sol ch6 part2
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nuclear engTRANSCRIPT
LAMARSH SOLUTIONS CHAPTER-6 PART/2
IMPORTANT TABLES:
*TABLE 3.2 NON-1/V FACTORS
*TABLE 3.4 THERMAL DATA (0.0253ev) FOR THE FISSILE NUCLIDES
*TABLE 5.2 THERMAL NEUTRON DIFFUSION PARAMETERS OF COMMON MODERATORS AT 20C
*TABLE 5.3 FAST GROUP CONSTANTS FOR VARIOUS MODERATORS
*TABLE 6.1 NOMINAL ONE-GROUP CONSTANTS FOR A FAST REACTOR
*TABLE 6.2 BUCKLINGS AND FLUXES FOR CRITICAL BARE REACTORS(ASSUME D IS SMALL)
*TABLE 6.3 VALUES OF T
*APPENDIXES:TABLE II.2 AND TABLEII.3
6.20
Assume d<<R
2 2( )BR
=3.95e-3 cm-2
a)
0
0
( )
( ) ( )
aM aM FFF M M
aF M aF aF M
E MMm Z m Z m
M g T E M
, eq(6.88) , where
2 2
2
1
1
TM
T TM
B MZ
B
,eq(6.83), 2 2 2480 102 582T T TM L cm
And in here, 0 0( ) 0.0092 , ( ) 681 , ( ) 0.978, 2.065aM aF aF TE b E b g T so inserting into
eq(6.88) we’ll find , 1.79 3F Mm e m
Then the total mass of Be in the reactor as follows,
31.85 /M g cm , 3 5 345.24 10
3V R cm
1.85 969 1.73M Fm V kg m kg [ANS]
b)
Thermal flux is given by,
R2
1( ) ( ), from table 6.2 in here P=50kW=5e4joules/sec ; E 3.2 11
4T
R f
r Pr A Sin A e joule
r R R E
F 0 from 6.85 N = = (T) ( ) V V 2
F A F Af f f f fF f
F F
m N m NN g E
M M
;and the values,
-1
0(T)=0.976; ( ) 582 =4.26e-3cmfF f fg E b and the constant A is found as follows,
2
5 4 13.66 13 ( ) 3.66 13 ( )
4 50 3.2 11 4.26 3T
e rA e r e Sin
e e r R
[ANS]
c)
4: 2.3 10 n/cm2.sec in here D=0.5 for Be
4r R R f
d D PLeakage D e
dr R E
[ANS]
d)
cons.rate=1.05(1+ ) P g/day=1.05(1+0.169) 50e-3MW=0.0613 g/day [ANS]
6.26
235 2 2 2
0.84 2.13 1.7892 ; is from table5.2
(300 ) 2.055 from tab.6.3 and 721
M
T T T T
D cm d D cm D
C M L cm
a)
2 -2
2 2
2 2
For a critical reactor; 1 =1.012e-4 cm 1
where 3 ( ) and 3 / 2 537.32
T
kB
M B
B a B a a d cma
[ANS]
b)
max 25
3
25 25 0 25
25
u
3.87 [from table 6.2] 1113.5 24 / 3
( ) (573 )2
1113.5 24235 4.3466 5 gr U-235 then found the mass of the natural uranium as,
0.6022 24
4.3466 5m 60 tons nat.
0.0072
R f f
PN e atoms cm
a E N E g K
em e
e
e
Note:U in here 0.0072 is the percent of U235 in natural U
6.37
a)
2 22.80 (from equal volumes approach) 1.58b L L b cm ,which is the radius of equivalent
radius [ANS]
b)
2
2 20.290F
M
V R L
V b L R L
[ANS]
c)
F ML 1.55 ; L 2.85 ; thus,
0.75 0.75 1.58x= =0.48 ; y= =0.26 ; z= 0.55
1.55 2.85 2.85
Then as x,y and z are less than 0.75 you can use eq(6.117) and eq(6.118) with a good accuracy,
After finding E and F the
cm cm
1
0 2, . 25 ,25 0 25 28 ,28 0 28
1
0 2, , 0 , 0
n finally we'll use eq.6.114 in where,
T( ) ( ( ) ( ) ( ) ( ) ) ( ) and
2 T
T( ) ( ( ) ( ) ( ) ( ) ) ( )
2 T
in here you can use the table II.3
a nat U a a a a
a water H a H a H O a O a O
T N E g T N E g T
T N E g T N E g T
1 1
235 238
,at 0.0253ev, 0.3677 & 0.0222 with a good accuracy or
you can calculate yourself the macroscopic cross sections, inserting the following above
680 & 2.73 & 0.664 and the ot
F M
a a
M
a a a
cm cm
b b b
3 3her constants as 19.1 / & 1 / so finally
0.797
F Mg cm g cm
f
[ANS]
d)
2 24 3
1.46 from table(6.6) where
4.83 10 10 / from table II.3
F F
M sM M
F
N V I
VM sMp e
N atoms cm
I A C a where 2.8& 38.3A C from Table6.5
