ML19250A823
| ML19250A823 | |
| Person / Time | |
|---|---|
| Site: | Big Rock Point File:Consumers Energy icon.png |
| Issue date: | 10/09/1979 |
| From: | Office of Nuclear Reactor Regulation |
| To: | |
| Shared Package | |
| ML19250A822 | List: |
| References | |
| RTR-REGGD-01.056, RTR-REGGD-1.056, TASK-05-12.A, TASK-5-12.A, TASK-RR NUDOCS 7910240657 | |
| Download: ML19250A823 (11) | |
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Enclosure BIG ROCK POINT TOPIC V-12.A WATER PURITY OF BOILINT WATER REACTOR PRIMARY COOLANT TopicV-12.AwasincludedintheSystematicEhaluationPrograminorderthat BWR compliance with Regulatory Guide 1.56 be determined. As part of this review,theguidance.'ifRegulatoryGuide1.56,Rehision1,wascompared against the facility design. This Regulatory Guide had been specifically identified by the NRC's Regulatory Requirements Rehiew Comittee as needing consideration for backfit on operating reactors. The review documents whether the facility design complies with the guidance of the Regulatory Guideorhassomeequihalentalternativeacceptabletothestaff. The acceptabilityornon-acceptabilityofthedehiationslistedbelowandthe need for further action shall be judged during the integrated assessment for this facility.
Although the topic definition mentions that there are proposed revisions to Regulatory Guide 1.56, and although NUREG-0531 (" Investigation and Evaluation of Stress Corrosion Cracking in Piping in Light Water Reacter Plants,"
February 1979) recommends oxygen control in BWRs, we have determined that Regulatory Guide 1.56, Rehision 1. July 1978, in its "For Coment" fom, is the latest approved staff guidance and have therefore based our rehiew upon s
this guidance. The specific points of the regulatory positica are quoted below and an explanation of the licensee's degree of conformance fbliows.
Informationforthisrehieww'asobtainedfromthelicensee'sTechnicalSpecifi-cations, applicable plant drawings, the licensee's response to a March 16, 1379 telephone conversation with his staff, and telephone conversations with his staff on May 8, 1979.
7910240d8f October 9,1979 120/
070
e.
. I.
Regulatory Position 1 The liceosee should establish appropriate limits for the electrical conductivity of purified condensate to the reactor vessel (the electrical conductivity of the BWR feedwater cycle and that of the reactor water cleanup cycle). Separate limits may be required for such operating conditions as startup, hot standby, low
- power, high power, and at temperatures <2120F (1000C).
Chemical analyses for dissolved and suspended impurities should be performed as called for in the plant technical specifications. A conductivity meter should be provided at each condenser hotwell or in the.line between the hotwell and the condensate demineralizer with. sufficient range to measure at least all levels of conductivity up to and including the limiting conditions of the technical specifications that require imediate shutdown of the reactor. The recording conductivity meters recomended in regulatory position 4.a may be used for this purpose.
Big Rock Point Technical Specification 4.1.2(b) establishes the following limits on primary coolant purity:
Maximum conductivity 5.0 umho/cm Maximum transient conductivity
- 10.0 umho/cm pH 4.0 - 10.0 Chloride 1.0 ppm EquilibriumHalogenRadioactihity 35.0 u Ci/ml Baron 100.0 ppm In addition, the specification requires a daily sample.of the primary coolant to determine that no limit is being exceeded. Plant procedures also require a daily turbidity test of the coolant as a means of detecting imourities.
This applies only to the period subsequent to a cold shutdown, between criticality and 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> after reaching 20% rated power.
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1 It is important to note specific statements in Technical Specification 4.1.2(b): "The following [ limits stated above] are absolute limits which if exceeded shall necessitate reactor shutdown. Correctiheactionshall necessarily be taken at more stringent limits to minimize the possibility oftheseabsolutelimitseherbeingreached."
