ML19221A623

From kanterella
Jump to navigation Jump to search
Describes Reactor Simulation Tests Performed or to Be Performed by Billings Energy Corp
ML19221A623
Person / Time
Site: Crane Constellation icon.png
Issue date: 05/21/1979
From:
BILLINGS ENERGY CORP.
To:
References
OLS-790521, NUDOCS 7905230461
Download: ML19221A623 (9)


Text

_.

~

~. :

[h 3..

c\\l i

5 4'

Reactor Simulation Tests Performed By Billings F.norgy Corporation 1

t-

+

, p.,

. C....

L, l

Current as of April,10,.'1579.

All tests described below l

.~

are. performed or will be performed on the Reactor Simulator

~

(Figure 1).

s.

TEST

'A April 6. 1979 The system was pressurized to 1000 psig (nooinal) and he ted to 280 F using a primary heating clament simulating the core and a secondary heating elament around the pipe leg.

A band ' heater 'on the steam generator was also used'.

~

During. test, the sacendary heater was disconnected.. The I

s'

.~

primary heate'r was 'used' to' maintain 280 F.

This heating element was. controlled manually in an on/off fa.shion.

The data plot ,

~

y

. "..shows pressure ripples that are coi'ncident with the temperz*nre i

s

{

.f

\\-

\\.

- _ Wariatich' associated with.the heating cycle.

U

.s

~

,?

n.o -

Water was dr' awn' frem thtase of the reactor vessel in an

(

e s

.~

[

~

amoun't that-produced approximately.:100 psi pressure drops.

The

,g.

.t

.7 va

_}

7,,.,

water sa=ple-passed.,through a heat, exchanger in an ica bath to

^ y i,-

'~,.'

coo 1* prior to measurements The mean temperature of t!be water existing in the heat' exchanger was.86 P.

The volume'o'f water t

J. k* e -

at s,

i..- :.

was measured directly with grapuated. glassware. '

=

. Py., -

The plot,o_f Test.' - A shows graphically that th( water van *

> g..-

a

.g.,

.. _ ;., not saturated with hg..g. en until: a pressure of app 0 4==tely...

c,.,

. g..

g..,,..

':,300 psig was obtained.' ' At this po,imit a, definite ppwsiure re-. -Q 7 ' l b_

i;;.

.=.

's

,., 1 ~~l

^

.t -

' bound,. characteristic..bf saturatioc. w-. *-w, f was ' observdd.n.. :The. f act i

~

1.,.,1 e

~.

n.

.....,.an, r..

m./'Q that the, oolution v.ss not%turgtad at.clooO peig was _ doe to

..n

~ scee procWal difficulyes ketEnized'in setting up for

~

s.-

. :W.l

~

~

s

.bb 0$0.

~

~

'7 90s D O VR k

. w.,

r:

. ;.- m

,..g i,,

[',

3..

7 s '%"...

.1

).

_, n

,... :sts e

this first test.

i The data shows, however, that 3-

cordance

' - ~

g,(.

j

.t

,.With the l'aboratory pressure drop testsj the pressure at

'N %

. 'v.hich saturation occurs can be determined by wabMng for u.

e pressure. rebound af ter an aliquot is extra'cted.

The hydrogen bubble volu:ne to system water volume ratio corresponded to 0.4 per cent at'300 psig.

By dropping the pressure further (to 100 peig)'the bubble volume grew to 6.5%.

I (Note that hydrogen bubble volume is inferred from measure nts of. water removal.

No correction has been made in the ula '

s

~

. tion for volume contraction of the. pressure vessels as pressure

'is decreased.- This effect will be examined in Test G.

i Test B April 9',

1979 l

Test B was performed similar to test A with the' exception

..s..

~

. that'the. core,sinulation heater was controlled via a variable 2I s.

.- T power transfor.ar rather than an on-off switch'.

As a result,.

U' k

s,-i-

.. the pressoro..r.ipple due..to beating variation was no longer in -

- kDW T

~. avidence. '

,, y.;.

r, w-

~

c

. Step,'clianges in vessel pressure were again caused by.

I

-. ;taking incremental volu=es of water frem the'.b,ase of tbs reactor.

sD-s.

The plot of Tast B ahows pressure rabound ef ter, the first 4

.x c.

s.

,u,tincrement.of water was removed.

This indicates that. hydrogen -

?

. g-saturation was achieved at'a pressure [in' excess'of 1000 psig.

?...

~

i.-...

A.r

' ' -- ?

.y

.r s ~A-

'.t iceerdi$41y,. the" fraction of bubbli volume to kater system h-

~

s

(;.,.

s',. -volume wasrruch greater thad 'in test' A'.

.,.....e.

At 30( g.p ig, for in-

-e

.., e.

d.

