4e figure so#s ammonia aste igest COP relative to teoter refrigerants% Ho#ever$#en te refrigerant?s cost$

    environmental impact &o7onedepletion and global #armingpotential)$ and safety issues#ere considered$ Heydariconcluded te optimalrefrigerant to use is R-(

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    Condenser 4emperature and

    Performance Heydari found tat #it

    te computer cip

    2unction temperatureand eat absorbed by

    te evaporator fi1ed$

    decreasing te

    condenser temperaturedecreases te COP%

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    Evaporator 4emperature and

    Performance .astly$ Heydari found tat

    for a fi1ed 2unction

    temperature and te

    amount of eat absorbedby te evaporator fi1ed$

    increasing te evaporator

    temperature increases

    te COP+ but te amountof eat condensed

    decreases%

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    Refrigerant Gluids

    *en it comes to te performance of refrigerants inminiature !CRs$ Pelan et% "l% &',,

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    Refrigerant Gluids

    Pelan et% "l% &',,

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    Refrigerant Gluids

    Gor eac condition$ ammonia as te igestCOP%

    4e iger COP values are due to ammonia?sgreater latent eat of vapori7ation% Ho#ever$ due to ammonia?s greater adverse

    environmental and pysiological effects$ R/-(

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    Microscale !CRs tili7ing !CRs for electronics cooling applications as

    been limited by teir large si7e due to te use oftraditional components li3e pistons$ lin3ages andpressure vessels%

    niversity of @llinois as a D"RP" grant to developminiature !CR?s for use #it cooled military uniforms foruse in desert #arfare% 4is 4ecnology could also beused for electronics applications% Ho#ever$ te miniaturecompressor as been difficult to acieve%

    Researc is ongoing on a Stirling cycle MEMS coolerbeing developed in "S" Flenn%

    &Moran$',,-)

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    Microscale !CRs

    4e Stirling Cycle is muc li3e te vapor

    compression cycle and is so#n belo#%

    &Moran$',,-)

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    Microscale !CRs

    sing diapragms instead of pistons$ te MEMS Stirlingcooler is fabricated #it semiconductor processingtecni8ues to provide a device #it planar geometry%

    4e result is a flat cold surface for e1tracting eat and anopposing flat ot surface for termal dissipation% " typicaldevice #ould be composed of numerous suc cellsarranged in parallel and0or series #it all layers 2oined atte peripery of te device to ermetically seal te#or3ing gas%

    &Moran$',,-)

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    Microscale !CRs

    &Moran$',,-)

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    Microscale !CRs

    4e e1pansion and compressiondiapragms are te only moving parts%

    E1pansion of te #or3ing gas directlybeneat te e1pansion diapragm in eaccycle creates a cold top end for e1tractingeat$ #ile compression at te oterbottom end creates a ot region fordissipating eat%

    &Moran$ ',,-)

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    References Cengel and Boles$ ',,'$ Aunus "%$ Boles$ Micael "% &',,')% Thermodynamics: an Engineering Approach.

    e# Aor3: A: McFra#/Hill% Ciriac$ Glorea+ NCiriac$ !ictor &',,;)% "n alternative Metod for te Cooling of Po#er Microelectronics

    sing Classical Refrigeration%ASME/Pacific im Technical !onference and E"hi#ition on Integration andPac$aging of MEMS% &EMS% and Electronic Systems: Ad'ances in Electronic Pac$aging% pp