ML20140B433

From kanterella
Jump to navigation Jump to search
Forwards Followup Responses to Draft SER Section 5.2.2 Open Items Re Conservatism & Input Assumptions Used in Dysid Analysis of Erroneous Actuation of One HPI Train & Cadds Benchmarks
ML20140B433
Person / Time
Site: Midland
Issue date: 09/10/1981
From: Jackie Cook
CONSUMERS ENERGY CO. (FORMERLY CONSUMERS POWER CO.)
To: Harold Denton
Office of Nuclear Reactor Regulation
References
13785, NUDOCS 8109140180
Download: ML20140B433 (14)


Text

-

. ~ -

4 ConSumBIS Power James W Cook Vice President - Projects, Engineering and Cnnstruction General offices: 1945 West Parnell Road, Jeckson, MI 49201 + (517) 788-0433 l

September 10, 1981 1

i s

(

\\\\

y b[

Harold R Denton, Director L

Li Office of Nuclear Reactor Regulation Division of Licensing 99 SEP 111981 * %

US Nuclear Regulatory Commission Washington, DC 20555

        • @ in

/

MIDLAND PROJECT

/

MIDLAND DOCKET NOS 50-329, 50-330 4

to FOLLOW-UP RESPONSE TO OPEN ITEMS OF DRAFT SER SECTION 5.2.

FILE: 0505.805 SERIAL:

13785 Reference (a): J W Cook letter to H R Denton, Serial No 13364, dated July 23, 1981 Enclosures (1) Follow-up Response to Open Item 2(c) of Draft SER Section 5.2.2 (2) Follow -up Re., <>nse to Open Item 2(c) of Draft SER Section 5.2.1 Reference (a) committed CP Co to provide to the NRC follow-up responses to Draft SER Section 5.2.2 Open Items 2(a) and 2(c) by September 10, 1981.

Enclosed are the follow-up responses to these items.

With the responses provided in this letter, we believe Open Items 2(a) and 2(c) can be closed out by the Staff.

f f

JWC/ PEP /fms CC RJCook, Midland Resident Inspector DSHood, US NRC r

TPSpeis, US NRC DBMille r, Midland Construction (3) 0gl RWHuston, Washington 5r s

oc0981-0251a131 fi109140180 810910 PDR ADOCK 05000329 l

E PDR

~

Conservatism and input assumptions used in the Midland DYSID analysis of erroneous actuation of one HPI train are as follows:

1.

The initial pressurizer pressure used was 550 psig which is the open setpoint for the PORV.

In actual plant operation, the pressure would be lower. At 280*F RCS temperature, the minimum pressure required for RC pump operation is 295 psig, so the plant operator would control the

'ressure between 295 and 550 psig. The middle of this allowable pressure

' window" would be 425 psig which is considerably below the 550 psig initial pressure used in the analysis. A lower initial pressure would reduce the pressure reached at 10 minutes.

2.

The initial pressurizer level used was 180 inches. The range of the level measurement is 0 to 400 inches and the normal level for power operation is 220 inches. The 180 inch level will be a Technical Specification limit in the 280 F to 330 F RCS te.;perature range as noted by Item No 7 in the response to FSAR Question No 211.105. During actual plant operation, the eperator would maintain the level below the Technical Specificatien limit.

a i<wer initial level would reduce the pressure reached at 10 Linutes.

3.

The HPI flow rate into the RCS was based on a presetting of the HPI valves whicn allows the HPI pump to reach the pump run out flow limit.

In plant preoperaticnal testing, the HPI valves will be set to achieve a flow rate between the minimum required flow rate and the pump run out flow rate limit. A lower HPI flow rate would reduce the pressure reached at 10 minutes.

4.

An insurge temperature into the pressurizer of 300 F was used. The Technical Specification pressure limit is lowest at 280 F (sea FSAR Figure 5.2-1).

Use of the lower insurge temperature would tend to reduce the pressure reached at 10 minutes.

5.

No credit wac taken for:

(1) any letdown flow from the RCS which would decrease the insurge, (2) any pressurizer spray which would slow the pressure increase rate, or (3) any relief by the PORV.

The Technical Specification pressure limit at 280'F RCS temperature is 1540 psig which includer a pressure decrease adjustment for possible instrument error on pressure and temperature. The DYSID analysis, with the above listed conservatisms, resulted in a pressure of 1455 psig at 10 minutes which is 85 psi below the lowest pressure limit in the 280 F to 330 F RCS temperature range where operator action is one of the two overpressure protection methods.

miO981-0264a131

ENCLOSURE 2 CADDS BENCMtARKS A comparison has been made of the CADDS computer program with actual operating data. The results indicate excellent agreement with that of f

reactimeter data taken during actual transients. The two cases investigated were a turbir:e trip at 72% FP at Oconee Unit 1, and a unit senerator trip I

at 96% FP at Three Mile Island Unit 1.

Both of these transients resulted in a high RC pressure trip.