" stance, ' the bubble ' volume. compriiod ',9.55 % of.M6tal. systerm

.*[-

.x.

s s as compared with 0.4%.at the sama peecsure in'tast.A..

,gr.

L.

..rs aj.-

166 051

6:

=

F

..e j-7 7,

l4. f g

,Q. :a :.'

t

'[

x i.

-3

( :,

. c., y.;,..

-~

I 4

At.. the conclusion. of the test, the size of the bubble in the steam generator was measured by exhausting the 'g'as through" a heat exchanger and measuring the volume by displace =0!tne of k-I

\\.,,

water.

At rocm temperature and atmospheric pressure, reabsorpg 7

g tion of hydrogen in the displacement water.,was assumed sibl.

..The bubble at the top of the steam generator was obtainad by u

n

~ maintaining the final pressure with the pressurizar valve 'into

.n.

the system.

The valve' at the'. top of the steam generator was 2

e then opened slightly 4nd;,the fluid passed through th'b' heat

~f exchanger.

When, liquid was obtained, samplingwasdisenktinued.

i

7),* The5 as v[:ilune in the. steam generator adjustad to ' 280"r and.300',,.

9*

f s

s.,,..s.

~

./. J c$

psig, conditions existing at,the.end of the test, was very 4.-

.. - - w,

., a g

' ' ~

small compared.tio. the hydrogen bubble contained '.in the ' total

,,f

- system.

Of the total hydro 9en bubble, 964 existed in the reactor

^*h y3. h'

~

and 4 t in. the.. stean.gogetator.,-

. a,, t _. '

n 7

-~

c l

,..,.s.-

,., [,,

Although~ t.hs stemn' generator As physically high'ar than the

._re' actor, thers.ar thr[tefef.fpcts that may contr to' to i-q ;'

^

t, t._

,s

= :, e v h,d'. hlacement'of thej major'.: portion of the 'bunble in-jths).. reactor..f,,

- s,.

.a

~

.u..-

. w,q

,n..

Y',%. j e;.;... 3

~

loca'lized 'prassure' dd,bp h- ~. ',;., @/G

'? *4

' These effe^ cts aMe relatsd'to 1)

- 7

-.t4..,...,

.1, if n.

-N.., e.,~ ~' the ' reactor; 2) dre,fergntia), removal; off hydrogfn3n. the.,-

^

_t

..,..i..,,s.

..,,.7.,.

t,

.e

.~

..s v.. -

s.

s-h r..

c.

z reacto Cdue to eat-effectN at.the core simulator:insater;- and.. -

i%,* ~ --.

3) sweeping actice of the,.twater flour which convtrets hydrogan'i;-

. s.,.

. -. m. t

-w

......~.;...-.... ~.

a.

3

' ; / st n.

g.. +..

-. bubbles fraca the' staan geerator.to the reactor where they

=-

1,,,

166 052"!

7

. ' count.in the upper half volume above the exit port.

w..

.', i %. ".; y :

~

~

ih D.

,. us. ' ~ ', i -

r

.e 4

W,

.. i W

+..

"? 3

,-t

- -~....

5 i

y,

%st - C

  • y. '
  • I Eo test nado e.

Test - D April 9, 1979.

ss 1 4

Test'D was similar to test B with the except. ion that the e

water withdrawal rate was continuous.instead of periodic..:-

t Although the. water had been previously saturated with hydrogen, the hydrogen saturation pressure had decreased prior to start of test,. cm is evidenced by the data plot.

Bubble growth s

'w.as only 3% of the system water'voltaa.

e Test - E.Aprfi 9. 1979 -

c-Tha continuous,, sample method of Testi ti was rebested in Test

' E af te,r re-ests.mlishing hydrogen naturation at 1000 psig.

The s

y-

.r

.figure shows a much more dramatic growth of bubble size with g

  • l Iy f

pressure decrease.

, e, '

As in all previous tests, the water temperature was held t-

~.

at 280 F.during'depressurization.

k

[

V"JF5"--v.sfirft W 1pril 9, 1979

'^

,,/.,'

... ~

., Test P was a repeat,.of test'. E with contirincus water removal.

The ~ only./ changentin'de was that the water was drawn l fred.,ah( p

...,; ~

.i at the. base'of the pressurizer instead.of sti b hn== of tha'..

4 y

.. b

.. reactor vassal.. This chango was auuin' to mo. ro closely minulate

.i

=

. p g..

z

.g.

7 the withdrawal ~'of water frem the_pressuritor and.also to ses,,

t.

f' C.,^ *.

2

[.,'

"P.5

.y%.

e

. j.,,. if. A graatar percantage of *the hydroge,n buhble yo,.

uld "f ors,.in'd. '

,L

,,. r.

7

. y.

~.

z!,:t h,

. l, ?..p'..'

