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Undergraduate Study of Thermal Condutivity of Metals

Estudodaondutividadetermiademetaisanveldegradua~ao

T. B. Ferrari,S. H. Hara, J. L. Aziani, L.Roha,

E. de Paula and M. Mulato

Departamento deFsiaeMatematia,Fauldadede FilosoaCi^eniase Letrasde Ribeir~aoPreto,

Universidadede S~aoPaulo,Av. Bandeirantes3900, Ribeir~aoPreto, 14040-901,Brazil

Reebidoem7demaio,2002. Aeitoem7dejunho,2002.

Inthisworkweanalyzeanundergraduateexperimentusedtodeterminethethermalondutivity

of metals(K). Weintroduefewmodiations inordertooer thestudentthe hanetoexplore

dierent models,learning thebasisienti methodofdevelopingappropriateand improved

ex-planationsforeahexperimentinordertobetterlinktheoryandempirialresults. Semi-empirial

orretions are introdued inthe system in orderto hek the experimental results aording to

previouslyreportedKvalues.Asspeiasesweuseopper[K=0.92al/(Csm)℄,aluminum

[K=0.49al/(Csm)℄andbrass[K=0.26 al/(Csm)℄ylinders.

Nesse trabalho analisamos um experimento de gradua~ao que e utilizado para se determinar a

ondutividade termia de metais (K). Introduzimos algumas modia~oes a m de ofereer ao

estudanteaoportunidadedeexplorardiferentesmodelos,deformaaaprenderobasiodometodo

ientodedesenvolvimentodeexplia~oesapropriadas,emelhoradasparaadaexperimentoom

oobjetivodeobterumamelhoranidadeentreteoriaeresultadosexperimentais. Corre~oes

semi-emprias s~aointroduzidasnosistemaa mdeompararos resultadosexperimentais omoutros

previamentetabelados. Como asosespeos utilizamosilindrosdeobre[K= 0.92 al/(Cs

m)℄,alumnio[K=0.49al/(Csm)℄elat~aobrass[K=0.26al/(Csm)℄.

I Introdution

Duringthehigh-shoollassesaroundtheworld, most

of theativities arestill based onthe lassi

seminar-like presentation by the teaher. Most of the ourses

arebasedontheoretiallasses,where onlyaverylow

perentage ofthe studentshavethe hane to explore

any kind of pratial demonstration or

experimenta-tion. Eveninthebestases,theapproahisvery

super-ial. Theamountofexperimentalstudiesinreasesat

the undergraduate level, speially onsidering Physis

and Chemistry lasses. It an thus be said that the

rstontatofthestudentswith thesientimethod

ofinvestigationoursduring thebasilaboratory

un-dergraduatephysisourses.

Thelassesofexperimentalphysisarenormally

de-veloped in parallel with the theoretial lasses during

thesame termorsemester. Inthis sense,most ofthe

timesitisassumedthatthestudentsperformtheir

ex-periments after the omprehension of all the physial

oneptsbehindthetheory,aswellasthedevelopment

ofall theequations, et. Unfortunately,historyshows

thatthisisnotalwaystheasebeausethestudentsdo

lasses. Theyseem to have the behaviorof olleting

thedatarst,andtryingtounderstandthemlatterasa

homework. Thisphilosophymustbehanged,although

this is notan easytask. Even in the best ases, after

olletingalltheneessarydataandsubstitutingthem

into therespetiveequations in orderto hek the

va-lidityofthelast(orthevalidityofthedesriptionofthe

physial phenomena), in many oasions the students

ndadisagreementbetweenthepreditionof the

the-ory and their ndings in the laboratory. Most of the

time this fat happens not beause the physial laws

are wrong, and not also beause the experiment was

wrongly performed. This happensindeed beause the

physial model is inomplete ortoosimple to explain

the whole experimental work. As two typial

exam-plesitanbesaidthat duringthelassesofmehanis

veryoften themodel does nottake into aount

non-onservativefores,andduringthelassesof

thermody-namisveryoftenthemodeldoesnottakeintoaount

the lossof energyby heat ondution at somesurfae

orinterfae,andso on.

Theimportantfat about thesituation is that the

(2)

disrep-ing onepts. The students adopt either one of two

proeduresduringtheirreports: a)theystatethat the

experiment is verybad, theavailable toolsand

equip-ments are inappropriate, the results are onsequently

very poor and they annot verify what they wanted,

thus blaming the experimental errors more than they

should orould;b)theytrytoadopttheoppositeway

of thinking, i.e., onsidering the many possible errors

in theexperiment,theytrytoreatealargererrorbar

in ordertojustify anymismathaordingto this

ma-neuver.

