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(2) Design pressure -that value corresponding to AS1LE code values which are obtained at or below code allowable material design stress values.1. 97-21 Range Tvaho pi 1on ,
(2) Design pressure -that value corresponding to AS1LE code values which are obtained at or below code allowable material design stress values.1. 97-21 Range Tvaho pi 1on ,
TABLE 3 -BWR VARIABLES Measured Variable CORE: Control Rod Position Neutron Flux REACTOR COOLANT SYSTEM: RCS Pressure Coolant Level in the Reactor Main Steamline Flow Main Steamline Isola-tion Valves' Leakage Control System Press-ure Primary System Safety Relief Valve Posi-tions including ADS or Flow Through or Pressure in Valve Lines Radiation Level in Coolant Range I -. i Full in in or not full 1 c/s to 1% power (at least one fission counter)15 psia to 2000 psig Bottom of core support plate to above top of discharge plenum 0 to 120% design flow 1 0 to 15" of water 0 to 5 psid Closed-not closed or 0 to 30 psig 10 pCi/g D B B,C B B B B,D to 10 Ci/g C Provide positive indication that the control rods are fully inserted.(Minimum of 2 hours after accident)ANS-4.5, Section 6.2.2 For indication of approach to criticality ANS-4.5, Sections 6.2.3, 6.2.4, 6.3.3 and 6.3.5 For indication of an accident and to in-dicate that actions must be taken to mitigate an event.ANS-4.5, Section 6.2.3 For indication of fuel submergency for a LOCA event.To provide an indication of the integrity of the pressure boundary.To provide an indication of the pressure boundary and containment integrity.
TABLE 3 -BWR VARIABLES Measured Variable CORE: Control Rod Position Neutron Flux REACTOR COOLANT SYSTEM: RCS Pressure Coolant Level in the Reactor Main Steamline Flow Main Steamline Isola-tion Valves' Leakage Control System Press-ure Primary System Safety Relief Valve Posi-tions including ADS or Flow Through or Pressure in Valve Lines Radiation Level in Coolant Range I -. i Full in in or not full 1 c/s to 1% power (at least one fission counter)15 psia to 2000 psig Bottom of core support plate to above top of discharge plenum 0 to 120% design flow 1 0 to 15" of water 0 to 5 psid Closed-not closed or 0 to 30 psig 10 pCi/g D B B,C B B B B,D to 10 Ci/g C Provide positive indication that the control rods are fully inserted.(Minimum of 2 hours after accident)ANS-4.5, Section 6.2.2 For indication of approach to criticality ANS-4.5, Sections 6.2.3, 6.2.4, 6.3.3 and 6.3.5 For indication of an accident and to in-dicate that actions must be taken to mitigate an event.ANS-4.5, Section 6.2.3 For indication of fuel submergency for a LOCA event.To provide an indication of the integrity of the pressure boundary.To provide an indication of the pressure boundary and containment integrity.
By these measurements the operator knows if there is a path open for loss of cool-ant and that an event may be in progress.ANS-4.5, Section 6.3.2 For early indication of fuel cladding failure and estimate of extent of damage.1.97-22 0.Ty pe Puirnnos  
By these measurements the operator knows if there is a path open for loss of cool-ant and that an event may be in progress.ANS-4.5, Section 6.3.2 For early indication of fuel cladding failure and estimate of extent of damage.1.97-22 0.Ty pe Puirnnos
: TABLE 3 -BWR VARIABLES continued  
: TABLE 3 -BWR VARIABLES continued  
-Measured Variable CONTAINMENT:
-Measured Variable CONTAINMENT:
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Vertical Temperature Difference Precipitation Range 0 I__ _ _ _ _ __ -I -I WI U CZ I-9*F to +9 0 F (tO.307 accuracy per 164 foot intervals Recording rain gage with range sufficient to assure accuracy of total accumulation within 1O% of record-ed value -0.01" resolution E For determining effluent diffusion rates for emergency planning, dose assessment C and source estimates.
Vertical Temperature Difference Precipitation Range 0 I__ _ _ _ _ __ -I -I WI U CZ I-9*F to +9 0 F (tO.307 accuracy per 164 foot intervals Recording rain gage with range sufficient to assure accuracy of total accumulation within 1O% of record-ed value -0.01" resolution E For determining effluent diffusion rates for emergency planning, dose assessment C and source estimates.
For determining effluent transport and ground deposition for emergency planning Notes for Table 3 -(1) Design flow -the maximum flow anticipated in normal operation.(z) Design pressure -that value corresponding to ASM code values which are obtained at or below code allowable material design scress values.1. 97-28 IT/Os of1'M en ft 0 0 ANS-4. 5 Draft 3 September, DRAFT CAUTION NOTICE: This Standard is being prepared or reviewed and has not been approved by ANS. It is subject to revision or withdrawal before issue.DRAFT American National Standard FUNCTIONAL REQUIRE1ENTS FOR POST ACCIDENT MONITORING CAPABILITY FOR THE CONTROL ROOM OPERATOR OF A NUCLEAR POWER GENERATING STATION Assigned Correspondent
For determining effluent transport and ground deposition for emergency planning Notes for Table 3 -(1) Design flow -the maximum flow anticipated in normal operation.(z) Design pressure -that value corresponding to ASM code values which are obtained at or below code allowable material design scress values.1. 97-28 IT/Os of1'M en ft 0 0 ANS-4. 5 Draft 3 September, DRAFT CAUTION NOTICE: This Standard is being prepared or reviewed and has not been approved by ANS. It is subject to revision or withdrawal before issue.DRAFT American National Standard FUNCTIONAL REQUIRE1ENTS FOR POST ACCIDENT MONITORING CAPABILITY FOR THE CONTROL ROOM OPERATOR OF A NUCLEAR POWER GENERATING STATION Assigned Correspondent
-T. F. Timmons Westinghouse Electric Corporation Power Systems Company P.O. Box 355, MNC-410 Pittsburgh, PA 15230 1979 09 Writing Group ANS 4.5 Standards Committee NUPPSCO Secretariat ANS 0 0 TABLE OF CONTENTS FOREWORD 1.0 Introduction
-T. F. Timmons Westinghouse Electric Corporation Power Systems Company P.O. Box 355, MNC-410 Pittsburgh, PA 15230 1979 09 Writing Group ANS 4.5 Standards Committee NUPPSCO Secretariat ANS 0 0 TABLE OF CONTENTS FOREWORD 1.0 Introduction 2.0 Scope 3.0 Definition 4.0 Discussion 5.0 Design Basis 6.0 Design Criteria -Phase I and Phase II FOREWORD ANS 4 established Working Group 4.5 in late July 1979 to prepare a draft standard on Accident Monitoring Instrumentation which would complement other standards, but be broader in nature by including economic consid-erations.
 