With this philosophy in mind, the licensee has established conductihity alam setpoints for the condensate demineralizer effluent and reactor water cleanup demineralizer effluent at 1.0 umho/cm, substantially below the allowable limit of the specification. Further discussion of alams, monit'oring instruments, and the specific requirements of the Technical
' Specifications will be brought out in Sections 4, 5 and 6 which follow.
The present specifications and plant procedure requieements meet the intent of regulatory position 1.
II. Regulatory Position 2 The licensee should establish the sequential resin regeneration frequency or resin replacement frequency required to maintain adequate capacity margin in the condensate treatment system for postulated condenser cooling water inleakage. The capacity required and corresponding resin regeneration or replacement frequency will depend on several parameters, including condenser cooling water composition, chloride concentration, flow rate in each demineralizer unit, type and quantity of resin, cation / anion resin ratio, postulated condenser leakage, and time for orderly reactor shutdown.
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e.
Big Rock Point does not regenerate resins, choosing instead to replace.
the resin when certain criteria for replacement are met. The reason for replacement, vice regeneration, is that Big Rock Point is cooled by,
LakeMichigan,a'freshwatersourcecontainingonlylbppmchloride withconductihitylehelsof 200-240 umho/cm. Such a relatively pure water is not expected to cause resin exhaustion for a long period of time, thus making regeneration, with its attendent large amounts of acid, base, and fresh water, an unnecessary expense in equipment, time, and expendables.
Instead, Big Rock Point has established resin replacement criteria as follows:
(1) Numberofdaysinserhiceonaresinbedandnumberandextentof condenserleaks(ifany)duringthatperiodofserhice.
(2) Expected future operation of the plant - this may result in replacementinadhanceofthatrequiredbytheothercriteriaand allows scheduling of the resin bed replat.ement when it is least likelytointerferewithotherplannedactihities.
(3) Differential pressure across each bed - retention of crud (corrosion products) on the resin beds will cause an increase in differential pressureandnecessitateresinreplacementinadhanceofthatdictated by resin exhaustion alone.
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.5.
(4) Resinbedeffluentconductihity Although the plant has sufficient instrumentation to alert the operators to a tube leak, and although plant experience has shown resin replacements nomally occur because of (1),' (2) or (3) b above (or a combination thereof) instead of (4), we are concerned that a condenser leak with failure or miscalibration of the extractionconductihityinstrumentationcouldresultinexhaustion of all resin beds at once and therefore no spare capacity with which to conduct an orderly reactor shutdown. The reason for this is that the three condensate demineralizer resin beds, although rated at 1/2-capacity each, are typically all inserhice at power levels greater than 50 MWe, thus challenging all three units at
'once. Becauseoftherelatihepurityofthecoolingwater,we can accept alternatthes to the regulatory position such as the inclusion of weekly condenser effluent sampling with bed DF determination and use as a criterion, or the maintenance of one demineralizer unit in " charged" standby to allow orderly shutdown, ffo action is necessary, on the licensee's part, at this time, since any recom.endations for physical or procedural changes will be rehiewedatthecompletionofthestaff'sintegratedassessment.
ThereplacementofresinintheRWCUsystemdemineralizerisgeherned bythesamefourcritertastatedabohe. However, in this case the maintenance of capacity is more important, in that any contaminants from condensate demineralizer breakthrough will tend to concentrate 12n7 074
?00R ORl8!NAL in the reactor, with RWCU the only means of removal other than an arduous" bleed and feed" reduction technique. Because there is only one RWCU demineralizer, special care must be taken to assure no breakthrough-in the condensate system, especially with no spare capacity in the condensate and RWCU demineralizers. Therefore the reconsnendations above(or other acceptable alternatihes) carry additional impact.
III. Regulatory Position 3 The initial total capacity of the new anion and cation demineralizer resins should be auiasured. Anion exchange capacity may be detemined by a procedure recomended by the resin manufacturer.
The total exchange capacity of the cation resin may be measured by a procedure recomended by the resin manufacturer or by paragraphs 41 through 49 of ASTM 02187-71, " Standard Methods of Test of Physical and Chemical Properties of Ion-Exchange Resins."