Regardlessofanyoftheabove,mostofthetimethe

students tryto blame theexperiment and the

experi-mental data in awayto protet theset of theoretial

equationsasahollystatement. Onlyaverysmall

per-entageofthestudentshaveinfattheouragetofae

the problem and try to look for the real explanation,

even though this seems to be a hard work for them.

Some times they an even elaborate a list of possible

ausesfortheobservedmismath,butdonothavethe

feeling ofhoweah oneofthem would ontributeto a

nalexperimentalvaluehigherorlowerthanexpeted.

Ingeneral,theyhavetroubletryingtoquantifythe

pos-sible auses of disagreement between expeted values

andobserveddata.

Inorderto trytohelp to solvetheaboveproblem,

the present paper disusses a simple experiment and

proedureofanalysisthat aresuggestedforlaboratory

lasseswherethestudentsareintrodued tothe

sien-timethodbasedonthedeterminationofthethermal

ondutivityofmetals.

The experimentdeals with theanientproblem of

thermal ondution throughametalli ylinderwhose

ends sit at temperaturesT1 and T2 where T1>T2 as

shownin Fig. 1(whereL istheylinderlengthandD

its diameter). Assumingan isolated system, the heat

exhangeanbewrittenas [1,2℄:

Q

t

= K

A

L

T (1)

where Q/t is theheat transferperunit time, Kis

thethermalondutivityof thematerial,Ais the

sur-faearea,Listhetotallengthoftheylinder,andT

isthetemperaturedierenebetweenthetwofaes,i.e.

T =T1-T2.

Inthisworkwereviewasimpleexperimentthatan

be used to determine K for dierent metalli

materi-alswhere thetheoretial model expressedby equation

1 represents only a rst approximation to the reality.

Themaindierenesbetweentheoryandexperimental

T1

T2

L

D

Figure1. IllustrationofametalliylinderoflengthLand

diameter D, whose faes sit at temperatures T1 and T2.

Heat ondution ours from fae 1 to fae 2 given that

T1>T2.

II Experimental

Theexperimental setuponsists of ametalli ylinder

(diameterD, and lengthLasshown in Fig. 1) that is

usedto onnettwoups asillustratedin Fig. 2. For

alltheexperimentspresentedinthisworkitwasalways

adoptedD=15.850.01mmandL=61.000.01mm.

Cup1is madeofaluminumandit islledwith water

(M1 = 300 1 ml) at room temperature. The

wa-tertemperatureinsideCup 1isgoingtobereferredas

T1,and it is monitoredby the useof a thermometer.

Cup 2is madeof Teon [3-5℄ and it weights M

C2 . It

hasalsoaTeonoverwithaholefortheintrodution

of a thermometer ( 0.5C) that is used to monitor

thetemperature(T2)ofaxedamountofwater(M2)

insideCup2.

Cup1isheatedbyaameuntilthewaterinside it

startsto boil. Atthismomentanstirrer isintrodued

insideCup2. Thisstirreronsistsofasmall

ferromag-netiylinderoveredwithathinlayerofepoxy. Under

Cup2sitsarotatingmagnetthatisusedtoinduethe

movementofthestirrerinside Cup2. Inthesequene,

small ubes of ie are introdued inside Cup 2, and a

hronometerisstarted. Afteralltheiehasmeltedan

inrease in temperature T2 is observed, and thus the

systemisunder analmost stationaryondition. A

ta-ble is onstruted ontaining eah degree of variation

ofT2,therespetiveT1andtheelapsedtimesinethe

beginningof theexperiment. Thetable of thepresent

paper(not shown)wasonstrutedfromT2equalto0

upto36C.NotethathigherT2nalvaluesouldalso

beused.

Attheend of theexperiment theamountof water

inside Cup 2(M

2

)wasmeasured. Weused M

2 values

of145.0 0.5 ml,135.0 0.5 mland 112.00.5 ml

for the experiments performed with brass, aluminum

and opper ylinders, respetively. Note that in

or-derto avoidburningaidentstheexternalpartofthe

ylinderwasprotetedby athin Teonlayerbetween

(3)

imental data, dierent models were applied for their

understandingaspresentedin thenextsetions.