===2.0 Scope===
3.0 Definition
 
==4.0 Discussion==
 
===5.0 Design===
Basis 6.0 Design Criteria -Phase I and Phase II FOREWORD ANS 4 established Working Group 4.5 in late July 1979 to prepare a draft standard on Accident Monitoring Instrumentation which would complement other standards, but be broader in nature by including economic consid-erations.
Two primary objectives were 1) to address that instrumenta-tion which permits the operator to monitor expected parameter changes in the accident period, and 2) to address extended range instrumentation deemed appropriate for the possibility of encountering previously unforeseen events.ANS 4.5 began work on July 30th and met for 13 working days in a seven week period. In addition, a Design Criteria subgroup met for two days in this same period.As presented, this draft standard provides: 1. a list of functions to be performed (design basis section 5.0)2. a framework to determine those variables to be monitored (design basis section 5.0)3. an identification of three time periods of interest (definitions 3.0)4. an identification of four variable types (definitions 3.0)5. a delineation of applicable design criteria for the variables to be monitored (design criteria section 6.0)No identification of specific Type A monitored variables is provided in this standard.
Two primary objectives were 1) to address that instrumenta-tion which permits the operator to monitor expected parameter changes in the accident period, and 2) to address extended range instrumentation deemed appropriate for the possibility of encountering previously unforeseen events.ANS 4.5 began work on July 30th and met for 13 working days in a seven week period. In addition, a Design Criteria subgroup met for two days in this same period.As presented, this draft standard provides: 1. a list of functions to be performed (design basis section 5.0)2. a framework to determine those variables to be monitored (design basis section 5.0)3. an identification of three time periods of interest (definitions 3.0)4. an identification of four variable types (definitions 3.0)5. a delineation of applicable design criteria for the variables to be monitored (design criteria section 6.0)No identification of specific Type A monitored variables is provided in this standard.
Recommendations for Type 3 and Type C monitored vari-ables are provided in Section 6.0.i The significant issues in the development of this standard have been: 1. the scope of the document in terms of applicability to the control room operator or the plant operator (licensee).
Recommendations for Type 3 and Type C monitored vari-ables are provided in Section 6.0.i The significant issues in the development of this standard have been: 1. the scope of the document in terms of applicability to the control room operator or the plant operator (licensee).
The work group chose a control room operator scope.2. the pre-planned operator actions designated by the accident analyses in Chapter 15 of a plant's FSAR and the not previously planned operator action that may be required during unforeseen events. The Working Group established Type A instrumentation for the former, and Type B or C instrumentation for the latter.3. The monitoring of actual fission product barrier integrity and the potential for breach of a given barrier. The work group chose monitoring of actual breach for the fuel, reactor coolant system, and containment barrier, but only the potential breach of the con-tainment barrier.4. the degree of alignment of accident monitoring instrumentation with IEEE Class .E (ANS Class EC-3) and whether an intermediate class is needed between 1E and non-1E.5. whether a list of variables should be included as an appendix to the standard: a. a list of only Type C parameters
The work group chose a control room operator scope.2. the pre-planned operator actions designated by the accident analyses in Chapter 15 of a plant's FSAR and the not previously planned operator action that may be required during unforeseen events. The Working Group established Type A instrumentation for the former, and Type B or C instrumentation for the latter.3. The monitoring of actual fission product barrier integrity and the potential for breach of a given barrier. The work group chose monitoring of actual breach for the fuel, reactor coolant system, and containment barrier, but only the potential breach of the con-tainment barrier.4. the degree of alignment of accident monitoring instrumentation with IEEE Class .E (ANS Class EC-3) and whether an intermediate class is needed between 1E and non-1E.5. whether a list of variables should be included as an appendix to the standard: a. a list of only Type C parameters
: b. a list of Type A, 3, C and 0 parameters
: b. a list of Type A, 3, C and 0 parameters
: 6. the definition of instrument types 3 and 0 and whether these types should be included in the standard.The membership of the Working Group is as follows: L. Stanley, Chairman T. Timmons, Vice Chairman and Correspondent ii  
: 6. the definition of instrument types 3 and 0 and whether these types should be included in the standard.The membership of the Working Group is as follows: L. Stanley, Chairman T. Timmons, Vice Chairman and Correspondent ii
: 0. Scmmers E. Wenzinger 0. Lambert R. Bauerle J. Castanes M. Wolpert H. Mumford X. Polanski E. Oowling Additional input has been provided to the Working Group by industry, university, and government participants throughout the meetings.
: 0. Scmmers E. Wenzinger 0. Lambert R. Bauerle J. Castanes M. Wolpert H. Mumford X. Polanski E. Oowling Additional input has been provided to the Working Group by industry, university, and government participants throughout the meetings.
The Work Group is very appreciative of this assistance.
The Work Group is very appreciative of this assistance.
A iii  
A iii 1.0 introduction The Code of Federal Regulations requires that instrumentation be provided to monitor variables and systems over their anticipated ranges for acci-dent conditions as appropriate to assure adequate safety. The purpose of this standard is to establish criteria for the selection of that instru-mentation.
 
