ML20024C703

From kanterella
Jump to navigation Jump to search
Nuclear Power Preparatory Training,Core Performance 4, Heat Transfer & Heat Generation
ML20024C703
Person / Time
Site: Crane 
Issue date: 12/31/1969
From:
NUS CORP.
To:
References
TASK-01, TASK-06, TASK-1, TASK-6, TASK-GB GPU-2250, PROC-691231, NUDOCS 8307130051
Download: ML20024C703 (4)


Text

,.

4

_~

~**~'

' = :. '~

v.,.

..T -:,y.

1

'. -[a~.;.j f 7.

  • ; ?~

^

,y

& ~'.,

s

.,[*

_.::y:3 _. ": c,

,.y vl* -

'*::.t. h '-

. ~~ x H

.+.

z'.,,. %.;, 2._:.

~_ _ _, _ _ y
;.

V4.

..'~~1 c

" ~

cusv~6-m rn 3.rm x l

. ~

.. Q 1,o i Em dj js.

=

s y

gm F

yv 3

3m

";"J WlU '

2 vt l

[

=%

g i

.a.

'h. A

.2 N'

1NI" CLEAR POT tR

.n m.

V.u i ;

PREPARATORY TRAINh"G i,..2 4;.7.-

<L, g "...,

n;: n.-n g

a...-

CORE PERFORhiANCE dM UW i

- - w :,. m x =.

e

.k-: ' -' s 4 L.

4 c.*

3.&

.$:\\:?,Q c:p +, n u.=.=.

t*-1:

y' a course for c y e. %.

b.@

.._g. :.

.e}.'~}m yt 1

1-

  • y METROPOLITAN EDISON COMPANY i?5 M

i m:.e. <

<-c; ~s-f -

via i eo ape

- s;;3e ve

-pq m

m..

w;-c :. o u-

-m s

. w 1* b,

e e*

by

6e. :e

-~p ht,

. w..

=

m e,.a@

c C L' NUS CORPORATION 3M h'* i m..,

w s

gj Rockville, Maryland

((.!

g~,

. 'k;:.Q~

i. ~ &

. / U._

e w

c.n r;

l.':d.I.O

$0 r,

b**l B307130051 691231 7;

PDR ADOCK 05000289 t,y W

A g

A 'l 4; ;'

?."::' (

h i '.~. g$ ', h *.:

k2 I

u - p%n:'r.sm, 4y,t,,cr, :,,.g 'n:.?: '~t e,x,'s'

.ms

'. ae.s... yy~.;.em. n..",

~.,n v* We gl,$i Y, '< ',..,..,.;;m,,. L,2..%,./p* w*}m~...~m.7,i,f,'

C.'>.?.r.~.c,,Q=,.t :',,.....

d

' '., 2 v.+. >

' n..gw*.:.-.

p.t w e..n

. ~;;. s

.c.

.- n

' ' g*.y%' g;.

3g..w.

.r st

  • n rmswy y *n**, *~ ~ W *..

W h W. w,

a.m ; a w e.= w c m.,7.:.2,,22 M *

  • '"y'h*L*;*Qv,w n.-w-,.c.4 g. Q'.

n,

.~s. :

.~ 4.or7x n.m.bym gg;gg g /

(

t s

'm

..g r> vp u s

A g,n.-

r

.a 6

..._.-'^,..."#8b"4*. _,,.

        • M<irgogn,4r9. psser.

ppp.,

,g

4-fs s

_. r,

- -r - -,-

..x.

., p r-r 7,

n

.. - - y, -..-

. ~.. -,

.a 3

a g.;....,..1,

, ~., _..

._...,.~a..,_.....;,__

. _.. u..m.. -.

. m.g r,

.+

c

,.~,..#

....x.

_ ~,..

1.

--6 4;

l

[.

1

'J r

,I

\\

i

- j l,....,

r Q

[-

s

~.

F. i am...,.

9 i u.

L * *1 I t.)

'9 1

e

.i q.m --

v.

.j

~.

I im 6

  • 4 w

h h:

..~-'#

f..

F

  • .. " j
  1. -.s.

_;4.c::. ;

E.. s, r.. l

. s.

.... +

p..

.. + -

m...

.s m

.U c-*i

=, ' " -

- > ~.

s p

w ;;-

..w

,.a

v. : -

L.

u y.^.

n 4

T

.J~

(* ~ ~ '

.[...,

.-.4 O

1 a.

n k J.

L..., t

.g.....

g.