For resins.that are to be regenerated, these determinations should be repeated at least samiannually. The resins should be discarded and replaced when their capacity.following regeneration falls below 60 percent of the initial value. More frequent deteminations should be made at plants using seawater or other water containing large amounts of dissolved or suspended matter as coolant in their heat exchangers. For resins that are not regenerated but are instead replaced periodically with material of the same type, measurements of initial capacity should be made on a sample of new material at least once a year (when the time between replacements is less than 1 year) or at each replacement (when the time between replacements exceeds 1 year). When the type of anion or cation resin is changed, a measurement of total capacity of the replace-ment resin should be made prior to use in the demineralizer.
The detemination of initial capacity is not perfomed at Big Rock Point, but is instead specified in the purchase specifications for new resins to be used in the condensate and RWCU demineralizers. Capacity is to be determined in accordance with MIL R-22258 or an equihalent method. We find this to be acceptable, in that we agree with the licensee that the specific measurements 1207 075
.7.
of the Regulatory Guide si, not necessary because of the cooling water purity. However, this conclusion depends upon the changes to be made in accordance with Position 2 above.
IV.' Regulatory Position 4 4.
The licensee should verify the minimum residual demineralizer capacity in the most depleted domineralizer unit established in accordance with the recommendations of regulatory position 2 is maintained.
The following is an example of an acceptable method for detemining the condition of the demineralizer units so that the ion exchange resin can be replaced or regener.ted before an unacceptable level of depletion is reached.
Recording conductivity meters should be installed at the inlet and a.
outlet of both the condensate treatment systemand reactor water cleanup system. The range of these instruments should be sufficient to measure all levels of potential water conductivity specified in the piant technical specifications. For the condensate treatment system, the conductivity meter readings should be calibrated so that estimates of condenser leakage can be made based on cooling water conductivity condensate conductivity, and flow rate. The chemical composition of the cooling water and its relation to specific conductance should be established ar. ' periodically confimed so that estimates of residual demineralizer cyacity can be made, b.
A recording flowmeter should be used to. measure the rate of flow through each demineralizer, The quantity of the principal fon(s) likely to cause demineralizer c.
breakthrough should be calculated by:
(1) Converting the conductivity readings of the water entering the demineralizer to weight fraction (e.g., ppm or ppb) of the principa.1 ion (s) and (2) Integrating over time the product of concentration of this fon(s) and demineralizer flow.
The input quantity of fon(s) to the demineralizers should be determined at a frequency adequate to ensure sufficient residual ion exchange capacity in the event of a major condenser leakage to prevent exceeding reactor coolant limits.
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. d.
Each demineralizer unit should be replaced or regenerated wh<.n the remaining capacity (calculated by subtracting the total utilization determined from conductivity and flow measurements in accordance with regulatory position 4.c from the initial capacity determined in accordance with regulatory position 3) approaches the minimum residua _1 demineralizer capacity determined in accodance with regulatory position 2.
The accuracy of the, above calcDation should be checked by measuremer.:s made on resin samples taken when demineralizer units are removed from servic: for regeneration or resin cleaning. Measurements on sample:
from each unit should be cade at each of the first two such removals from service and at every fifth such removal from service thereafter.
If appropriate, the actual measurements may be used to adjust the calculated value of residual demineralizer capacity. Such adjustment and its justification should be reported to the NRC in the annual operating report.
Once again, the licensee does not believe that such determination is necessary, given the unique characteristics of the Big Rock Point plant and its Lake Michigan coolant. We agree with this assessment (with the exception noted in Position 2) and note that the following instruments, as determined from the Big Rock Point drawings and discussions with licensee personnel, are provided to assure early operator notification of potential problems:
A.
Conductivity instruments:
(1) Feedwater system -
two conductivity elements (range 0-1 umho/ca), recorder and alarm (control room at 1.0 umho/cm)on the discharge of the main condenser prior to the condensate demineralizers.
ene conductivity element (range 0-10 umho/cn), recorder and alarm (local at 1.0 umho/cn) on the discharge of each of the three condensate demineralizers.