~

thd.* steam generator.

,t

.,.:c Assulta-wers very si=4 Yar to tast' E.

A'a'lighp,1y greatarz

~.

~a..

l,...

. ?

.k M

n

. hydrogen bubble was created in' the.systes' a 2300 peilr~in test E.

i

~ ;

'.. J j,

l The amount of hydrogen volusto present in'the than in test F.

l 166 053

7

- ~.

, ~s c.

-s7 s.

s y x :,..

e.;

t

~*

y 1<,

0 J

steam generator was still asall in comparison to the t.otal 4

bubble size 1 indicating that the location of the water withdrawal t.

tap was not a significant factor.

A cross plot of bubble volu se vs syste:s pressure is

  • 7

^

-given for runs A, B, E,'and F.

Gompk Test - G (Tet-i.c im W formed 4

~

Part is Using unsaturated water the system will be brought up to temperature while measuring delta p.

Pressurization above the boiling point will be accomf'.ished'by applying hydrogen to the pressurizer,.

t is assu:ned that tha. surface area of contact s

will be sufficiently small and the presuure sufficiently low

.that the ar.ount of hydrogen going into solution will be slight.

i Part 2:

The system will be depressurized as in Tests j

e,. A. '. '

,,D,.,,E, and F.

This run will establish the system volume decrease with pressure reductiosias the vessels. contract.

Measurement of', delta p will'also be'made to establish a>

a

,; 3

w... referanco signal for; ;the c.on. dition of unsaturated water. l >

..A..

g.

'.'.i Test - B (Yet to 4:e performed) e w

i y

'In tost B the,, amount of hydrogen that enters the system

,^

will bi asamur45 'as' pressure'.is increased at constant t:supera-F,

.A

,y 4

tureof2tb*F.. E M an'.will be wit $1rawn[ frets a hydrogani,',,

h...I (,

.,3

. y..

.. cylinder of known.y~olume and temperatufe,, Mass of hyd.v W.c

..r p.,'...

~

m.

. -^,9..

.. ~..

,.. e

..; fue:9ved-frees the cy)inder will be. calculated f.z:pm the pressuro....

~

c,.k..;

_, ~.

^

c

. g. g,lg ;'

g.-

p

, Qm of thelcylindar Jaa it aerptias.

r

.8

' n ' - daturated' water 'will be obtained at several per' lures by"'. -

~

,~

_. q s

(

pressurizing 'and observing preasure.atability.

~

8 W

s.

G*

f.

a

  • e 166 E54

C r'

t I

f l.

'Q r

c s

,4 e

..e.-

1

. c;'.

~.

I

  • ~ -

~

....~;..,

v ont of delta;p will be made a.,t each saturation step

, Maasure a,

c.

.c to ces if a change in either flow dyna:2icsi water density, or noise can be ob served.

Test - I

_c M -perforr.ed)-

m-

.,, Af ter achieving a saturated sointion at 1000. psig' and 2"80 F, t, '.;.,J.

. the:syst m will be. copped in ta=perature and pressure in

?,..

separata steps.^s s

Part ~1 will be a drop in ta=perature from 200 F to 130 F

~

r at constant pressure.of 100.;psig.

Pressure will be maintained l

^

~

y

_ ' +,e y-constant througif use ch the pre =surizer'as needed.

The volume

'~

p

.. s a

.,.of water in the pr.essurizer before and after test will be

~

W x.

o b t & "i.

N-m.. w.'

?

A.

.Y'.

y. .. # -

~

r m

r Pa.rt 2 will.<be' a co.a errt,Druous pressure drop from 1000 '.

e

~~

.w w,

y...

_ p

4.,,

q

-i:

4-psig to 300.piig by water prawal frota.the.s/ stas.

Te=perature.

.'p. j ur n

,.I will be hs1Fconstant n't'. 3,00'F, g,..

r..

4

,,.',../.

,, Maasureranti of ' del'ta p wf1I'be-taken 1.n.,both parts.

Thg

.7 peak to jeak.noiseievel'. o'f the delta p signa 1. hilITDepot6d ' ' Y

  • ~

j

  • **' ' ~7
q. f, <

T*%

,.,'. 'j on.a strip],. -1.

.i cbart-recordar2

^.. -

~

2'

%tJ;fl -

Y'

,. p'W

~

',.%~*r-.

- W.

Test- -c (proposed topeat of Test 5 in order to perform ~ Test 4)

v;.

!.w. i... u.,..%.c %.. s.,

m, e

,,w.s.

k 4.

r;

. +.....