  • vs t m*"

g.j '

.; m m

r

,rs

_ g.a, m.

Orpmght 19n9 by NCS Capwesica

+., a l..1.-

r 7,

u.

All rights merved. This book or any part p

4-4 thereof must not be reproduced in any form ib i -

..3

.ithout the written permission of NUS

%~

~

x'

w y;

Corporation.

i-m

. e -.

h,.......

q i

rnatea sn the Catted States of Amerece

?

P"..

.,.f.c.

. Ke g.p r d

e.

h+'ut

, > Q* r Ln" w

";.,u. ]

n c

i.

T' d

~

~

. sD 4 * ;4 *

, f=..

h 5~ l t

T:.+

p

'n m.

=

r,, = 3 1 7, I

,:a! &j.

r

. we

.MF s.-

P T

y

  • E-.-.

e -,.$ '-k"" "-" ' 5' t'.'.-K' = Wi f5'=4,.,$

~g Q.'m{&.'.' h.s.v,f ";:::;g

- - -' $~$~..g "

$g =,.?h' 5. 5. S, $.. $... IY. h.,, N,N, W'p-R~ -$'r.,N;Y

,w*. Y'.'ny'- *. w&$?N.'-5 g _

-.F"'

g

?

w,w-t,. w m : w,, w.

-. r-

.b-:nL+.

s

.y, ~sa -/

ww

,..,.;m..et q,.

~p

- e < = s; 7 *-

- w>.a...

A.~ s t

. g yy.?
,g, g Rc:

1

.,p.

-,. t we.f.,'?.w! a. n,C;. iG= M ?:b,,Q*.n Lg-M.am M :.2. A r p w--:lw;.. A*.

1,V1.Qggs.y' ~i,1:

.r,.

usl y ~-

M,ir

.. w

m. wM. ;~r~y-D. -

e M.--, 4 i

e. ".L;.w " ~ qwP g %

- -: Ag;*z-y._na. e,;n,~j,~* ~up. i g -*- - da..s J.*

r v~

...p...-r"

- s-x.w u-

=,s,....

w w~."a~

.e; i 7 -

?.P. -

g.

. w. p ens.*

I 1

I J

.y.,,

h j

v,-

x

. ; p m., -

s -~.2.;,3 ;:-=~.u s...-,.: %,p...

-== }

.~z 1:, -

.n:.w. - -

'~..

v-

-. e~-

.,. ~ 1.D ;.u' ',n:..;.%. ;...

. x..,..

~.y.' s

r...
= ~=..a *., ;O 1, %.... - ~... m.__.-c n

n.

.....n-

,3

--,.~. 3 (w.,; ; j

. w

. c..

n..,

w. y -.m-c -
f.:.*s*

j.

r..,

p r

.<~~-m 4

i

.4

n. a.

.e 7-~. <

u

-1 r

. HEAT TRANSTDL AND HEAT GENIRATION

%r.p g"

-j

]

4.

f+i~.~ :q, a

?

t A.

General q

hy N The study of heat transfer is wT.ed with the details

~- C (1)

H 4

of the rate of new of heat energy between bodies. It has been stated that F,:4.. ;9,1 heat will flow between two bodies if one is at a higher temperature, but L. M. 7 'I

.g[.i te U: NZ for design purposes it la also impcrtant to know how fast the process will

,;[j p u, occur. The three basic categories of heat transfar are:

X-J W y

~-w -

-W

w. :.,.:w i

e conduction f4..:.,

Cr&

i e

cortvection e ; e sw,W m'."*..

5 o radiatica

.m M.y +m :

,;.t

.mr.%

1mpact. When a part of a metal bar is heated, molecules at the point being

,@@]

GW.J ! :

(2)

Conduction is direct transference of heat by molecular y

.u.

'}^[ii I

%m. N.. g'q heated vibrate mere and more rapidly, collide more vigorously with their

(.Q.I neighbors, and transmit seme of their energy to them. A good example of

}

. '. m-~1

?.g?@

conduction is the now of heat up a spoca frem the coffee in your cup to c.v w -. n

cd A=

your fingers.

  • se

@v;46

^p 9.w'A 0)

Heat transfer by ccavectica is the transfer of thermal 4

v.;

rn" KC energy by the motien of a nuld that is being heated. There are two general g.d PrM+wt s.e

."4, ca.-

m rm.W categories of ccavectica, called naturni ccavection and forced ccavectica.

