ML17053A592

Expects to Complete Generic Review of Mark I Containment long-term Program by May 1979.Requests plant-unique Analysis Shortly Thereafter & Completion of Plant Mods by Dec 1980. Forwards Evaluation of Suppression Pool Temp Limits

ML17053A592
Person / Time
Site:	Nine Mile Point
Issue date:	03/12/1979
From:	Stello V Office of Nuclear Reactor Regulation
To:	Dise D NIAGARA MOHAWK POWER CORP.
References
NUDOCS 7904110122
Download: ML17053A592 (22)

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Local PDR NRC PDR VStello BGrimes TIppo1 ito

Attorney, OELD CGrimes DEisenhut TERA JRBuchanan ACRS (16) 0181E (3)

PPolk SSheppard Docket No. 50-220 hir. Donald P. Disc Vice President - Engineering t1iagara htohawk Power.Corporation 300 Erie Boulevard

'West

Syracuse, flew York 13202

Dear ter. Disc:

RE:

SCHEDULE FOR THE IHPLEthEWTATION AND RESOLUTION OF THE hfARK I COtjTAIHhlENT LOtJG TERt)

PROGRAM v

O ORRICR+

The generic aspects of the Hark I Containment Long Term Program (LTP) are nearing completion.

Me have concluded that it is appropriate at this time to establish specific schedules for the implementation of the plant-unique aspects of the LTP.

lie have scheduled the completion of our review of the Load Definition Report (LDR) and Plant Unique Analysis Applications Guide (PUAAG) for Hay 1979.

Upon the completion of our review of the LDR and PUAAG, we will,advise the Hark I Owners'roup of any specific exceptions to these documents that must be addressed for a satisfactory LTP plant-unique analysis.

Your plant-unique analysis should be submitted as soon after that time as possible.

Following our review of your plant-,

unique analysis, we will take appropriate licensing action, including a license amendnent, to assure the timely completion of the LTP.

At this point in the program, you should be in a position to know the majority of plant modifi'cations that will be necessary to conform to the LTP acceptance criteria.

Therefore, we request that, within 60 days foilotnng your receipt of this letter, you provide a har-chart gag schedule shoeing the time periods for the installation of specific q

plant modifications.

Your schedule should be directed toward the completion of the needed plant modifications by December 1980.

Should you be unable to meet this targeted completion date for the installation of the major plant modifications, your response should include sufficient justification to demonstrate your best efforts to aoa1.

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Nr. Donald P. Disc I

An issue that relates to your LTP implementation schedule is the use of Rramshead" devices for safety-relief valve discharge.

The enclosed staff evaluation discusses our conclusions regarding the basis for the definition of the ramshead threshold temperature (ieeee stability limit).

As discussed in this report, the quencher discharge device has been shown to significantly improve both the loading on thy con-tainment and the'ondensation stability.

The quencher device has been shown to provide the necessary improvements in the containment, load-ing and the con'densation stability, and you have informally advised us of your intention to install, quencher discharge devices in your facility.- Please identify when the quencher discIiarge devices will be installed.

Another aspect of the,resolution of the LTP concerns the licensing fees required by 10 CFR 170".

The LTP constitutes a "special projectR

'as defined by that regulation.

As such, we have determined that the fee associated with the generic aspects of the LTP will be-based on the manpower required to review the LDR and PUAAG.

The responsibility for this fee will be shared by the Owners Group as a whole.

In addition, a fee will also be imposed on each individual utility for the lic'ense amendment associated with the LTP.

The fee class fo'r the license amendment wi'll be based on the manpower required to review the LTP plant-unique analysis and any related changes to the plant Technical Specifications.

As discussed above, your detailed schedule for modifications should be submitted within 60 days following your receipt of this letter.

If you so desire, we'will m'eet with you to discuss your specific plant modification schedules.

Sincerely,

'Priginal 8ignl.d hy b

Pictor stella

Enclosure:

As stated I

cc w/enclosure:

See next page V. Stello, Jr., Director Division of Operating Reactors Office of Nuclep( Reactor Regulatlou

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Niagara Mohawk Power Corporation cc:

Eugene B. Thomas, Jr., Esquire

LeBoeuf, Lamb, Leiby 5 MacRae 1757 N Street, N.