Cup 1

Aluminum

at T1

Cup 2

Teflon

at T2

Thermometer Thermometer

Metallic

cylinder

Motor

Flame

Magnet

Figure2. Shematidrawing orrespondingto the

experi-mentalset-up. Cup1madeofaluminumislledwithwater

and heatedbya ame while itstemperature is monitored

by a thermometerT1. Cup 2is made of Teon, whih is

also lled with ie and water. It has a Teon over and

itstemperatureT2 is also monitored. Heatis transferred

fromCup1toCup2throughthemetalliylinder. A

stir-rerisusedfor abetter temperaturehomogenization inside

Cup2.

III Results and Disussion

III.1 The simplestmodel

We observed that for the ase of a opper

(alu-minum/brass) ylinder the system takes about 800

(1350/1840)seondsfortheheatingofT2from0Cup

to 36C. These are importantnumbers that help the

professorduringthepreparationofthelasses.Inorder

to determine Kusing the theoretial model predited

byequation1,Qanbealulatedusingthe

approx-imationsthat alltheheatthatistransferredfromCup

1 throughthe metalli ylinderis stored in the water

insideCup2. Aordingtothatsimplemodel,foreah

variation of T2 by onedegree, Q an be written as

[6,7℄:

Q=M

2 C

W T

W

(2)

where C

W

is the spei heat of water (equal to

1al/gC) and T is the inrease in temperature

equalto 1C.Foreahmaterial Kanbedetermined

by substituting equation 2into equation 1. We name

thismodelasmodel1,andthusKisdenotedasK

1 and

written as:

K

1 =(M

2 C

W T

W

L)=(T At) (3)

Note that in equation (3) most of the parameters

are onstants, besidesT and t(assuming T

W as

1C).

Figure 3 shows the results of K

1

as a funtion of

T2 foropper(squares),aluminum(irles)and brass

(triangles) respetively. Three dierentregionsnamed

A, B and C are illustrated in Fig. 3, and they are

separated by the vertial dashed lines. Eah of them

will beonsidered separatelynext. ThedataforT2 <

5Cwerenotshown in regionA. Theywere exluded

from the graphbeauseregion A representsa regions

where thesystemin notinequilibrium yet (amixture

ofwaterandieexistsinsideup2,thatalsopresentsa

temperaturegradient),thusK1valuesstartfromlose

to zero and reah the equilibrium value at about T2

equal to 5C. Inthis sense,region A is totally

disre-garded. Regions B and C are separated aordingto

roomtemperature,that wasabout27C.

0

10

20

30

40

0.10

0.15

0.20

0.25

0.30

0.35

0.40

C

B

A

Copper

Aluminum

Brass

Calculat

ed

K1 (

cal

/

o

C s

cm

)

Temperature T2 (

o

C )

Figure 3. Experimentally obtained thermal ondutivity

values(K1)aordingtothesimplesttheoretialmodel

de-sribed by equations 1 and 2 (see text) for three metalli

ylindersmadeofopper(squares),aluminum(irles)and

brass(triangles) asa funtionof thetemperature(T2)

in-sideCup2. Vertialdashedlinesseparatethreeregions: a)

non-equilibriumregion; b)quasi-equilibriumregion for T2

smallerthanroomtemperature;)quasi-equilibriumregion

for T2higher thanroomtemperature. Note that the

ob-tained K1are neither onstant nor linear as afuntion of

T2,indisagreementwiththetheory.

It an be observed from Fig. 3 that the

experi-mental K

1

is neitheronstantnorlinear asafuntion

of T2. This nding is in total disagreementwith the

preditedtheoretialmodel. Ontopofthatthe

(4)

thanthosereportedforopper[0.92al/(Csem)℄,

aluminum[0.49 al /(C se m)℄ and brass [0.26al

/(Csem)℄[8℄. Thedierenebetweenreportedand

experimentallydeterminedvaluesarebigger,thehigher

the reported Kvalue. At this moment the studentis

leadtothinkabouttheexperimentalresults,andisalso

lead to tryto understand them andto formulate new

modelsthatwould betterexplainthedata.