==1.0 introduction==
The Code of Federal Regulations requires that instrumentation be provided to monitor variables and systems over their anticipated ranges for acci-dent conditions as appropriate to assure adequate safety. The purpose of this standard is to establish criteria for the selection of that instru-mentation.
These criteria are based on the sequence and duration of the phases through which an accident progresses.
These criteria are based on the sequence and duration of the phases through which an accident progresses.
The control room operator may have different information requirements for each phase of an accident.This standard presents criteria for monitoring the response of the plant to design basis events. It also presents criteria for monitoring the integrity of fission product barriers under conditions which have degraded beyond the design bases. This fission product barrier monitoring is con-sidered to be an extra set of instrumentation beyond that required for satisfactorily monitoring accident scenarios postulated in the plant safety analysis.Throughout these criteria, three verbs have been used to indicate the degree of rigor intended by the specific criterion.
The control room operator may have different information requirements for each phase of an accident.This standard presents criteria for monitoring the response of the plant to design basis events. It also presents criteria for monitoring the integrity of fission product barriers under conditions which have degraded beyond the design bases. This fission product barrier monitoring is con-sidered to be an extra set of instrumentation beyond that required for satisfactorily monitoring accident scenarios postulated in the plant safety analysis.Throughout these criteria, three verbs have been used to indicate the degree of rigor intended by the specific criterion.
The word "shall" is used to denote a requirement; the word "should" to denote a recommenda-tion; and the word "may" to denote permission, neither a requirement nor a recommendation.
The word "shall" is used to denote a requirement; the word "should" to denote a recommenda-tion; and the word "may" to denote permission, neither a requirement nor a recommendation.
1  
1 2.0 SCOPE This standard contains criteria for determining the variables to be moni-tored by the control room operator, as required for safety, during the course of an accident and during the long-term stable shutdown phase fol-lowing the accident.
 
===2.0 SCOPE===
This standard contains criteria for determining the variables to be moni-tored by the control room operator, as required for safety, during the course of an accident and during the long-term stable shutdown phase fol-lowing the accident.
Also included are criteria for determining the requirements for the equipment used to monitor those variables.
Also included are criteria for determining the requirements for the equipment used to monitor those variables.
The scope of the standard is limited to onsite environment and process monitoring.
The scope of the standard is limited to onsite environment and process monitoring.
Emergency preparedness planning is, or 'will be, covered by other standards.
Emergency preparedness planning is, or 'will be, covered by other standards.
2  
2 3.0 OEFINITIONS Phase I That portion of the accident extending from the initiation of the accident to that point at which the plant is in a con-trolled condition.
 
==3.0 OEFINITIONS==
Phase I That portion of the accident extending from the initiation of the accident to that point at which the plant is in a con-trolled condition.
Phase II That portion of the accident extending from the time at which the plant is in a controlled condition to that point at which personnel access to the location of the accident is possible.Phase III That portion of the accident extending from the time at which personnel access to the location of the accident is possible to the time at which the plant has returned to operating status or been decommissioned.
Phase II That portion of the accident extending from the time at which the plant is in a controlled condition to that point at which personnel access to the location of the accident is possible.Phase III That portion of the accident extending from the time at which personnel access to the location of the accident is possible to the time at which the plant has returned to operating status or been decommissioned.
Type A Instruments  
Type A Instruments  
-Those instruments which provide the information required to permit the control room operator to take the pre-planned manual actions to accomplish safe plant shutdown for design basis accident events and to maintain long term plant-stability.
-Those instruments which provide the information required to permit the control room operator to take the pre-planned manual actions to accomplish safe plant shutdown for design basis accident events and to maintain long term plant-stability.
Type B Those instruments which provide to the control room operator information to monitor the process of accomplishing critical safety functions, i.e., reactivity control, core cooling, maintaining reactor coolant system integrity, maintaining containment integrity and radioactive effluent control.Type C Those instruments that indicate in the control room (1) the extent to which parameters, which have the potential for causing a breach of the final fission product barrier (i.e., the containment), have exceeded the design basis values, or (2) that a fission product barrier (i.e., fuel clad, reactor coolant pressure boundary or the containment) has been breached.3 Type 0 Those instruments which indicate to the control room operator the performance of individual safety systems.Design Basis Accident Events Those events postulated in the plant safety analyses, any one of which may occur during the lifetime of a particular plant, excluding those events which are expected to occur during a calendar year for a particular plant;and those events that are not expected to occur but are postulated in the plant safety analyses because their consequences would include the poten-tial for the release of significant amounts of radioactive material.4  
Type B Those instruments which provide to the control room operator information to monitor the process of accomplishing critical safety functions, i.e., reactivity control, core cooling, maintaining reactor coolant system integrity, maintaining containment integrity and radioactive effluent control.Type C Those instruments that indicate in the control room (1) the extent to which parameters, which have the potential for causing a breach of the final fission product barrier (i.e., the containment), have exceeded the design basis values, or (2) that a fission product barrier (i.e., fuel clad, reactor coolant pressure boundary or the containment) has been breached.3 Type 0 Those instruments which indicate to the control room operator the performance of individual safety systems.Design Basis Accident Events Those events postulated in the plant safety analyses, any one of which may occur during the lifetime of a particular plant, excluding those events which are expected to occur during a calendar year for a particular plant;and those events that are not expected to occur but are postulated in the plant safety analyses because their consequences would include the poten-tial for the release of significant amounts of radioactive material.4 4.0 DISCUSSION It is the philosophy of this Standard that instrumentation is required to monitor plant performance during and after an accident.
 
==4.0 DISCUSSION==
It is the philosophy of this Standard that instrumentation is required to monitor plant performance during and after an accident.
The purposes of the accident monitoring instrumentation are enumerated in Section 5.0, Design Basis. This Standard specifies the plant safety functions to be performed and the criteria to be used by the designer in selecting the variables to be monitored.
The purposes of the accident monitoring instrumentation are enumerated in Section 5.0, Design Basis. This Standard specifies the plant safety functions to be performed and the criteria to be used by the designer in selecting the variables to be monitored.
Certain concepts have been established to aid the system designer in the selection of variables to monitor the course of an accident and to arrive at appropriate design criteria for instruments to monitor these variables.
Certain concepts have been established to aid the system designer in the selection of variables to monitor the course of an accident and to arrive at appropriate design criteria for instruments to monitor these variables.
 
