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HEAT CONDUCTION IN SPHERES dt k 4 r dr Q dr dt ) r 4 -k( Q r 4 A dr dt -kA Q Law s Fourier' From 2 2 2 ) t t ( k 4 r 1 Q ) t t ( k 4 1 r Q dt k 4 dr r Q 1 2 2 1 1 2 2 1 1 2

Conduction Through Spheres

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Page 1: Conduction Through Spheres

HEAT CONDUCTION IN SPHERES

dtk4r

drQ

dr

dt)r4-k(Q

r4A

dr

dt-kAQ

Law sFourier' From

2

2

2

)tt(k4r

1Q

)tt(k41

rQ

dtk4drrQ

12

2

1

12

2

1

1

2

Page 2: Conduction Through Spheres

21

12

21

12

21

12

21

12

12

12

rkr4

rrR

R

t

rkr4

rr

)tt(Q

)tt(k4rr

rrQ

)tt(k4r

1

r

1Q

Page 3: Conduction Through Spheres

HEAT TRANSFER FROM FLUID TO FLUID IN SPHERES

2

2o

oo

3

21

122

2

1i

ii

1

321

r4 A; Ah

iR

rkr4

rrR

r4 A; Ah

iR

RRR

totiQ

total

ooii

t

R

1AUAUUA

)t(UAQ

R

tQ

Page 4: Conduction Through Spheres

A 3 m internal diameter spherical tank made of 2 cm thick

stainless steel (k = 15 W/m-K) is used to store iced water

at t+ = 0C. The tank is located in a room whose temperature is

to = 22C. The walls of the room are also 22C. The outer sur –

face of the tank is black ( = 1) and heat transfer between the

outer surface of the tank and the surroundings is by natural

convection and radiation. The convective coefficients at the

inner and the outer surfaces of the tank are hi = 80 W/m2-K

and ho = 10 W/m2-K, respectively. Determine

a. the rate of heat transfer to the iced water in the tank

if the outer surface temperature is 5C

b. the amount of ice at 0C that melts during a 24 hrs

period

Page 5: Conduction Through Spheres

r1 r2 k hi ho hice

1.5 1.52 15 80 10 333.7

ti to t2 Ai Ao T2

0 22 5 28.274 29.03 278

To Qc Qr Q mice

295 4936 2.6E+03 7.6E+03 1960

kg 1960m

)mice(333.7sec) hrs)(3600 7.6(24Q

KW 7.6 Watts7600Q

)TT(AQ

)t22(AhQ

QQQ

ice

4

2

4

oor

2ooc

rc