III.2 The inuene of the TeonCup

The model needs aorretion in region Bbeause

the totalinreasein T2 is due to theheat ondution

throughthemetalliylinder(Q

CYLINDER

),plusthe

heatondutionfromtheTeonCup(Q

CUP

)beause

theinternalpartoftheTeonCupsitsatT2whilethe

outmostpartsitsatroomtemperature(whihishigher

than T2). In this sense, the total heat transferred to

thewaterinside Cup2anbewritten as:

Q

WATER

=Q

CYLINDER

+Q

CUP (4)

Q

CYLINDER

alulated from equation 4 an be

substitutedintoequation1.Q

WATER

isalulatedas

inequation2,andQ

CUP

isalulatedas:

Q

CUP =

K

TE A

TE

d

TE T

TE

t (5)

where t is the same time interval as before, T

TE

isthetemperaturedierenebetweentheinternal and

externalwalls ofthe TeonCup, d

TE

is the thikness

ofthewallsofthe Cup (7.5mm),K

TE

is thethermal

ondutivityofTeon(4.53x10 4

al/(Csm)),and

A

TE

istheeetiveareaoftheup inontatwiththe

waterinsideit. Thisareaanbewrittenasthesumof

thelateralandthebottom areas,andanbe

approxi-matedbythefollowingequationusing anaverageup

radiusR

TE

(37.2mm):

A

TE

=2 R

TE

H+R 2

TE

(6)

whereHistheheightofthewaterolumninsideCup2

(76.1mm). Notethattheupis nottotallylledwith

water, and the top of the up is not in ontat with

thewater inside it. Aording to the above, the right

Q

CYLINDER

tobeusedinequation1wouldbegiven

by:

Q

CYLINDER =M

2 C

W T

W

K

TE

d

TE (2 R

TE

H+R 2

TE )T

TE t

(7)

d

what suggests an even worse result than the one

ob-servedin Fig. 3, given that a smaller Q

CYLINDER

wouldbeobtained. Wewillome bakto thatfurther

below.

Themodel needstobeorretedforregionCalso,

but in thisase thetotalheattransferred throughthe

metalli ylinderisbasially dividedinthree parts: a)

part of it is used to inrease the water temperature

inside Cup2(Q

WATER

);b)partofitisused to

in-rease the temperature of the up itself (Q

CUP A ),

and ) partof it is lost dueto themehanism ofheat

transferthroughCup2totheatmospherienvironment

(Q

CUP B

). Thus,Q

CYLINDER

anbewritten as:

Q

CYLINDER

=Q

WATER +Q

CUP A

+Q

CUP B

(8)

where Q

WATER

is alulated as in equation 2, and

Q

CUP B

isalulatedasinequation5.

Inorderto alulateQ

CUP A

weassumealinear

temperature distribution though the thikness of the

Teonup asillustratedbythesolid linein Fig. 4(a).

Wealsoassumethatforeahtthetemperature

distri-butionvariesqualitativelyaordingtothedashedline

inFig. 4(a),onethatthetemperatureof theinternal

wallinreasesby1C,and thetemperatureofthe

ex-ternalwallstaysat roomtemperature. Of ourse this

is just a rst simple approximation, sine the higher

thevalueofthetemperatureoftheinternalwallofthe

up,thebiggerthedierenebetweenthetemperature

oftheexternal walland theexternalambient. This is

goingtobelatteraddressedinmoredetail. Aording

tothisrstapproximation,thetotalheatstoredinside

theup materialitselfwouldbegivenby:

Q

CUPA =

Z

dTE

0

TE A

TE C

TE

T(x)dx=

TE A

TE C

TE Z

dT

E

0

(5)

where

TE

isthemassdensityofTeon(2200kg/m 3

),

A

TE

isgivenbyequation6,C

TE

isthespeiheatof

Teon(0.28al/(gC)),andT(x)isthetemperature

variationinsidethethiknessoftheupasafuntionof

thelengthfor0xd

TE

. Inordertosolvetheabove

integral,T(x)mustbeknown. Thisinformation an

be extrated from Fig. 4(a) using the dierene

be-tweenthetwoequationsthatdesribeeahofthelinear

dependeneofTwithxbeforeandaftert. Aording

tothat,theinitialdistributionoftemperaturewouldbe

givenby:

T1(x)=T

INT 1

a1x with a1= T

INT 1 T

EXT

d

TE

(10)

and thenaldistribution of temperatureafter t was

elapsedwouldbegivenby:

T2(x)=T

INT 2

a2x with a2= T

INT 2 T

EXT

d

TE

(11)

Usingequation10and11,T(x)anbewrittenas:

T(x)=T2(x) T1(x)=T

INT 2 T

INT 1 +

T

INT 1 T

INT 2

d

TE

x (12)

