CHEMICAL ENGINEERING

(Amelia) #1

FLOW IN PIPES AND CHANNELS 59


D


Rr^3

(^4) p


{


1  4 / 3 X 2 X^2 C 4 X^3 


5


3


X^4


}


(ii)

In the core region


Substituting:sDrcDRY/RrDXrin equation (i) for the core velocityucgives:


ucD

1


(^) p


{


R


2 r

r^2 X^2 r^2 RYrXr

}


D


Rr

(^) p


{


1


2


 1 X^2 X 1 X


}





Rr

(^4) p
f 2  1 X^2  4 XC 4 X^2 g


D


Rr

(^4) p


{


2  4 XC 2 X^2


}


Theflowrate through the core is:ucr^2 cDucX^2 r^2 DQc


Thus: QcD


Rr

(^4) p
X^2 r^2 f 2  4 XC 2 X^2 g


D


Rr^3 

(^4) p
f 2 X^2  4 X^3 C 2 X^4 g
The totalflowrate is:QACQcDQ
and: QD
Rr^3
(^4) p


{


1 ^43 XC^13 X^4


}


Putting RD


Pr
2 l

then :

QD


Pr^4
8 l p

f 1 ^43 XC^13 X^4 g

When: PD 6 ð 105 N/m^2 ,lD200 m dD40 mm andrD 0 .02 m.


Then: RDP


r
2 l

D 6 ð

0. 02


400


ð 105 D30 N/m^2

(^) pD 0 .150 Ns/m^2
RYD 14 .35 N/m^2
and: XD


RY


R


D


14. 35


30


D 0. 478


Thus: QD


 6 ð 105  0. 02 ^4
8 ð 200 ð 0. 150

{


1 


4


3


ð 0. 478 C

1


3


 0. 478 ^3


}


D 0 .000503 m^3 /s
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