W.

Washington, D. C.

20036 Anthony Z.

Roisman Natural Resources Defense Council 917 15th Street, N.

W.

Washington, D.

C.

20005 Oswego County Office Building 46 E. Bridge Street

Oswego, New York 13126

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EVALUATION BY THE OFFICE OF NUCLEAR REACTOR REGULATION OF SUPPRESSION POOL TEMPERATURE LIMITS IN BWR FACILITIES

I. Introduction and Summar Safety-relief valves (SRVs) in BWR plants are used for reactor vessel pressure relief during either anticipated plant transients or accident situations.'hese valves are installed on the main st'earn lines. of the reactor system with discharge lines from the valves routed to the suppression pool.

When the valves

open, the steam i s discharged through the piping into the pool where it is condensed.

A discharge

device, which is'ffixed to the end of the piping beneath the water level in the pool, serves to mix the discharged air and steam with the pool water.

The most common discharge device in use today is the ramshead type, which consists of.,two 90-degree pipe elbows welded together, as shown in Figure l.

During SRV operation, when air and steam are discharged into the suppres-sion pool,'vibratory loads (due to bubble formation and subsequent collapse) are imposed on the containment structure and components within the'-pool.

The characteristics and magnitude of the load profile are dependent upon the type of discharge

device, the temperature of the pool, and the mass and energy discharge rate.

For the ramshead

device, the two most significant loads occur during vent clearing and subsequent steam condensation.

When the latter loading condition occurs at elevated pool temperatures, condensation becomes unstable and significantly higher loads result.

Because of this pheno-

menon, General Electric (GE) has proposed a pool temperature limit for all plants using ramshead devi ces to avoid operation in this unstable conden-sation'one.

GE's proposed threshold for unstable condensation is 150 F

for, the bulk pool temperature and 160 F locally.

Justification for the limit was supplied by GE to the staff in the form of topical reports (References I and 2).

These reports contain the experimental data base used by GE to establish the temperature threshold.

The initial concern arose, from an event that occurred at a foreign plant," that caused damage to the containment and subsequent leakage from the wetwell.

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We have recently completed our review of the GE supplied justification for the pool, temperature limit.

We and our consultants (from BNL and NIT) have concluded (Reference

3) that the data base alone is not sufficient to support the GE proposed temperature limit because of a lack of'full-scale SRV ramshead discharge load data.

First, the data base consisted of small-scale elbow and straight pipe data as well as small-scale ramshead

tests, with no scaling analysis provided to show the direct applicability of such tests.

Second, the results showed substantial data scatter.

Limited plant operational data were also provided, indicating that local

. pool temperatures of approximately 165 F have been experienced during a

stuck-open SRV>event without.any evidence of structural damage.

This experience can. be considered as supporting data for the limited-mass flow-pool temperature zone that occurred.

However, it cannot be considered as the operational basis for all potential events.

We have, therefore, concluded that the GE bulk suppression pool temp-erature threshold of 150 F cannot be adequately supported with the existing'ata base for the ramshead discharge device.

We can,

however, conclude that the actual temperature threshold is in the vicinity of the GE proposed limit (i.e., about 150 F).

In light of our current understanding of the ramshead device and since actual plant pool tem-peratures could approach the GE-proposed limit, we believe that the ramshead device should be replaced to preclude the unstable condensa-tion. phenomena.

The basis for this conclusion follows in Section II of this report.

A "quencher" type of device has been used for several years in foreign-based plants.

This device was developed to improve the performance of SRV discharge at elevated pool temperatures as well as to reduce the air clearing loads.

The principle behind the quencher-type device is to promote the creation of large surface areas of air and steam bubbles for rapid mixing and diffusion rather than the jet type of discharge mixing provided by the ramshead device.

Thus, the quencher consists of pipe sections that contain many small holes, either uniform or graduated.

along the surface to promote and enhance diffusion and condensation in the pool.

The quenchers are typically referred to as either the "cross" or "T" types, depending upon their geometrical configuration.

The data base for several quencher-type designs has demonstrated superior performance at elevated pool temperatures.