4.1 Planned Versus Unolanned Operator Actions The plant safety analysis defines the accident scenarios from which the safety system design bases and the planned or anticipated operator actions are derived. Accident monitoring instrumentation is provided to permit the operator to take required actions to address these analyzed.situations.
===4.1 Planned===
Versus Unolanned Operator Actions The plant safety analysis defines the accident scenarios from which the safety system design bases and the planned or anticipated operator actions are derived. Accident monitoring instrumentation is provided to permit the operator to take required actions to address these analyzed.situations.
However, instrumentation must also be provided for unplanned situations, (i.e., to ensure that, should plant conditions evolve differently than predicted by the safety analysis, the operator has sufficient information to monitor the course of the event). Instru-mentation must also be provided to indicate to the operator if fission product barrier integrity has degraded beyond the prescribed limits of the Safety Analysis.4.2 Variable Types Four classifications of variables have been identified.
However, instrumentation must also be provided for unplanned situations, (i.e., to ensure that, should plant conditions evolve differently than predicted by the safety analysis, the operator has sufficient information to monitor the course of the event). Instru-mentation must also be provided to indicate to the operator if fission product barrier integrity has degraded beyond the prescribed limits of the Safety Analysis.4.2 Variable Types Four classifications of variables have been identified.
Operator manual actions during accidents included in the plant safety analysis are anticipated or pre-planned.
Operator manual actions during accidents included in the plant safety analysis are anticipated or pre-planned.
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Guidance on the selection of Type 0 vari-ables and the specification of appropriate design criteria are not given in this standard.
Guidance on the selection of Type 0 vari-ables and the specification of appropriate design criteria are not given in this standard.
This guidance is provided in standards for design of safety systems (e.g. IEEE-603, ANSI N1S.2, etc). The four classifica-tions are not mutually exclusive in that a given variable (or instrument) may be included in one or more types. This differentiation by variable type is intended only to guide the designer in his selection of accident monitoring variables and applicable criteria.4.3 Accident Phases The typical accident sequence has been subdivided into three phases: Phase I covers the initial portion of the accident, Phase II covers the stable long-term cooling portion of the accident up to the time where personnel access is possible, and Phase III addresses the period follow-ing personnel access to the accident area. This sub-division has been made so that variable selection and design criteria application can reflect the differing conditions which characterize these three phases.For example, Phase I can be anticipated to be of relatively short dura-tion, having relatively severe plant conditions, and allowing no person-nel access to the accident area. Phase II is expected to be of longer duration, to require a significant number of operator actions, under milder plant conditions, but with still no personnel access to the acci-dent area. Phase III is expected to be of even longer duration where 6 personnel access is possible.
This guidance is provided in standards for design of safety systems (e.g. IEEE-603, ANSI N1S.2, etc). The four classifica-tions are not mutually exclusive in that a given variable (or instrument) may be included in one or more types. This differentiation by variable type is intended only to guide the designer in his selection of accident monitoring variables and applicable criteria.4.3 Accident Phases The typical accident sequence has been subdivided into three phases: Phase I covers the initial portion of the accident, Phase II covers the stable long-term cooling portion of the accident up to the time where personnel access is possible, and Phase III addresses the period follow-ing personnel access to the accident area. This sub-division has been made so that variable selection and design criteria application can reflect the differing conditions which characterize these three phases.For example, Phase I can be anticipated to be of relatively short dura-tion, having relatively severe plant conditions, and allowing no person-nel access to the accident area. Phase II is expected to be of longer duration, to require a significant number of operator actions, under milder plant conditions, but with still no personnel access to the acci-dent area. Phase III is expected to be of even longer duration where 6 personnel access is possible.
Oifferent design criteria are then appro-priate for each of the three phases. In this Standard, guidance and criteria are provided for Phases i and Ii.7  
Oifferent design criteria are then appro-priate for each of the three phases. In this Standard, guidance and criteria are provided for Phases i and Ii.7 5.0 Oesign Basis The plant designer shall perform and document an analysis to select acci-dent monitoring instruments.
 
===5.0 Oesign===
Basis The plant designer shall perform and document an analysis to select acci-dent monitoring instruments.
He shall identify instruments required by his design to enable the control room operator to: A. Perform pre-planned manual actions.B. Ascertain the performance of: (1) Reactivity control (2) Reactor core cooling (3) Reactor coolant system integrity (4) Containment integrity (5) Radioactive effluent control C. Ascertain the extent to which parameters, which have the potential for causing a breach of the containment, have exceeded the design basis values and to ascertain that a fission product barrier (i.e. fuel clad, reactor coolant system pressure boundary or the containment) has been breached.5.1 Variable Selection for Phases I and II The process for selection of the Accident'Monitoring Instrumentation vari-ables shall include: 5.1.1 For Type A 1) Identification of the postulated accidents for which manual action is required.2) Identification of planned operator actions 3) Identification of the monitored variables needed for planned operator actions.a 5.1.2 For Type B 1) identification of the monitored variables that provide the most direct indication needed to assess the accomplish-ments of: a. Reactivity Control b. Reactor Core Cooling c. Reactor Coolant System Integrity d. Containment Integrity e. Radioactive Effluent Control Guidance on the selection of these variables is provided in Section 6.0.5.1.3 For Type C 1) Identification of the monitored variables that provide the most direct indication of a gross breach of a fission product barrier or of an approach to breach of the con-taimment.
He shall identify instruments required by his design to enable the control room operator to: A. Perform pre-planned manual actions.B. Ascertain the performance of: (1) Reactivity control (2) Reactor core cooling (3) Reactor coolant system integrity (4) Containment integrity (5) Radioactive effluent control C. Ascertain the extent to which parameters, which have the potential for causing a breach of the containment, have exceeded the design basis values and to ascertain that a fission product barrier (i.e. fuel clad, reactor coolant system pressure boundary or the containment) has been breached.5.1 Variable Selection for Phases I and II The process for selection of the Accident'Monitoring Instrumentation vari-ables shall include: 5.1.1 For Type A 1) Identification of the postulated accidents for which manual action is required.2) Identification of planned operator actions 3) Identification of the monitored variables needed for planned operator actions.a 5.1.2 For Type B 1) identification of the monitored variables that provide the most direct indication needed to assess the accomplish-ments of: a. Reactivity Control b. Reactor Core Cooling c. Reactor Coolant System Integrity d. Containment Integrity e. Radioactive Effluent Control Guidance on the selection of these variables is provided in Section 6.0.5.1.3 For Type C 1) Identification of the monitored variables that provide the most direct indication of a gross breach of a fission product barrier or of an approach to breach of the con-taimment.
These instruments may have extended ranges.Guidance on the selection of these variables is provided in Section 6.0.5.1.4 Phase III Access Prior to the termination of Phase II, the ability to gain access to the location of the accident must be determined.
These instruments may have extended ranges.Guidance on the selection of these variables is provided in Section 6.0.5.1.4 Phase III Access Prior to the termination of Phase II, the ability to gain access to the location of the accident must be determined.
Instrumentation that indicates when conditions are acceptable for personnel access shall be identified.
Instrumentation that indicates when conditions are acceptable for personnel access shall be identified.
 