- i,. r w

.u,

~

M- _(fgep6 sed repeatipf.. Test,iITwith, reversal of the orderr. ""'$

.V' "

Tm

.p

..s,%,

e.<~-

}1 a-

  • ? :

'..;. 7

.m y'.

j,

.' constant tsopera'ture pressure],raduction followed constant

~

~.

w l

~' '

.-i,

[ ' '.':y.pfessure ta:sperathre " reduction'.$ --

, n

,a n -

f*s.

e SS: 999 B5EPrg6=1 J

~

e-1

.e 4

f,.* s' 6'

,d

'p

+

~

t-s; y.

g g.

.,, m u.

s.-

.. - ' a.

.y y d.

M' 4. 2,n..

y-1

,y-.

e, 6,

.~... %. ^ k.vf

n. ~....
r. w. v. r*

.c.

.c.

i*s s

g%

^ y..*

.*

  • e.. _

r~

1

..q., -

4

~r

.4' e

t' C

~ A. 1 e.

. ".Y %)g.

e.

g w*.

.,aq 7

- *, '.., St y,,,

, r s.

..cn 4;-

...y.

u.-.

g

.~

, b, 3

3

4. '.s Q *. d l

,\\

l e

L-

.~

.e g

1

's M. h 4

[*

fg

[,

.)..

d

(-

-~

..i.w

.w

,*.m.

s **

e r -

$4..-

?

~ 7..

l r

=

r s b C

e e

6>

g.

s,

. l. Q.. Li.ll8g1,l.t)8aE:w,. -

s...

c.

.....r

. ~. -

,f e

.p.

2 y

3

.c

. E.gp-

[

~

g:

m s_

3

& ))))))

, ~ ~

t ex s

~

t $$

,., g

\\ _ ~ P.W -

,y

\\p v.

I p

e i

.g g *.

h, g

r g lx f,, y p

+

's a

N.

=

s.

r a

J g

X 4

.e g

-l41. -h'

~

E

y

_f(-

166 056 s

w. ?

4_

4

.. ~.

_ c

~

3,.

-,/

...A %O.. O ',* N.*[M i 1

v.~

.....J p.-

....., "...,c&m w

e y,pog ge

,y ~

o gm.-

n e

r*

_me

.e.

,.j,.,.,

-a c

.. -.- * += g;J ;,,,7.,,.y\\

',-A,,

,,d - *

. ~,s e

.py sg ra -

s a.

6..

.. a

., e

- W '"t..' w

  • >.ha.w.'aca

.,.,s=

~

T O

-j,}

'4-. 2 L G 4 3s

. g a

g g

, g-a g

g.

g g

g g.

4

'- 5 a

a e

a a

-; +

,7.;

f I;

),

- ~

yll l

  • . &r.'

N j

4,.

l l

J

\\

i 8,

M sass::3 q

~

qg g

Q d

8..

Q H

Cf3 ' g N

C=

t--

4

-- g d-1 g

me Iue

~

p tr.J e

~

s

. -.m

+

2

~W.

, ~ _

. = ~

=

,. Q v=.

e i

1 p

t 5

. 2 s

_~.

j y

p

..--ep.

w ff se hJ --

-g f-

.EQ j

=<

t s

-y.

. j-s

.4 l.

Q ',

>;_e' am

,p.

f. *>

    • 2

.rg f

,4 4:

fj, i 4,8

'g a

i

  • }

e

.3,

?

- ^

f 4,, ~

4..

=*

g.,

' ~,.

/*#,

D s

a

.s s

p e' y

, g g-

,, J, hj er Q#

7, n

g g

,,a

-e M

w.-

.. 1 t

r O,

i' f-9 e

f n'

I 9

.t f

~,

.m

-1t l

G -.

O ! CO f%

'O to t

Cr)

N a

N 5

O-Ibb 057 ~

. n.,

s-e

  • r x '70A anyn wasAsno^ 37ssnS N2SO2f0M n

g t

I t

f Of U2.

on 4Q mbwsonskwuT S{Io~ f/W.7*)

+

i t

u

-s 6

r..

R EllCTOR.SMUTIG rt37-I 4/1in3

. ::.e s.,

=.

y: :

.),x~p

\\

s--..

3nco..

~1 1

?

,'. i.'

  • ,. t.

+

r

.,4.,

.s

,.c g

,3

=.

3 g

\\

~ ~. a

.+

+-

+

%. 3 4500-

'y a

~

.~.

y ELTA P

.r 1;., +

- e s,

.3

4000, M~

t 4

> +-

g y

c.

3500~ "

.3 Q

.'^.

a,

y 00

  1. [ '

.g...

, p.

g5 g

g N

3 t..,I.

=-

s p-2500 t

I-4 L

g

.y g

.4 oc0

~

t2 Toezarrme 3I

-.y

,y

.L

..g.

p e

e..

j

- loco r

jgg 6

t 160 058 L

i i

i

. r

-i t

0 4

0

.i 0

20

- 4 8

8 ' 188 129 (G

160 189 288 p

..