Characteristically, a quencher-type device has not exhibited the temperature threshold phenomenon that

. i<has been observed for the ramshead

device, based on the test data gener-,

ated to date.

Pool temperatures have approached the boiling point (i.e., greater than 90 C) without any noticeable load increases.

Hydro-dynamic, loads on structures during vent clearing are also reduced, due to the inherently better distribution of the steam/air mixture in the pool.

The use of the quencher device would therefore lead to larger safety margins.

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Based on the available data, we conclude that a design basis suppression pool temperature limit has not been adequately established for the ramshead device.

Furthermore, we believe that, even if full-scale ramshead testing were performed, it is likely that a temperature limit would be established so that operator, action would be required during SRV'ischarge transients to ensure that the pool temperature limit would not be exceeded.

(Note:

Full-'scale ramsh'ead testing at 'elevated pool temperatures to establish a

design basis pool temperature limit has not been proposed).

Therefore, in the absence of any further information on the ramshead, we conclude that it should-not be used.

We also conclude that the quencher-type device provides improved safety margins and can be used in all BWR plants with water suppression containments.

The comparative benefits are given in the following table:

Table 1

SRV DISCHARGE DEVICE EVALUATION

SUMMARY

Device Local Temperature Limit*

Remarks Air Clearing Loads**

Ramshead 160 F

1. Test data do not support the pro-posed limit.

2. Severe vibration occurs if the limit is exceeded.

+21 psi,

-10 psi guenche'r 200 F

1. Test data show no severe vibration for tank water tempera-tures approaching boiling.

2.

Steam condensation loads are about

+2.2 psi.

+6 psi

-5 psi

• Minimum temperature limit for onset of condensation instability.

• • Peak positive and negative torus shell loads observed in the Monticello in-plant tests.

, We, have considered the bases for interim operation of the Nark I

..plants, currently using ramshead devices.

~ The SRV loads are cyclical in nature, thereby creating the potential for fatigue degradation

,. of, the, containment.

For currently operating Mark, I plants, we have,.

.determined that there is sufficient fatigue margin to permit continued plant operation while a new discharge device is being developed and installed.

Al,though some damage to the torus internals has been observed.

due to apparent SRV operation, there has not,been.

a loss of containment integrity or function in any-case.

.II.

Evaluation of Su ortin Data for Ramshead Device In late 1975, GE submitted a topical report (Reference

1) to support the temperature limit for the. suppression pool when using a ramshead device.

The report, however.contained test data for SRVs having a

straight down pipe discharge devi ce and no test data for the ramshead device.

As a result of our evaluation, we conclude. that the data base did not support the proposed limit.

In response to our request, GE provided additional data (Reference,

2) that contained three sources of test data:

subscale test data of ramshead and elbow devices, small-scale test data of straight-down pipes, *and plant operational data.

Results of our evaluation of this report are discussed below.

A.

Local and Bulk Tem erature Differences

.,Local temperature is referred to as the water temperature.

that is in tHe-vicinity of.the discharge device but not

, in contact wi,th the steam bubble.

Bulk temperature, on the other hand, is a, calculated temperature that assumes a

uniform pool temperature.

Bulk temperature is normally used for pool temperature transient analyses.

Because the test facilities are confined pools, the measured temperatures are considered to be local temperatures.

This has"been confirmed through evaluation of the test data.

Generally, the test results show less than a 2-to 3-degree variation within-the test pool.

To allow proper interpretation of the test data, GE performed a test at the squad Cities plant.

The pool was instrumented with 18 thermocouples, 6 of which were located in the vicinity of'he discharge device to determine local pool temperatures.

The test was conducted by continuously dischargi'ng an SRV into the 'suppression pool for 27 minutes.

Throughout the transient, the results showed that the measured local temperature did not deviate, from the,.calcu-lated'bulk temperature by more than 10 F.

Based on this

result, GE has suggested that a difference of 10F between

,local and bulk conditions be used.

We concur with this evaluation of the test data'.

Based on thig, temperature difference, therefore, the GE-proposed 150 F bulk temperature limit is equivalent to a

160 F local temperature.

Test results then represent local temperature conditions.

The following data evaluation is based on this. assumption.