5.2 PERFORMANCE REQUIREMENTS FOR PHASES I ANO I: The process for determining performance requirements of Accident Moni-toring Instrumentation shall include, as a minimum, the following con-siderations:
===5.2 PERFORMANCE===
 
REQUIREMENTS FOR PHASES I ANO I: The process for determining performance requirements of Accident Moni-toring Instrumentation shall include, as a minimum, the following con-siderations:
9 5.2.1 For Types A and 8 1) Identification of 2) Identification of 3) Identification of 4) Identification of ment is needed.5) Identification of ment must operate.the the the the expected range of the process variable.required accuracy of measurement.
9 5.2.1 For Types A and 8 1) Identification of 2) Identification of 3) Identification of 4) Identification of ment is needed.5) Identification of ment must operate.the the the the expected range of the process variable.required accuracy of measurement.
required response characteristics.
required response characteristics.
time interval during which the measure-the local environment in which the instru-5.2.2 For Type C The performance requirements for these instruments are arbitrary.
time interval during which the measure-the local environment in which the instru-5.2.2 For Type C The performance requirements for these instruments are arbitrary.
Guidance on these requirements is provided in Section 6.0.10  
Guidance on these requirements is provided in Section 6.0.10 6.0 DESIGN CRITERIA 6.1 GENERAL DESIGN CRITERIA 6.1.1 SEISMIC QUALIFICATIONS Accident monitoring instrumentation that is to be seismically qualified shall be qualified according to IEEE Standard 344-1975.
 
===6.0 DESIGN===
CRITERIA 6.1 GENERAL DESIGN CRITERIA 6.1.1 SEISMIC QUALIFICATIONS Accident monitoring instrumentation that is to be seismically qualified shall be qualified according to IEEE Standard 344-1975.
The instrumenta-tion shall be qualified to continue to function within the required accuracy following, but not necessarily during, a safe shutdown earth-quake. Vibration loads which occur as a result of plant system operation during any phase for which the instrument is required shall be considered.
The instrumenta-tion shall be qualified to continue to function within the required accuracy following, but not necessarily during, a safe shutdown earth-quake. Vibration loads which occur as a result of plant system operation during any phase for which the instrument is required shall be considered.
 
6.1.2 DURATION Accident monitoring instrumentation shall be qualified for the length of time its function is required.
====6.1.2 DURATION====
Accident monitoring instrumentation shall be qualified for the length of time its function is required.
Unless other times can be justified, Phase II instrumentation shall be qualified to function for not less than 100 days. A shorter time may be acceptable if instrumentation equipment replacement or repair can be accomplished within an acceotable out-of-service time, taking into consideration the environment where the equip-ment is located.6.1.3 DIRECT MEASUREMENT To the extent practical, accident monitoring instrumentation inputs shall be from sensors that directly measure the desired variables.
Unless other times can be justified, Phase II instrumentation shall be qualified to function for not less than 100 days. A shorter time may be acceptable if instrumentation equipment replacement or repair can be accomplished within an acceotable out-of-service time, taking into consideration the environment where the equip-ment is located.6.1.3 DIRECT MEASUREMENT To the extent practical, accident monitoring instrumentation inputs shall be from sensors that directly measure the desired variables.
 
6.1.4 MINIMIZING MEASUREMENTS To the extent practical, the same instruments shall be used for accident monitoring as are used for the normal operations of the plant to enable the operator to use, during an accident situation, instruments with which he is most familiar.
====6.1.4 MINIMIZING====
However, where the required range of accident moni-toring instrumentation results in a loss of instrumentation sensitivity in the normal operating rance, separate instruments shall be used.11 6.1.5 INSTALLATION Permanently installed instrument equipment is required for those instru-ments required to function during Phase I. Permanently installed instru-mentation systems need not be provided for those functions required only for Phases II and III providing it can be demonstrated that the instru-ment components can be installed when required, considering the local environment.
 
6.1.6 INSTRUMENTATION LOCATION AND IDENTIFICATION Accident monitoring instrumentation shall be located accessible to the operator and be distinguishable from other displays so that in an acci-dent situation, the operator can rapidly identify the accident monitoring instrumentation.
MEASUREMENTS To the extent practical, the same instruments shall be used for accident monitoring as are used for the normal operations of the plant to enable the operator to use, during an accident situation, instruments with which he is most familiar.
6.1.7 EQUIPMENT REPAIR, The accident monitoring instrumentation shall be designed to facilitate timely recognition, location, replacement, and repair or adjustment of malfunctioning equipment.  
However, where the required range of accident moni-toring instrumentation results in a loss of instrumentation sensitivity in the normal operating rance, separate instruments shall be used.11  
 
====6.1.5 INSTALLATION====
Permanently installed instrument equipment is required for those instru-ments required to function during Phase I. Permanently installed instru-mentation systems need not be provided for those functions required only for Phases II and III providing it can be demonstrated that the instru-ment components can be installed when required, considering the local environment.
 