TakingintoaountthatthevariationfromT

INT 1 toT

INT 2

isequalto1C,equation12anbereduedto:

T(x)=1 x

d

TE

(13)

Thesubstitutionofequation13into equation9leadsto:

Q

CUP A =

TE A

TE C

TE Z

d

TE

0 1

x

d

TE

dx=

TE A

TE C

TE d

TE

2

(14)

Then, theexpressionforQ

CYLINDER

anbeobtainedbysubstitutingequations2,5and 14into equation8:

Q

CYLINDER =M

2 C

W T

W +

K

TE

d

TE (2R

TE

H+ R 2

TE )T

TE t

+

TE A

TE C

TE d

TE

2

(15)

d

0

d

TE

T

EXT

T

INT_1

T

INT_2

1

2

a)

0

L

T2_f

T2_i

T1

1

2

b)

Figure 4. Shemati illustration of temperature

distribu-tion: a) from the inner surfae of the Teon wall of Cup

2 to the outersurfae; and b) along the extension of the

metalliylinderfromCup1toCup2. Thesolidline

(num-bered1)representstheinitialtemperaturedistributionand

thedashedline (numbered2)representsthenal

tempera-turedistributionafterthetimeintervalt,forbothurves.

Ina) thehorizontal axis orrespondsto thewall thikness

(from0tod

TE );T

EXT

istheexternaltemperature,T

INT 1

and TINT

2

arethe internal initial andnal temperatures

respetively. In b) the horizontal axis orresponds to the

ylinderlength(from0to L);T1is theonstant

tempera-tureofCup1; T

2i andT

2 f

arethe initialand nal

tem-peraturesofCup2respetively.

At thismomentthestudentshould beableto

per-form new alulations taking into aountthe

ontri-bution of eah dierent mehanism desribed so far.

We donot presentthese datahere. Instead, we move

one stepfurther and disuss in thenext setion extra

mehanismsthat must also be taken into aountfor

(6)

III.3 Losses throughthe ylinder

Two other dierent mehanisms exist, besides the

heat ondution from up 1 to up 2 by the metalli

ylinder. Therstofthemregardstheheatthatislost

through the surfaeof the ylinder (Q

SURF

)(in its

radialdiretion,i.e. alongthevertialarrowinFig. 1)

beause,inpriniple,eahsetionoftheylindersitsat

a temperature T higherthan roomtemperature. The

seond mehanism regards the storage of heat inside

themetalli ylinderitself(Q

STORED

)aspreviously

desribedfor Cup 2. Inthis sense,the totalheat lost

(Q

LOST

)anbewrittenas:

Q

L

O ST

=Q

SURF

+Q

STORED

(16)

TheheatlostthroughthesurfaeQ

SURF

isoneof

themostdiÆulttobequantied,mainlybeauseofits

three-dimensionalharater. Asaveryrough

approxi-mation, itould be saidthat theheat transferrateat

eahsetionoftheylinder(i.e. in itsradialdiretion)

wouldbegiven,asintheaseofequation1,by[1,2℄:

Q

SURF

t

= K

A

SEC

L

SEC

T(x) (17)

wheret is theelapsedtime asbefore, Kis the

ther-malondutivityofthemetalli ylinder,T(x)isthe

temperature dierene between the highest

tempera-tureinside eahsetionoftheylinder androom

tem-perature, A

SEC

is an eetive area and L

SEC is an

eetivelengthfortheheattransfer,respetively. Just

as a simple approximation it ould be assumed that:

a)A

SEC

anbeapproximatedbytheperimeterofthe

setion at position x, i.e., A

SEC

= D; and b) the

highest temperature inside the setion is loalized at

theylinder axis,i.e., alineargradientof temperature

willbeassumedforeahsetionwiththehighest

tem-peraturevaluesittingattheylinderaxisandthelowest

temperature valuesitting at the externalsurfae thus

leadingto L

SEC

=D/2. It is obvious that thisis not

the exatase, and thus extradisussion about these

approximations is needed. Anyway, aording to the

aboveQ

SURF

ouldbewritten as:

Q

SURF =

Z

L

0

K2D

D

tT(x)dx=2Kt Z

L

0

T(x)dx (18)

NotethatL inequation18refersto theylinderlengthbetweenthetwoups.