With respect to the quencher

device, the magnitude of the difference between the local and bulk temperatures has not been established due to the lack of an adequate data base.

However, recently performed in-plant tests are expected to provide the necessary data base.

We will continue our review of this matter.

B.

Sub-scale Ramshead and Elbow Data Sub-scale tests were performed at Hoss Landing Test Facility and in a, separate test facility in San Jose, California.

These consisted of seven tests using a ramshead and 37 tests using a 90-degree elbow.

The mass flux ranged from 50 to 195 ibm/sq ft-sec.

The local threshold temperature for steam condensation instability calculated by GE for each of these tests ranged from 152 to 176 F for the ramshead and 146 to 172 F for the elbow.

Based on the following specific concerns, we conclude that the applicability of the sub-scale test data has not been adequately demonstrated and cannot be supported without addi tional testing.

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Seal in Law A 1 icati on:

We know from our, experi ence with the Nark I pool swell phenomenon, and from the work that has been done by the Mark II Owners'roup on steam condensation chuggi ng, that small-scale modeling laws are complex and must be established from fundamental principles and carefully applied in model testing.

No such modeling 1 aws have been deri ved for'he SRV di scharge phenomenon.

,Test facilitie's were not scaled to simulate an actual.

, plant.

Therefore, neither dynamic nor geometrical similarities. can be established by the tests.

Furthermore, GE has not justified the assumption that scalin'g 'has no effect on the temperature threshold.

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the-sub-scale test..results.

As noted previously, the

. temperature threshold ranges from 146o to 176oF.

With such a wide scattering, the probability for. the tempera-ture thresold to be below the GE proposed 160 F is relatively high (16% of the sub-scale data points fall below the limit).

Small Seal,e Strai ht Down Pi e Data This data set was obtained from foreign tests (Reference 1).

The tests used a straight-down pipe and yielded 12 data points.

The threshold was defined as the pool temperature at which the peak-to-peak pressure oscillation first reached 2 bar (29 psig).outside a circular projection with twice the-pipe diameter on the floor of the tank.

Results of the tests show that all data points fall below'he 160 F

limit.

However, the straight-pipe discharge is phenomeno'-

logically different from that of the ramshead device and therefore this data is not applicable.-

D.

Plant 0 eratinal Data The,GE memorandum report (Reference

2) provides actual i n-plant data.

Five plants have experienced SRV discharge into the suppression pools where temperatures in excess of 100 F

were reached with no reported instabilities.

Specifically, the highest pool temperature from those events ranged from 122 to 165 F.

However, the report only provides detailed data for two plants identified as Plant A and Plant C.

Data indicate that Plant A was manually scrammed before the suppression pool temperature reached 110 F following a stuck-open event.

The suppression pool temperature increased rapidly and reached 165 F when the reactor pressure was 184 psig.

Plant C reached 146 F only because the reactor was scrammed at a

lower pool temperature.

Figure 2 shows. the loci of the Plant A and C events on a plot of pool temperature versus SRV steam mass flux during blowdown.

It also shows the GE-proposed pool 'temperature limi~t. It is clear that the plants experience SRV discharges far below the GE proposed pool temperature limit at virtually all mass fluxes except the lowest.

" Thus, their experience does not provide support for the higher mass flux at the GE-proposed limit of 160 F.

III. Discussi'on of SRV uencher Dischar e Device Desi ns In 1972, a foreign BWR plant'ith water pressure suppression containment experienced severe vibratory loads on the containment structure during extended SRV operation at high pool temperatures.

The loads were severe enough to cause damage to the containment shell and components and to result in water leakage from the suppression pool.

Following this incident, extensive experiments were conducted to investigate various alternate discharge configurations.

The objective of the investigation was to develop a device that would reduce the hydrodynamic loads during SRV air clearing and provide stable steam condensation.

Varied configurations of the discharge device considering more than 20 design parameters were investigated.

Results of the investigation concluded that the quencher-type device yielded superior performance.

Some of the test results are provided in a GE topical report (Reference I).

Figure 1

shows the configuration of a typical cross

quencher, which is currently used by all Nark III contai nments.

The cross quencher

.has four arms with each arm perforated by several rows of small holes.'he tip of each arm is plugged and the device measures approximately 10 feet long from tip to tip.