====6.1.6 INSTRUMENTATION====
 
LOCATION AND IDENTIFICATION Accident monitoring instrumentation shall be located accessible to the operator and be distinguishable from other displays so that in an acci-dent situation, the operator can rapidly identify the accident monitoring instrumentation.
 
====6.1.7 EQUIPMENT====
 
REPAIR, The accident monitoring instrumentation shall be designed to facilitate timely recognition, location, replacement, and repair or adjustment of malfunctioning equipment.  
-6.1.8 TEST AND CALIBRATION 6.1.3.1 Test Capability shall be provided for testing, with a high degree of confi-dence, the operational availability of each instrument channel during plant operation.
-6.1.8 TEST AND CALIBRATION 6.1.3.1 Test Capability shall be provided for testing, with a high degree of confi-dence, the operational availability of each instrument channel during plant operation.
This may be accomplished in various ways, for example: 1. By observing the effect of perturbing the monitored variable.2. By observing the effect of introducing and varying, as appropriate, a substitute inout to the sensor of the same nature as the measured variable.12  
This may be accomplished in various ways, for example: 1. By observing the effect of perturbing the monitored variable.2. By observing the effect of introducing and varying, as appropriate, a substitute inout to the sensor of the same nature as the measured variable.12
: 3. By cross-checking between channels that bear a known relationship to.each other.Where testing during reactor operation is not possible, it must be shown that there is no practical way of implementing such a requirement without adversely affecting plant safety or operability.
: 3. By cross-checking between channels that bear a known relationship to.each other.Where testing during reactor operation is not possible, it must be shown that there is no practical way of implementing such a requirement without adversely affecting plant safety or operability.
In addition, it must be shown that the probability of a failure of the component which is not periodically tested is acceptably low and that such testing can be rou-tinely performed when the reactor is shut down.6.1.8.2 Calibration Capability shall be provided for calibration of each instrument channel during normal plant operation or during shutdown as determined by the required interval between calibrations.
In addition, it must be shown that the probability of a failure of the component which is not periodically tested is acceptably low and that such testing can be rou-tinely performed when the reactor is shut down.6.1.8.2 Calibration Capability shall be provided for calibration of each instrument channel during normal plant operation or during shutdown as determined by the required interval between calibrations.
Equipment that does not require periodic calibration is exempt from this requirement.
Equipment that does not require periodic calibration is exempt from this requirement.
 
5.1.9 DIVERSITY Diversity is preferred in fufilling redundancy requirements.
====5.1.9 DIVERSITY====
Diversity is preferred in fufilling redundancy requirements.
5.1.10 REDUNDANT READOUT AMBIGUITY Where a disagreement between redundant displays could lead the operator to defeat or fail to accomplish a required safety function, additional information shall be provided to allow the operator to deduce the actual conditions that are required for him to perform his role. This may be accomplished by providing an independent channel which monitors a dif-ferent variable bearing a known relationship to the redundant channel or by providing an additional independent channel of instrumentation of the same variable or by providing the capability for the operator to perturb the measured variable and determine by observation of the response which instrumentation display has failed.13
5.1.10 REDUNDANT READOUT AMBIGUITY Where a disagreement between redundant displays could lead the operator to defeat or fail to accomplish a required safety function, additional information shall be provided to allow the operator to deduce the actual conditions that are required for him to perform his role. This may be accomplished by providing an independent channel which monitors a dif-ferent variable bearing a known relationship to the redundant channel or by providing an additional independent channel of instrumentation of the same variable or by providing the capability for the operator to perturb the measured variable and determine by observation of the response which instrumentation display has failed.13
* 0 6.2 TYPE B INSTRUMENTS
* 0 6.2 TYPE B INSTRUMENTS 6.2.1 GENERAL REQUIREMENTS  
 
====6.2.1 GENERAL====
REQUIREMENTS  
-The number of instruments used shall be only that minimum set needed to adequately monitor the accomplishment of the following functions:
-The number of instruments used shall be only that minimum set needed to adequately monitor the accomplishment of the following functions:
: a. Reactivity Control b. Reactor Core Cooling c. Reactor Coolant System Integrity d. Containment Integrity e. Radioactive Effluent Control Type 3 instruments provide control room indication beyond that which may be required for any preplanned operator action and as such constitute an extra set of instrumentation which results in an additional layer of protection.
: a. Reactivity Control b. Reactor Core Cooling c. Reactor Coolant System Integrity d. Containment Integrity e. Radioactive Effluent Control Type 3 instruments provide control room indication beyond that which may be required for any preplanned operator action and as such constitute an extra set of instrumentation which results in an additional layer of protection.
 
6.2.2 VARIABLES FOR REACTIVITY CONTROL MONITORING The measured variable shall indicate the accomplishment of control of reactivity in the core. The measured variable should be neutron flux.The range of measurement should extend from one count per second on the source range instrument to the intermediate range instrument value cor-responding to 1.5. of full reactor power. This range is intended to encompass all neutron flux levels at which the core can be subcritical.
====6.2.2 VARIABLES====
6.2.3 VARIABLES FOR CORE COOLING MONITORING The measured variables shall indicate the accomplishment of core cool-ing. For the PWR, the measured variables should be TH, TC, pres-surizer level, and pressurizer pressure.
 
For the BWR, the measured variable should be reactor vessel water level. Incore thermocouple monitoring should be considered for inclusion as a desireable variable to ascertain cooling.14 6.2.4 VARIABLES FOR REACTOR COOLANT SYSTEM INTEGRITY The measured variable shall indicate the accomplishment of RCS inte-grity. The measured variable should be primary system pressure.6.2.5 VARIABLES FOR CONTAINMENT INTEGRITY The measured variables shall indicate the accomplishment of containment integrity.
FOR REACTIVITY CONTROL MONITORING The measured variable shall indicate the accomplishment of control of reactivity in the core. The measured variable should be neutron flux.The range of measurement should extend from one count per second on the source range instrument to the intermediate range instrument value cor-responding to 1.5. of full reactor power. This range is intended to encompass all neutron flux levels at which the core can be subcritical.
 