0.883P [ANS]
e)Using fig. 6.10 and 1.5 cm rods on that figure
1.04 [ANS]
f)
25 25 25 25
2825 2825 28
25
02825 25 f25
25
0 0
25 a25 28 a25
The ratio 138 for natural U.Using 2.42, 582 ,g (20 ) 0.976
681 ,g (20 ) 0.978, 2.70 ,g (20 ) 1.0017 gives,
1.32 and using t
f f
T
a aa a
f
a a
T
N
N
Nb C
N
b C b C
he four factor formula we can find k
0.9828 k fp
6.17
(-a) -100 0 100 (a)
a)
2 2
2 -2
( ) in here 2 where d=2.13D and D=0.84 for graphite finally
9.53 4 cm
B a a da
B e
b)
2
TM
2 2
2
F F 0 F
M M M
F
M
,
F,critical
3500 , 368 , 2.065
16.56 and the using the relation,
1
N N ( ) ( ) NZ= 3.34 5 so use,
N N N
N1.046 3 gr/cm3 and finally,
N
N
TM T
TM
T TM
aF aF aF
aM aM
F MF
M F
F cri
L
B MZ
B
g T Ee
Me
M
2.68 18 atoms/cm3tical AV
F
Ne
M
c)
2 2 2Z(1 ) and here f= 0.867 and so 463 2
Z+1T TM TL f L L cm
d)
k 1.79 T f
e)
max( ) cos( ) 5 12cos( ) and the current
d ( ) DJ=-D 5 12 sin( )
x xx e
a a
x xe
dx a a
f)
max
, ,25 25 0
25 0
1.57[ again from table 6.2]
( ) ( )2
where 200 2 2.13 0.84 203.57
( ) can be found from table II.2 in appendix
so you can find P from here!
R F critical f fF
f
PA
aE N E g T
a cm
E
6.27
assume d<<a
2
2
1
and k=1 for criticality
k
kBL
2 2
c c
2
R R2
R
in the power producing section,core,you should solve the equation
B 0
and in the reflector region there is no fission ;so solve then,
10
L
For criticality conditions:
a)
İnf. reflector core core İnf. reflector
-a/2 0 a/2
c 1 2
c2 c 1
R 3 4
R 4 R 3
c R
c Rc R
cos( ) sin( )
@ 0 B.C.1 0 cos( )
lim x must be finite so 0
then interface B.C.
a a[I] ( )= ( )
2 2
a a[II] -D @ D @ the
2 2
R R
R
x x
L L
x
L
A Bx A Bx
dx A A Bx
dx
A e A e
A A e
d dx x
dx dx
2
1 3
23c 1
c
n introduce these into the fluxes,
aI cos( ) =
2
aII D sin( )
2
acriticality condition gives:D tan( ) (*)
2
(*) must be satisfied by the reactor to be critical.
R
R
x
L
x
L
R
R
R
R
A B A e
ABA B D e
L
DIIB B
I L
b)
ref. core core ref.
-a/2-b -a/2 0 a/2 a/2+b
R R
c 1
x x
L L
R 3 4 R
R 3
R
c R
c
again A cos(Bx)
aA e A e from vacuum B.C. ( b) 0
2
a( b) x
a2so we can write =A sinh( ) note that @ x= b vacuum B.C. is satisfied.L 2
then interface B.C.
a a[I] ( )= ( )
2 2
[II] -D
c RR
1 3
R
3c 1 R
R R
Rc
R R
d da a@ x D @ x then introduce these into the fluxes,
dx 2 dx 2
a bI A cos(B ) = A sinh( )
2 L
Aa bII D BA sin(B ) D cosh( )
2 L L
DII a bcriticality condition gives:D B tan(B ) coth( ) (**)
I 2 L L
(**) must be s
atisfied by the reactor to be critical.
c)
R+b
R
c 1 2
c 2 c 1
R R RR 3 4 R R 3
c R
sin(Br) cos(Br)A A
r r
sin(Br)as r 0 must be finite so A 0 A
r
r r R b rsinh( ) cosh( ) sinh( )
L L LA A or using vacuum B.C. (R b) 0 A
r r r
then interface B.C.
[I] (R)= (R)
[II] -
c Rc R
R1 3
R Rc 1 3 R2 2
R
c
d dD @ r R D @ r R then introduce these into the fluxes,
dx dx
bsinh( )
Lsin(BR)I A = A
R R
b bcosh( ) sinh( )
L LBcos(BR) sin(BR)II D A ( ) A D ( )
R R L R R
II 1criticality condition gives:D (Bcot(BR) ) D
I R
RR
R
bcoth( )
L 1( ) (***)
L R
For the fluxes:
c 1
a / 2
R f 1 1
R fa / 2
c 1
R 22
R f 1 1
R f0
For infinite slab; A cos(Bx) so,
1.57PP=E A cos(Bx) dx A
aE
sin(Br)For the sphere; A so,
r
sin(Br) PBP=E A 4 r dr A
r 4 E (sin(BR) BR cos(BR))