InordertosolvetheaboveequationT(x)mustbeknown. Applyingthesameapproximationasintheprevious

setion,T(x)=T

INT -T

EXT

,andT

INT

anbeapproximatedbyalinearfuntion ofxas:

T

INT

=T1 ax; with a=

T1 T2

L

(19)

ThenQ

SURF

anbenallywritten as:

Q

SURF

=2 Kt Z

L

0

(T1 T

EXT )

T1 T2

L

xdx=2KLt

T1 T

EXT

T1 T2

2

(20)

On the other hand, the heat stored inside the ylinder itself Q

STORED

an be alulated using the same

proedure asbefore for thease of Cup 2. The onlydierene nowis thefat that thetemperaturedistribution

inside the ylinder and itsvariation after t would be illustratedby Fig. 4(b). Aording to Fig. 4(b), T(x)

ouldbewrittenas:

T(x)=T1

T1 T2f

L

x

T1

T1 T2i

L

x

= x

L

(T2f T2i)= x

L

(21)

beausethedierenebetweenT2 fandT2 iisalwayskeptequalto1C.

Theheatstoredineahsetionofthemetalli ylinderanbewrittenas:

Q(x)=

M

D

2

2

C

M

T(x) (22)

where

M andC

M

arethemassdensityandspeiheat ofthemetalli ylinder,respetively.

M (C

M

)isequal

to 8400(0.090), 2700 (0.215) and 8920 (0.092)kg/m 3

(al/(gC)) for thease of brass, aluminum and opper,

(7)

Q STORED = Z L o M D 2 2 C M x L dx = M D 2 2 C M L 2 (23)

Thesubstitutionofequations20and23into equation16leadstothenalQ

LOST :

Q

LOST

=2KLt

T1 T

EXT

T1 T2

2 + M D 2 2 C M L 2 (24)

ForregionB,allontributions(equations7and24)disussedinthelasttwosetionsaddupas:

Q

CYLINDER =M 2 C W T W n K TE dT E (2R

TE

H+R 2 TE )T TE t o +

2KLt T1 T

EXT

T1 T2

2 + M D 2 2 C M L 2 (25)

Thesubstitutionofequation25into equation1would leadtoanalKvalueforregionBof:

K B = Z (26) where =M 2 C W T W K TE d TE (2R

TE

H+ R 2 TE )T TE t + M D 2 2 C M L 2 (27) and Z= A L tT W

2 Lt

T1 T

EXT

T1 T2

2

(28)

ForregionC, ontheother hand,allontributions(equation 15and 24)disussedin the lasttwosetionsadd

upas: Q CYLINDER =M 2 C W T W + n KTE d TE (2R

TE

H+R 2 TE )T TE t o + TE A TE C TE dT E 2 +

2 KLt T1 T

EXT T1 T2 2 + M D 2 2 C M L 2 (29)

Thesubstitutionofequation29into equation1would leadtoanalKvalueforregionCof:

K C = Z (30) where =M 2 C W T W + K TE d TE (2 R

TE

H+R 2 TE )T TE t + M D 2 2 C M L 2 + TE A TE C TE d TE 2 (31) d

andZisgivenbyequation28.

It is obvious that the models desribed above

ei-ther for region B or C are not exat. In fat lots of

approximationshavebeenmadejustbeauseitwas

as-sumed that the students do not have enough

mathe-matial toolsyet,giventhat this experimentould be

performedduringtherstyear(seondsemester)ofthe

undergraduateourse. Infat,thepresentauthorshave

alreadyadoptedthisexperimentaspartofalaboratory

ourse alled Laboratorio de Fsia II, at the

DFM-Notethateventhoughthemathematialmodelsare

not orret, the most important physial mehanisms

forheatondutionandheatstoragehavebeen

identi-ed. Thusthealulationspresentedsofarrepresenta

wayofinduingthestudentstotheontinuous

interro-gationoftheexperimentalresultsandtotheontinuous

developmentof betterandmorespei models. As a

simpleexample,startingwiththeanalysisofregionB,

the students aneasily observeby simplesubstitution

ofthevariables'valuesintotheequationsthat the

(8)

Aordingtothat,Zwouldhaveanalnegativevalue,

lakinganyrealphysialsigniane. Thisshowsthat

Q

SURF

,asobtainedbyequation20isoverestimated

mainly due to the inorret temperature distribution

insideeahsetionoftheylinderaspresentedby

equa-tions18and19.