====6.2.3 VARIABLES====
 
FOR CORE COOLING MONITORING The measured variables shall indicate the accomplishment of core cool-ing. For the PWR, the measured variables should be TH, TC, pres-surizer level, and pressurizer pressure.
For the BWR, the measured variable should be reactor vessel water level. Incore thermocouple monitoring should be considered for inclusion as a desireable variable to ascertain cooling.14  
 
====6.2.4 VARIABLES====
 
FOR REACTOR COOLANT SYSTEM INTEGRITY The measured variable shall indicate the accomplishment of RCS inte-grity. The measured variable should be primary system pressure.6.2.5 VARIABLES FOR CONTAINMENT INTEGRITY The measured variables shall indicate the accomplishment of containment integrity.
The measured variables should be containment hydrogen con-centration, containment pressure and containment isolation valve posi-tions..6.2.6 VARIABLES FOR RADIOACTIVE EFFLUENT CONTROL The measured variables shall indicate the accomplishment of radioactive effluent control. The measured variables should be noble gas monitoring of the identified plant release points.6.3 TYPE C INSTRUMENTS 6.3.1 Type C instruments shall meet the following criteria: 5.3.1.1 The number of instruments used shall be only that minimum set needed to adequately monitor the three barriers;6.3.1.2- Each measurement shall be as direct as possible;6.3.1.3 Any chosen measurement shall detect a gross breach of one or more barriers (i.e., > 1 percent fuel clad failure, a RCS pressure boundary breach producing a loss of reactor coolant inventory in excess of the normal makeup capability, a con-tainment breach capable of producing radiation releases in excess of 10 CFR 100 at the site boundary using TID-14844 source terms); the ranges established for Type C instruments are not mechanistically related to a postulated accident scenario.15 6.3.1.4 During the period of need for Type C instruments, no other failures shall be assumed in the analysis beyond the assumed breach of a barrier coincident with loss of off-site power;0.3.2 Fuel Clad Barrier Monitoring 6.3.2.1 The measured variable shall detect and alarm the breach of the fuel clad barrier (i.e., > 1 percent fuel clad failure);6.3.2.2 Operator sampling of reactor coolant shall be used as the means to verify the measured variable alarm.6.3.2.3 The measured variable should be reactor coolant system radia-tion. The instrument range should be equivalent to the fuel clad gap activity corresponding to 0.5% to 5% failed fuel. A narrow accuracy band for this measured variable is not signi-ficant in achieving this function; for example, +50%, to +100%accuracy of reading should be acceptable.
The measured variables should be containment hydrogen con-centration, containment pressure and containment isolation valve posi-tions..6.2.6 VARIABLES FOR RADIOACTIVE EFFLUENT CONTROL The measured variables shall indicate the accomplishment of radioactive effluent control. The measured variables should be noble gas monitoring of the identified plant release points.6.3 TYPE C INSTRUMENTS 6.3.1 Type C instruments shall meet the following criteria: 5.3.1.1 The number of instruments used shall be only that minimum set needed to adequately monitor the three barriers;6.3.1.2- Each measurement shall be as direct as possible;6.3.1.3 Any chosen measurement shall detect a gross breach of one or more barriers (i.e., > 1 percent fuel clad failure, a RCS pressure boundary breach producing a loss of reactor coolant inventory in excess of the normal makeup capability, a con-tainment breach capable of producing radiation releases in excess of 10 CFR 100 at the site boundary using TID-14844 source terms); the ranges established for Type C instruments are not mechanistically related to a postulated accident scenario.15 6.3.1.4 During the period of need for Type C instruments, no other failures shall be assumed in the analysis beyond the assumed breach of a barrier coincident with loss of off-site power;0.3.2 Fuel Clad Barrier Monitoring 6.3.2.1 The measured variable shall detect and alarm the breach of the fuel clad barrier (i.e., > 1 percent fuel clad failure);6.3.2.2 Operator sampling of reactor coolant shall be used as the means to verify the measured variable alarm.6.3.2.3 The measured variable should be reactor coolant system radia-tion. The instrument range should be equivalent to the fuel clad gap activity corresponding to 0.5% to 5% failed fuel. A narrow accuracy band for this measured variable is not signi-ficant in achieving this function; for example, +50%, to +100%accuracy of reading should be acceptable.
instrument tran-sient response should be compatible with its recorder.5.3.3 Reactor Coolant System Pressure Boundary Monitoring 6.3.3.1 The measured variable(s) shall detect and alarm a breach of the reactor coolant system that produces a loss of coolant inventory in excess of normal makeup capability.
instrument tran-sient response should be compatible with its recorder.5.3.3 Reactor Coolant System Pressure Boundary Monitoring 6.3.3.1 The measured variable(s) shall detect and alarm a breach of the reactor coolant system that produces a loss of coolant inventory in excess of normal makeup capability.
Line 295: Line 235:
No additional qualification margin needs to be added to the extended range parameter.
No additional qualification margin needs to be added to the extended range parameter.
See figure 6.3-1. All environmental envelopes except that per-taining to the parameter measured by the instrument shall be those associated with the Design Basis Accidents.
See figure 6.3-1. All environmental envelopes except that per-taining to the parameter measured by the instrument shall be those associated with the Design Basis Accidents.
 