Steam flows through

" the hub,'s distributed among the four arms, and is discharged

'nt'o'he pool.

The T-quencher device presently bei ng developed for'he Mark I plants is similar to the cross quencher except that it has only two arms that are approximately 20 feet long from tip to tip. The quencher device produces a cloud of air or steam mist, whereas the ramshead produces large bubbles.

Because of the quencher configuration, the magnitude of the quencher air clearing, load is, reduced by.a factor of.two to four..

In addition,. steam condensati-on -instability. does not occur although the pool temperature approaches boiling point.

Figure 3 shows the comparison of structural loading functions for quencher and ramshead devices for a 238 GESSAR Mark III plant.

Although these loading functions. are not applicable for the Nark I design, they demonstrate ~that.the quencher device, in general, substantially, reduces the loads on the containment structure with the, magnitude of the load reduction being dependent on the quencher configuration and its relative location to the adjacent stuctures.

Foreign large-scale testing and in-plant tests from the United States (Monticello), haye verified the reductionin hydrodynamic

.loads when using the quencher-type discharge device.

Additional testing on a small scale has also shown the temperature thresliold for unstable condensation to increase to about 200 F using the quencher-type, device.

GE is presently conducting full-'.scale, confir'matory testing of the cross-type quencher device at the Caroso plant in Italy.

Additional,testing on a full-scale pl,ant has been performed in Japan at the Tokai 2 facility.

IV.

Conclusion The suppression pool temperature limit proposed by GE to preclude,.',.

unstable condensation during SRV. discharge through a ramshead device has not been adequately demonstrated.

Furthermore, we believe that, even if sufficient full-scale testing of the ramshead device.were to be performed.to adequately define the suppression pool temperature limit, it is likely that the resulting limit would re'quire several operator actions and perhaps an"additional margin in the allowable pool temperature during normal plant operation to preclude unstable condensation.

I The test data that has been generated to date for the quencher devices have not exhibited the.unstable condensation observed in the ramshead tests at elevated pool temperatures.

These data also demonsrate that the quencher air clearing loads on the containment are substantially lower than the loads resulting from discharge through a ramshead device.

Furthermore, based on the limited number of suppression pool temperature

transient anal'yses that we have received for Mark I plants, it.

appears that a lesser amount of operator action would be required.

Based on the improved performance demonstrated. for the quencher discharge devices and the uncertainty associated with the defini-tion of the pool temperature limits for ramshead discharge

devices, we conclude that the use of ramshead devices in BWR water suppression containment systems is not acceptable for long-term operation.

We also conclude that the quencher-type devices provide a satisfactory resolution to the condensation stability concerns and is, therefore, an acceptable replacement.

References 1.

General Electric Company, "Test Results Employed by GE for BWR Containment and Vertical.Vent Loads,"

GE Topical Report NEDE-21078-P, October 1975.

2.

General Electric Company Memorandum Report, "17(PF Pool Temperature Limit for SRV Ramshead Condensation Stability,"

September 1977.

3.

Ain A. Sonin and C. Tung, "Comments on the Pool Temperature Limit for Avoiding Pulsating Condensation with Ramshead SRVs,"

Brookhaven National Laboratory, February 1978.

4.

General Electric Company, "Information Report Mark III Contai n-ment Dynamic Loading Conditions (Final),"

GE Topical Report NED0-11314-08, July 1975.

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RAMSHEAD CROSS-QUENCHER

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T-QUENCHER

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Figure 1

TYPICAL SRV DISCHARGE DEVICES

GE's Recommended Limit 160'F I-I ENO (C)

DEMONSTRATED ENO (A)

START (C)

PLANT C

START (A)

PLANT A

100 S~ OSS FLuX, (LPVFT2-SEO Figure 2

PLANT OPERATIONAL EXPERIENCE

Source:

Reference 4

RAMSHEAD QUENCHER QUENCHER RAMSHEAD 2

3 4

5 6

1 8

9 IO 1I t2 13 DRYWELLWALL BASE MAT CONTAINMENT Figure 3

MARK III STANDARD PLANT SRV MALL PRESSURES

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