Primary side parameters which best represented the reactor steady state operation (core life, power level, boron concentration, etc.) prior to the j

transient, were used in each of the CADDS calculations. Actual secondary side pressure and feedwater flow responses derived' from the reactimeter data were input to CADDS to describe the secondary side behavior prior to and during the tran;;ients. The calculated primary side responses thus represent the effect on the primary side of transient changes in the secondary side.

Oconee Unit I Trip:

Due to a malfunction in the speed controller in the "B" main feedwater pump, a sequence of events was initiated which resulted in the "A" Main Feedwater Pump (MFDWP) tripping due to the loss of the auxiliary oil pump, and the "B" MFDWP tripping on high discharge pressure. This caused a turbine trip (immediately) which resulted in a secondlary side pressure surge due to the I

closing of the turbine stop valves. This is shown in Figure 1.

The RC pressure 1

and temperature increased (see Figures 2 and 3) due to the reduction in steam flow and the loss of feedwater. The reactor tripped on high RC pressure approximately 20 seconds after the start of the transient. The reactor started a power runback due to the loss of feedwater, and peak prior to the high RC pressure trip via the positive moderator coefficient as seen in

-y,

.m.

i-y-

2 Figure 4.

All measured data was recorded at 3 second intervals, so the response times can only be approximated. A comparison of the measured and CADDS calculated responses are shown in Figures 2, 3, and 4.

With the exception of the power peak just prior to the reactor trip, the CADDS calculated results agree very well with the recorded responses.

Differences in peak power may be attibutable to the moderator coef.'icient used and NI calibration.

1HI Unit 1 Trip:

A planned unit generator trip transient was initiated at Three Mile Island Unit i by opening the breakers while the reactor was operating at 96% FP.

The loss of load caused the turbine to overspeed and initiate closing of the turbine stop valves. The removal of steam flow to the turbine initiated a 1

pressure rise on the secondary side to the code safety value of 1065 psia in approximately 4.5 seconds. A feedwater pump speed " kicker" initiated by the ICS, upon a turbine trip, helped to keep up the feedwater flow, l

(See Figure 5 for secondary pressure and feedwater flow response).

l The reduction in steam flow caused a pressure and temperature rise in the reactor coolant system.

(See Figure 6 and 7). The ICS started a rod runback (20%/ min.) as can be seen in the power response in Figure 8.

The reactor tripped on high RC pressure in approximately 3.5 seconds. The change in pressurizer level during the transient is shown in Figure 9.

A comparison cf the measured and CADDS calculated responses are indicated in Figures 6, 7, 8, and 9, The calculated pressure response, as shown in Figure 6, took almost 2 seconds longer than the recorded response to turn fully around. This may be due tc the code's inability to respond quickly to the feedwater recovery near the trip time which appears to be responsible for the recorded response.

e

,.14

__--M

3 The CADDS calculated RC outlet temperature agrees well with the recorded results (see Figure 7). Delays in temperatures are difficult to account for due to differences in the code nodes and agtual sensor locations.

The agreement is goJd, between the calculated and measured pressurizer level response during the transient (see Figure 9).

No rod runback was used in the CADDS calculation (Figure 8), since in the 3.5 seconds prior to reactor trip, the power level decreased only s2% FP, and should have little effect on RC pressure and temperature response. A slightly negative moderator coefficient was estimated for this case based on the initial power level, EFPD, and boron concentration. The calculated effect on the power level was negligible; the measured effect was marked by the rod runback.

~

O e

D l

e 4

e e

_q e

d 0

m

.y

.,r,,-,,

,,_~

g__., _..,

4 FIGURE 1 OCONEE I - TRIP #21 1180 '-

1600 FROM OCONEE REACTIMETER DATA 1140 1400 o

Y FW FLOW STEAM n00 1200 PRESSURE e3 w

E N

5 o

1060 1000 "

i h-0 1020 800 u

O E

i 0

l, 5

o e

E 980 600 o

~

~

l S

l 400 940 i

900 200 l

I 860 e

t 0

-10 0

10 20 30 40 50 t

Time After Trip of Feedwater Pumps, sec r

e 1


,g-,

--.%__.._,,,,,_.-,7_.__,,-,,,,r_-

,,-_,,,,__,y,_,,_,__,,,,,_,.,,,__-__.-,,,,.%.,

5

~

FIG'JRE 2

~:

CCGNEE 1 - TRIP 521

']

t 4

2500

.?.,

2400 A

CADDS (K'INETICS FORCED WITH

't E

I ROD RUN3ACK) j l

j

\\

~

g 3

6 E

2300

/

I OCONEE 1 REACTIMETER DATA e

j

\\

,,.j; n.-

g en 3

I

\\

2200

/

I INITIATION CF AUX. FW o

[

/

I NOT INCLUCED IN CADDS m

I ' CALCUL ATIONS 0

\\

y 3

n 2100 g

\\

\\

y a

O

\\

2000 1900 t

t e

0 10 20 30 40 50 60 Time After Trip of Feedwater Pumps, see

---.,,.---.-,m,,--------w

.,,,,-.....,,-----mv.--,-.-.