(2) Reactor Water Cleanup System -
one conductivity element (range 0-1 umho/cn) and alarm (control room at 1.0 umho/ca) on the discharge of the RWCU demineralizer.
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7
-g-(3) Steam drum (instead of RWCU inlet) -
one conductivity element (range 0-10 umho/cm), recorder, and alarm (control room at 2.0 umho/cm) 8.
Flow measuring' instruments:
(1) Feedwater system -
one flow element, transmitter, local recorder, and alam on each of the three condensate demineralizers.
(2) Reactor Water Cleanup system -
one flow element, transmitter, and local recorder on the inlet to the RWCU demineralizer Although the instrumentation: satisfies the general requirements, we are concerned that the local alams of the condensate oemineralizers could signal a warning for as long as two hours before being noticed. This also gives added weight to the recomendations of Position 2 above.
V.
Regulatory Position 5 The conductivity meter (s) located at tne inlet and oul;let of the demineralizer(s) of the condensate treatment system and the reactor water cleanup system should be set to trigger alarms in the control room when, as a minimum, either of the following conductivity levels is reached (values of which should be determined by the licensee):
a.
The level that indicates marginal perfomance of the demineralizer systems.
b.
The level that indicates noticeable breakthrough of one or more demineralizers.
The alams are listed above in Section 5 and satisfy the recocrnendations of the Regulatory Guide.
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1-
. VI. Regulatory Position The chloride content in the reactor vessel water should.be maintained as low as practical. The ionic equilibria of the reactor vessel water should be controlled to ensure a neutral pH. The licensee.should establish limits for condctivity, pH, and chlorides in the reactor vessel water and should specify procedures to be used for their detemination. Acceptable reactor water chemistry limits are given in Table 1 of the appendix to this guide.
If the limiting values of the conductivity, pH, or chloride content are exceeded, appropriate corrective actions as defined in the plant technical specifications should be taken.
Given that the lake water contains only approximately 10 ppn chloride, chances for a gross and undetected chloride intrusion are small. However, there are areas of disagreement between the guidance limits and the licensee's limits.
A comparison follows:
Parameter R.G. 1.56 limit Big Rock Point limit (a)
Conductivity I umho/cm at steaming rates 5 umho/cm during power operation, greater than 1% of rated with a 10 umho/cm maximum steam flow (maximum limit transient value allowed only established at 10 umho/cm, during the period subsequent to which would require orderly a cold shutdown, between shutdown, but 72 hours8.333333e-4 days <br />0.02 hours <br />1.190476e-4 weeks <br />2.7396e-5 months <br /> criticality and 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> after above 1 umho/cm and.2 ppm reaching 20% rated power. Alarms chloride allowed per and required action are set incident not to exceed much lower.
2 weeks per year)
(b)
.2 ppm at steaming rates 1.0 ppm during power operation greater than 1% of rated steam flow (maximum established at 0.5 ppm, which would require orderly shutdown, but 72 hours8.333333e-4 days <br />0.02 hours <br />1.190476e-4 weeks <br />2.7396e-5 months <br /> above
.2 ppm and 1 umho/cm allowed per incident, not to exceed 2 weeks per year) 1?n7 079
(c) pH limits between 5.3 and limits between 4.0 and 10.0 8.6 (d) Conductivity
.5 umho/cm at the inlet I umho/cm (alarm) of the Feed-to the demineralizers water System (mazimum of 10, requiring orderly shutdown)
.2 umho/cm at the indivi-1 unho/cm (alarm) dual demineralizer outlet It is our belief that BWR pipe cracking has been proven to be such an extensive problem that the limits of Regulatory Guide 1.56 should be conformed to where the licensee does not already have equivalent or lower limits.
Conclusion With the modification of technical. specifications as discussed in Position 6 and the recocmendations of Position 2, the licensee will conform to the intent of the regulatory guide. However, since the need for modification to the plant (including technicri specifications and procedural modifications) will be judged only during the integrated assessment, the licensee need take no action at this time.
s
=
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