4 pw.f.=

Natural ccavectica takas place because the density of the heated Guld is

.j M.',7,.].yj 1

~

p'JI. m W less than that surrounding it and as a result it rises. This can be seen on pW..G A

~;

y M.nC an autemchile en a hot summer day. The air touching the metal. surface is 4

m s

n m

m.m.e.

heated by conductim and stavection currents are set up, resulting in a trans-

]

.c %n.,

4:--

S.M M. '

for of heat away from the surface. Terced convection occurs when the

,}

'i

%1:m.

Ruld motion is caused by seme facter other than the density difference.

such as pumps or fans. For forced convection the effect of the different Ndg 3

M Guld densities usually has little significance. A good example of con-g p.h 1

r.ha vactla la tsa c;,uatim sf a c.-ffc=

reciat=r, ws: s ras a net.t Ch $ y-.-

Q circulation.

&wmE

  • R W.

hy **%w.,,4

\\

E* N '.w^'

I.

\\

1l-

. n g& F;W

)

1070P 4-1

\\

V!p;!MW a

M,w'W I

ce*

mw w h

]

.\\

\\

, s k[, U $b O.

W

> seammanswnm

~.

_"__....V.?1'

.*~*"'* 9.* y = y ee,y gm. o 4 ,_,7 ' ~ - - - - - - - -.. -.,

u /- '," ~. ~ _ >Q~ *,,w:gf.3;. =-;:. :_:'.p::.:,z _.g.g .%.. 4 yw- . ' ;.:}.a.,M.*~*n-N M i} & y: 5 .:Q'j[ . :..~:. . 'M4 I L :w. ; v.. ~. ;* -

.c..

.-v ..... r

f. s...

~..m. , _., ~,.. _.. _.9 V w. dl.'-3 CORE PERf0RMANCE f.'.a. Her.. Transfer and Heat Generstion (cent.) w

c....... !

4. Q 3,! I~ ~.c. results in a decrease of steam generator volume for making stasm and, fins 11y, ['f__ I

  • ', ~.;

supiiheating. The result is that less superheat will cecur and the stoam out-let temperature will be Icwor. L. :,, f k L' L., Decreasing feodwater temperature causes steam generator t e s~ N' outlet temperature to drop. (; ;.Q . n..... d What happens to the st:am outlet tamperature if the plant load is reducsd in 9+ ;y $~g a centro 11ed manner from 100% to 50%? Whan Iced is reduced, the feedwatar f.![ ., ~ flow will decrease siefwntly. The effact of this is that the same heat n ?, source volume is available to heat considsrably less sWm'y process. E7 .n-=s.: 1

t;_

fluid. This results in more space being available for superhosting and a re- .- s,- b.r, d.,i sulting higher steam cutlet temperature. .. w a n:.: ..r

g...,

e., ! cad or feedwater flew redven result in an increase in the .%.S Y,d:* b .,W e steam generator outlet tamperature, except at low p:nser levels.

v. '
1...,

F@+N j f.a The reactor coolant in a PWR system is kept undar pressure to prevent bulk ~-2 y TfW -% w> boiling in the core. In the esse of an ahncrmal transient, where this pros-

.m

@.S sure is lost and some steam is gansrated in the core, how will we know it? , wp a@., We will see a large increase in leval in the pressurizer until pressure is tE.y 1 4 m.x Lj ' V L;, ! W $. tR built back up above the saturation value cerrnsponding to the temperature g..- bM in the core. The stsam bubbles will then condense, and the level will drcp $dh .. m back dcwn close to its normal value. . TM d lii,.g .n 4 ..p,..( c.-v. e Uk i r.@p P-mblen my, mw b h The secondary side of a once-through steam generator has a net 3

  1. W value of 3500 ft. At the time of a plant trip, the folicwing q;

, m v... d.(1 Watus el ciwracteristics applied to the steam generatcr:

f..%.

M pn kp,%' .m v-mp c;;j hr.w h..t. &j l m . fl}x*W 7<. s s% g d W.'.i. 4-20 .,6 972P-B E.!.J.5- .g c. J N. "g&.=LGini Q.$5dI?%;p;;6:*Q%? %Q;E.G5ki;N&h&,%.'$v*'R ~. ' ' 5,p'"$% .w Am my mu n .:y=~ w h WM N?qMp n w % y pxd wrsyU N N;F %kk is 24 9 E M & Rt e rst$ % s % b. IMNN$d'M fjk*fh*O M3h Mh h w. c: B?%G e"&,.,F4 A pWiMMEMdEMPMPfMI/01Il3% h_.~EM.

  • %W.s 3

.pg pq q .}}