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    Heat and Mass Transfer/Transport Phenomena BTE 3215/ 3210

    INTERNATIONAL ISLAMIC UNIVERSITY MALAYSIA

    END-OF-SEMESTER EXAMINATION

    SEMESTER II 2013/2014 SESSION

    KULLIYYAH OF ENGINEERING

    Program : ENGINEERING e!e" of #t$d% : &G 3

    T'me : (:00 am ) 12:00 noon *ate : 02/05/201+

    *$rat'on : 3 Hrs

    ,o$rse ,ode : BTE 3215/3210 #e-t'ons : 1

    ,o$rse T't"e : Heat and Mass Transfer/ Transport Phenomena

    Th's .$est'on Paper ,ons'sts of 21Pages 'n-"$d'ng ,o!er Page 'th Eight (8).$est'ons

    INSTRUCTIONS TO THE CANDIDATES

    DO NOT OPEN UNTIL YOU ARE ASKED TO DO SO

    There areTHREE (3) se-t'ons 'n th's $est'on paper4

    Section A is omp!"sor#$ nser An#THREE (3)$est'ons from Section %4Section is

    %on!s

    nsers sho$"d 6e -"ear and 'nte""'g'6"e &sef$" E$at'ons4 Ta6"e and 7'g$re are atta-hed

    No 6oo8s4 notes and programma6"e -a"-$"ators are perm'tted

    7or spe-'f'- 'nstr$-t'ons4 p"ease refer to the appropr'ate se-t'on

    Any form of Cheatn! or Attem"t to Cheat # a Sero$# O%en&e

    1

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    Heat and Mass Transfer/Transport Phenomena BTE 3215/ 3210

    'h&h may Lea( to D#m##a)*

    Section A: Compulsory .

    Tota" mar&s for this part ' * mar&s+

    ,1-

    ,2-

    1* Mar&s+

    a 9hat 's the d'fferen-e 6eteen nat$ra" -on!e-t'on and for-ed -on!e-t'on

    9h'-h one 's genera""% more eff'-'ent 9h%

    6 ;ne of %o$r fr'ends sa%s N$sse"t N$m6erNu's e$a" to the d'mens'on"esstemperat$re grad'ent at the s$rfa-e of a g'!en geometr% The other fr'end

    sa%s 't 's the rat'o of -on!e-t'on to p$re -ond$-t'on heat transfer 9hose

    s'de of the arg$ment o$"d %o$ ta8e 9h%

    1* Mar&s+

    a 9hat 's the d'fferen-e 6eteen "o-a" !e"o-'t% ur4x and mean !e"o-'t% um

    *er'!e the e

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    Heat and Mass Transfer/Transport Phenomena BTE 3215/ 3210

    ,- 1* Mar&s+

    f"at p"ate has "engthL= 3 m4 the "o-a" -on!e-t'on heat transfer -oeff'-'ent ma%6e e

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    Heat and Mass Transfer/Transport Phenomena BTE 3215/ 3210

    Part %0 , is omp!"sor#- Anser an# To (2) !estions from .>4 .C4

    .( and .10Tota" mar8s for th's part' * mar&s+

    ,-

    ,.-

    (In solving problems in this part follow the

    systematic approach; clearly state known, fin,

    schematic, assumptions, properties, analysis an

    comments.!

    2* Mar&s+

    Hot e5 -m 'n d'ameter and @ m "ong at a rate of 05

    8g/s The s$rfa-e of the a"" 's ma'nta'ned at an a!erage temperat$re of 500

    The a!erage a'r temperat$re 'n the d$-t 's 550 ,a"-$"ate the

    a the Re%no"ds n$m6er

    6 the -on!e-t'!e heat transfer -oeff'-'ent h

    - the de-rease 'n temperat$re of the a'r as 't passes thro$gh the d$-t

    (8 Mar&s)

    (8 Mar&s)

    ( Mar&s)

    ( Mar&s)

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    +

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    ,8-

    ,4-

    1 Mar&s+

    *r% a'r 's 'nha"ed at a rate of 10 /m'n thro$gh the tra-hea 'th a d'ameter of 20

    mm and a "ength of 125 mm The 'nner s$rfa-e of the tra-hea 's at norma" 6od%

    temperat$re of 3>D, and ma% 6e ass$med to 6e sat$rated 'th ater

    a ss$m'ng stead%4 f$""% de!e"oped f"o 'n the tra-hea4 est'mate the mass

    transfer -on!e-t'on -oeff'-'ent

    6 Est'mate the da'"% ater "oss /da% asso-'ated 'th e!aporat'on 'n the

    tra-hea

    1 Mar&s+

    ,ons'der a !ert'-a" p"ate of d'mens'on 250 mm < 500 mm that 's at Ts= 13+D,'n a $'es-ent en!'ronment at TF= 20 D, 7or ea-h or'entat'on4 -a"-$"ate

    a) The Ra%"e'gh n$m6er

    5) The rate of heat transfer 6% -on!e-t'on from the front s$rfa-e

    c) In the 'nterest of m'n'm''ng heat transfer from the p"ate4 h'-h or'entat'on 's

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    ( . Mar&s)

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    5

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    Heat and Mass Transfer/Transport Phenomena BTE 3215/ 3210

    preferred 9h%

    ,1*-

    ,11-

    1 Mar&s+

    Ethano" 's d'ff$s'ng thro$gh a + mm stagnant f'"m of ater The ethano"

    -on-entrat'ons of the entran-e and the e

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    S6ME SE9: E,AT;67S A7< 67STA7TS0

    1- ;nterna" forced con=ection for constant s!rfacetemperat!re condition$

    Therma" entr% "ength for "am'nar f"o

    Graet n$m6er

    am'nar4 therma" entr%4 Pr5

    Ts= -onstant

    HereP's per'meter P= D

    9here p's the press$re drop andP's p$mp'ng poer

    >

    =

    =

    hcm

    PL

    TT

    TT

    T

    T

    pims

    oms

    i

    o

    e

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    2- ;nterna" forced con=ection

    Ta8e C= 02@4 m= 0@4 and n= 03>

    3- 7at!ra" on=ection for #"inder0

    C

    ( )

    3DTTgRa sD

    =

    ( ) +1PrPrPrRe snm

    DD CNu =

    4k

    hDNu

    D= 4

    A

    mD

    DDh!h =

    ( ) +1Re snm

    DD !c!c!cC!h =

    4AD

    !c =

    / = TThA" s

    04/ 44 = AsatAmA Ahn

    444 satAA =

    fgAs hnTThA" += /

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    Heat and Mass Transfer/Transport Phenomena BTE 3215/ 3210

    7or Ra* 1012

    4

    - Heat E>changer ?7T Method

    - 9ic&@s :a of imation)

    (

    ( )

    2

    2>

    C

    1@

    (

    @1

    Pr/55(01

    3C>0@00

    +

    += DDRa

    Nu

    4ma