Past Final Papers 1
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8/10/2019 Past Final Papers 1
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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$-t
(8 Mar&s)
(8 Mar&s)
( Mar&s)
( Mar&s)
( Mar&s)
( Mar&s)
+
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Heat and Mass Transfer/Transport Phenomena BTE 3215/ 3210
,8-
,4-
1 Mar&s+
*r% a'r 's 'nha"ed at a rate of 10 /m'n thro$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
( 8 Mar&s)
( . Mar&s)
( Mar&s)
( Mar&s)
( Mar&s)
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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Heat and Mass Transfer/Transport Phenomena BTE 3215/ 3210
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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Heat and Mass Transfer/Transport Phenomena BTE 3215/ 3210
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