Inordertobetterunderstandthesystem,adierent

approahanbeadoptedbyahugeturninthe

experi-ment. Thestudentsan:a)adoptthereportedKvalues

asknownonstants;b)introdueafuntionF(T2)that

wouldrepresentthe orretionthat must multiplythe

seond termof Z in equation 28 for the right answer,

thusleadingtoanewfuntion alledZ2;and)

deter-mine F(T2)usingexpressions26,27andtheorreted

equation28. Notethatanewsemi-empirialmodelfor

theseondtermofequation28wouldbeobtainedthis

way.

Curiously, after the proper substitution, the

ob-tainedF(T2)isalinearlydereasingfuntionof T2in

theregion5T227Cforthethree ylinders,i.e.,

F(T2) = a - b.T2. Fig. 5 presents the experimental

data for the aseof the aluminum ylinder only. The

orrespondingoeÆientsofthelineartsforthease

of thethree metalli ylindersarepresentedin the

in-set of Fig. 5. Note that eah metalli ylinderhas its

ownsetofttedparameters,indiatingthatthe

orre-tionfuntionF(T2)isinfatafuntionoftheylinder

materialalso.

0

10

20

30

0.0

0.5

1.0

1.5

2.0

Aluminum

F(T2) = a - b . T2

Material a ( 10

-2

) b( 10

-4

)

Brass 1.27 2.6

Aluminum 1.80 3.5

Copper 1.90 4.0

F(T2) ( 10

-2

)

Temperature T2 (

o

C)

Figure 5. Empirial funtion F(T2) as a funtion of the

temperatureinsideCup 2 for the orretionof the seond

terminequation28(fortheanalysisofregionBinFigure

3) for thease of analuminumylinder. Notethat F(T2)

is alinearfuntion ofT2,thesamebeing truefor thease

of the othermetalliylinders. The orresponding tting

parametersaregivenattheinset.

The tted parameters a and b are plotted in Fig.

6 as a funtion of eah reported K value, where the

ylindermaterialisalsoidentied. Parameterais

plot-ted as solid squares at the left axis, while parameter

b is plotted as open triangles at the right axis. It is

bothparametersasafuntionofthereportedKvalue,

indiatingthat one again the ylinder material itself

plays averyimportant hole. Note that both aand b

parametersinreasewithK,andthatwhiletheratioof

thehighesttolowestreportedKvalueisabout3.5,the

ratioof highestand lowest a(or b) parametersis less

than2. The dashed line in Fig. 6 is only aguide for

theeyes,andnottingwastriedbeauseofthelimited

amount of experimental data. Finally, thenal

semi-empirialorretiontotheseondtermof equation28

woulddependontwovariables(K andT2)as:

F(T2;K)=a(K) b(K):T2 (32)

regardlessof other parameters intrinsially related to

thegeometry ofthesystem.

0.0

0.2

0.4

0.6

0.8

1.0

1.0

1.2

1.4

1.6

1.8

2.0

2.2

0.0

0.2

0.4

0.6

0.8

1.0

2.0

2.5

3.0

3.5

4.0

4.5

a

a ( 10

-2

)

Reported K value (cal /

o

C s cm )

b

F(T2) = a - b . T2

Copper

Aluminum

Brass

b ( 10

-4

)

Figure 6. Fitted parameters of F(T2) for the ase of the

three metalliylinders (as presented inthe inset of Fig.

5)plottedas afuntionof theorrespondingthermal

on-dutivityofeahmaterial,thelast onesobtainedfrom the

literature(seetext).

Note that although an experimental funtion is

found,thestudentsannottotallyunderstandits

phys-ialmeaning and origin, what an ontribute to their

own stimulation for the following ourses of physis,

mathematisandnumerialalulus.

Moving to the analysis of region C, the orreted

Z2 term should be used in plae of Z in equation 30

asdisussedabove. Nevertheless,evenin thisase,the

Kvaluealulatedaordingto equation 30 is

overes-timated. Therst three terms in equation 31 are

ba-sially thesameasin equation 27(the only dierene

beingthefatthattheseondtermisnowaddedrather

thansubtratedinthewholeexpression). Aordingto

thepreviousdisussionaboutregionB,thesetermsan

beonsideredmathematiallyorret,andinthisase,

theonlypossibilityofdisagreementmustomefromthe

fourthterminequation 31. Thatisindeed theaseas

anbenumeriallyonrmed: thefourthtermin

equa-tion31ismorethantwieasbigasthesumoftheother

(9)

one. Themain reasonforthat istheverysimple(and

inorret) distributionof temperatureinside thewalls

ofCup2itself.