---4

.w

- - -..,. -.. - - - ~

6 FIGURE 3 OCONEE 1 - TRIP 421 592 i

590 CADDS 4

I t p

588

/

g f

OCONEE 1 REACTIMETER DATA ti I

\\

{

586

/

g E

/

\\

h l

\\

l I

l INITIATION OF AUX. FW.

l g

584 I

}

NOT INCLUCED IN CADOS

.g

/

CALCULATIONS g

I h

582 g

I y

I

\\

/

\\

l

\\

/

580 I

\\ ^\\

/ ~S /

v v

/

(4 578 = -

J

/

S76 f

l 0

10 20 30 40 50 60 Time At ter Trip ot Feeawater Pumps, sec l

7 FIGljRE 4

^

OCONEE 1 - TRIP 821 b0 s

CCONEE 1 70 i

s 1

CADOS REACTIMETER OATA m =0.66x10-4 a

60 AK/K/ F l~

l u

l E

50 O

a.

l

~

3 1

40 1

O l

x

~u l

o 30 a

g 4

y 8

1 l

l 73 20 i

m C"

l 10 l

\\ %

l 0

-10 0

10 20 30 40 50

/

T.ime Atter Trip of Feedwater Pumps, sec 4

. e. eg aw w e se NN

    • ere NMW ee

=me

8 s.)

FIGURE 5 TMI-1 GENERATCR TRIP t 96% POWER l

e 1085

=*

7 cn 1060 i

STEAM PRESSURE

  • =a e,

e0 g

l 1035 6

y

=

c i

w N

\\

t)

E H

g l

1010 5%

g-p F# FLOW w

i M

3 985 4. u.

0 e

a e

m "J

E C3 0

960 3

8 g

m u.

N m

m

=

_m 935 2

1 910 2- ~

=

88')

6 O

-10 0

10 20 30 40 Time After Generator Trip, see i

9 s

I FIGURE 6 TMI-l GENERATCK TRIP t 96% POWER 2390 o

  • et CADDS

~

2300 y \\

g a

I m

>=

{

S W

2210 t

_3 1

l TMI-l REACTIMETER DATA

\\

=

W g

2120 1

a

\\

a O

. \\,....

,;c,......

+

j.

',, ~

2020 m

\\

e u

a

\\

o 1940

\\

m e

\\

\\

oa:

N N

,1850 N

g N N N

1760 N*%

'1670 J

I

-10 0

10 20 33 40 50 Time At ter Generator Trip, sec e

e e.==, e

.a..

emp #

b

,,,,._,n.---,,_.._,--.-.---,,--,-,,,,,-,----,,._---_,,n.--------,,n-,,,--

10 FIGUP.E 7 TMI-l GENERATCR TRIP t 96% POWER 610 CADDS 600

---J l

TMI-l REACTIMETER DATA 590 1

u.

b

.m H

su 580

\\

=u

\\

..........\\. R.

.,s....s70... ~..

n..

. ~...

a..

a

\\

O H

N u

S N

g

\\

560 N

550 L 540 l

5'30

~

t i

i i

-10 0

10 20 30 40 50 Time After Generator Trip, sec

.=


w v.y-w.<-

,y y-

.,,r--

11 FIGURE 8 TMI-I GENERATCR TRIO e cSM PC','iER r

105 CADDS

=.M tv 90 l

l l

TMI-l REACTIMETER DATA 75 M

=

3

-4 s

0 lc.

. f.Q.'.

e '..n.. m g*. r. 'w...,..,..

s.+6 a.s

- =., s_

,.,,e p

t-

.,.s..

=

a

.s.

?.g..

s s...

  • s; I

w to l

E

\\

O 45 u

g O

3

\\

j o

CUW ct 30 l

I

't 1

1 15

l

\\ % **** % % **** *-* emene m mmm O

I i

i 10 0

10 20 30 40 -

50 Time After Generator Trip, see e

I

--,-m

,--m.

__-.,,m-----m.-

g--e.-m,ee.-4--y e,e

,r-p~er,e e,a_,ww,,a..m-,-e-e-,---w,-w-e-y----,y- - --+e-+--ww

,e

---.q--wa

,---ee-m--v-<-

12 FIGURE 9 TMI-l GENERATCR TRIP t 96% PC?FR 320 280 240

/

g CADDS es

/

5c D.

200

\\

TMI-l REACTIMETER DATA u-<e e

s

..... u..e

.1_60

...c., ~.

.m

.......;.....a.

. c............

.c..

.....;.,......... m.,.....,:..., :. -

.a...

N

  • e4 k

s nW 8

120 o-N N N 80 l

g l

\\ \\

40 h

t O

10 0

10 20 30 40 50 Time After Generator Trip, sec

=

  • e e-4 ame w

ye

---+w

,---e--

__m---w-.--,.-

%m

,me


w.-ve.-

,-e, w-----

p.=---,--e-.-.s

-*----v

--,e3,-.-----w

---.w-.-

,- er w-

-