Following thesame proedure as for region B,the

student an try to determine a funtion G(T2) that

would multiply the fourth term in equation 31, thus

leadingto aorretedY2valueinsubstitutionto Yin

equation31. Oneagain,asemi-empirialmodelwould

beobtained. Inpratie,oneagaintheobtained

fun-tionislinearlydependentonT2,andanbewrittenas

G(T2) = +d . T2. The tted parameters and d

areplotted in Fig. 7fortheaseof thethree metalli

ylinders. As in theprevious ase, thetted

parame-ters depend onthe materialalso, and the nal G(T2)

ouldthenbewritten as:

G(T2;K)=(K)+d(K):T2 (33)

0.0

0.2

0.4

0.6

0.8

1.0

-5.0

-4.0

-3.0

-2.0

-1.0

0.0

1.0

2.0

3.0

0.0

0.2

0.4

0.6

0.8

1.0

-1.5

-1.0

-0.5

0.0

0.5

1.0

1.5

2.0

c

c ( 10

-1

)

Reported K value (cal /

o

C s cm )

d

G(T2) = c + d . T2

Copper

Aluminum

Brass

d ( 10

-2

)

Figure 7. Fitted parameters of G(T2) for the ase of the

three metalli ylinders plotted as a funtion of the

or-respondingthermalondutivity ofeahmaterial,the last

ones obtainedfrom theliterature (seetext). G(T2) is the

empirialfuntionthatorretsthefourthterminequation

31.

Fig. 8showsthenalresultsfortheaseofthethree

metalliylindersforalearomparisonofthemodels

disussed. The K1alulated aordingto equation 1

areshownasopensquares. Thenal Kfalulated

a-ordingtotheorretionsintroduedforregionsBand

Care shownas solid squares, andthe reported values

for K for eah material is shown as asolid line. The

improvementof thesemi-empirial model is

outstand-ing.

The main reason behind the need for funtions F

andGintheorretedmodelsisthefatthatthe

tem-peraturedistributioninsideeahsetionoftheylinder

and inside the walls of Cup 2were oversimplied. In

order to better presenta physial model the students

needmoremathematialandomputationaltools,not

availableforthemyetduringtheirrstyearofthe

un-0.0

0.2

0.4

0.6

0.0

0.5

1.0

0

10

20

30

40

0.0

0.1

0.2

0.3

Aluminum

K ( cal /

o

C s cm

)

Copper

K1

Kf

K

T

Brass

Temperature T2 (

o

C )

Figure8. Comparisonoftheresultsthatwouldbeobtained

with the simples model (K1, open squares) and with the

modelthattakesintoaountseveralorretions,inluding

the empirial funtions F and G (Kf, solidsquares). The

thermalondutivityvaluesobtainedfromtheliteratureare

shownashorizontalsolidlines(KT). Resultsareshownfor

thease of thethreemetalliylinders(opper, aluminum

andbrass).

IV Conlusion

In fat, the ndings of this experiment are important

not beause of the nal results, but beausethey an

showthe students howomplex a physis experiment

anbeeven thoughitmight look too simplefrom the

beginning, and how simplied the theoretial models

an be sometimes. This is an experiment that leaves

student thinking about it even after the end of the

lass,andsureontributestotheirselfmotivation

dur-ingotherlassesofphysis,mathandnumerial

alu-lus. Finally,morethanthesimpleveriationofertain

equations, the students are foredto think about the

nature of manyphysial mehanismsduring heat

on-dution.

Aknowledgements

This work wassupported by the Brazilian ageny

CNPq.

Referenes

[1℄ J. Carslaw, in Condution of heat in solids, Seond

Edition,OxfordUniversityPress,Oxford,p.2(1989).

[2℄ J. Phillips, inExamples in AppliedThermodinamis,

(10)

[3℄ see

http://www.dupont.om/teon/hemial/properties.html

#thermal

[4℄ seehttp://www.jenseninert.om/properties-teon.htm

[5℄ seehttp://boedeker.om/ptfe p.htm

[6℄ M.Plank,inTreatiseonThermodinamis,Dover

Pub-liationsIn.,NewYork,p.35(1945).

[7℄ E.Fermi,inThermodinamis,DoverPubliationsIn,

NewYork,p.21(1936).

Imagem

Figure 1. Illustration of a metalli ylinder of length L and
Figure 3 shows the results of K
Figure 4. Shemati illustration of temperature distribu-
Figure 6. Fitted parameters of F(T2) for the ase of the
+2

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