5.4 SPECIFIC DESIGN CRITERIA Design Criteria specific to particular accident phases and variable types are presented in Table 6.4-1.18 TABLE 6.4.1 DESIGN CRITERIA CRITERION l.. Qualify seismically to IEEE 344-75 (operate after SSE)2. Meet single failure per IEEE 379-77 3. Qualify environmen-tally to IEEE 323-74 4. Consider loss of off-site power 5. Power source, 6. Out of service interval-prior to accident 7. Otit of service inter-val -during accident PHASE 1 VARIABLE TYPE B A Yes Yes Yes Yes Yes Yes Yes Yes Emergency (2) .None Emerg.(2)None C No No A Yes Yes Yes(l)Yes Emerg.<72 fir(3)<2 hir Yes Yes Emerg.(2)(2)PHASE II VARIABLE TYPE B No Yes Yes No Normal(6)(2)(2)C No No Yes U )No Normal (6).<72 fIrs 3)<2 hIrs 0 0 TABLE 6.4-1 (Continued)
===5.4 SPECIFIC===
DESIGN CRITERIA Design Criteria specific to particular accident phases and variable types are presented in Table 6.4-1.18 TABLE 6.4.1 DESIGN CRITERIA CRITERION l.. Qualify seismically to IEEE 344-75 (operate after SSE)2. Meet single failure per IEEE 379-77 3. Qualify environmen-tally to IEEE 323-74 4. Consider loss of off-site power 5. Power source, 6. Out of service interval-prior to accident 7. Otit of service inter-val -during accident PHASE 1 VARIABLE TYPE B A Yes Yes Yes Yes Yes Yes Yes Yes Emergency (2) .None Emerg.(2)None C No No A Yes Yes Yes(l)Yes Emerg.<72 fir(3)<2 hir Yes Yes Emerg.(2)(2)PHASE II VARIABLE TYPE B No Yes Yes No Normal(6)(2)(2)C No No Yes U )No Normal (6).<72 fIrs 3)<2 hIrs 0 0 TABLE 6.4-1 (Continued)
DESIGLN CRITERIA P11ASE 1 VARIABLE TYPE CRITERION A B 8. Portable instrumenta-No No t iol 9. Level of quality ANSI N45.2 ANSI t assurance 10. Display type(4) Continuous Contif 11. Display method Recording(5)
DESIGLN CRITERIA P11ASE 1 VARIABLE TYPE CRITERION A B 8. Portable instrumenta-No No t iol 9. Level of quality ANSI N45.2 ANSI t assurance 10. Display type(4) Continuous Contif 11. Display method Recording(5)
Record 12. Identification as Yes Yes accident monitoring type 13. Periodic Test per Yes Yes IEEE-338-1977 NOTES: (1) See Paragraph 6.3.6 of this Standard.(2) IEEE 279-1971 Paragraph 4.11 Exemuption C No(7)445.2 luou s di ng A Yes ANSI N45.2 Continuous Indicator Yes Yes ANSI N45.2 Continuous Recording(5)
Record 12. Identification as Yes Yes accident monitoring type 13. Periodic Test per Yes Yes IEEE-338-1977 NOTES: (1) See Paragraph 6.3.6 of this Standard.(2) IEEE 279-1971 Paragraph 4.11 Exemuption C No(7)445.2 luou s di ng A Yes ANSI N45.2 Continuous Indicator Yes Yes ANSI N45.2 Continuous Recording(5)

Revision as of 15:58, 12 July 2019

Proposed Revision 2 to Regulatory Guide 1.97, Instrumentation for Light-Water-Cooled Nuclear Power Plants to Assess Plant and Environs Conditions During and Following an Accident, Draft 1
ML080390415
Person / Time
Site: Watts Bar  Tennessee Valley Authority icon.png
Issue date: 10/15/1979
From:
American National Standards Institute (ANSI)
To:
Office of Nuclear Reactor Regulation
References
NUDOCS 7912060569
Download: ML080390415 (55)


Text

3 Draft 1 October 15, 1979 PROPOSED REVISION 2 TO REGULATORY GUIDE 1.97 INSTRUMENTATION FOR LIGHT-WATER-COOLED NUCLEAR POWER PLANTS TO ASSESS PLANT AND ENVIRONS CONDITIONS DURING AND FOLLOWING AN ACCIDENT A. INTRODUCTION Criterion 13, "Instrumentation and Control," of Appendix A, "General Design Criteria for Nuclear Power Plants," to 10 CFR Part 50, "Licensing of Production and Utilization Facilities," includes a requirement that instrumentation be provided to monitor variables and systems for accident conditions as appropriate to ensure adequate safety.Criterion 19, "Control Room," of Appendix A to 10 CFR Part 50 includes a requirement that a control room be provided from which actions can be taken to maintain the nuclear power unit in a safe condition under accident conditions, including loss-of-coolant accidents and that equipment at appropriate locations outside the control room be provided with a design capability for prompt hot shutdown of the reactor including necessary instrumentation.

Criterion 64, "Monitoring Radioactivity Releases," of Appendix A to 10 CFR Part 50 includes a requirement that means be provided for monitoring the reactor containment atmosphere, spaces containing components for recirculation of loss-of-coolant accident fluid, effluent discharge paths, and the plant environs for radioactivity that may be released from postulated accidents.

This guide describes a method acceptable to the NRC staff for complying with the Commission's regulations to provide instrumentation to monitor plant variables and systems during and following an accident in a light-water-cooled nuclear power plant.1.97-1 aK B. DISCUSSION Indications of plant variables and status of systems important to safety are required by the plant operator (licensee) during accident situations to (1) provide information required to permit the operator to take pre-planned manual actions to accomplish safe plant shutdown; (2) determine whether the reactor trip, engineered-safety-feature systems, and manually initiated systems are performing their intended functions, i.e., reactivity control, core cooling, maintaining reactor coolant system integrity, and maintaining containment integrity; (3) provide information to the operator that will enable him to determine the potential for causing a breach of the barriers to radioactivity release (i.e., fuel cladding, reactor coolant pressure boundry and containment) and if a barrier has been breached; (4) furnish data for deciding on the need to take unplanned action if an automatic or manually initiated safety system is not functioning properly or the plant is not responding properly to the safety systems in operation; (5) allow for early indication of the need to initiate action necessary to protect the public and for an estimate of the magnitude of the impending threat.At the start of an accident, it may be difficult for the operator to deter-mine immediately what accident has occurred or is occurring and, therefore, determine the appropriate response.

For this reason, reactor trip and certain other safety actions (e.g., emergency core cooling actuation, containment isola-tion, or depressurization) have been designed to be performed automatically during the initial stages of an accident.

Instrumentation is also provided to indicate information about plant parameters required to enable the operation of manually initiated safety systems and other appropriate operator actions involv-ing systems important to safety.1.97-2

  • S Instrumentation is also needed to provide information about some plant parameters that will alert the operator to conditions that have degraded beyond those postulated in the accident analysis so that the operator can take actions that are available to mitigate the consequences.

It is not intended that the operator be encouraged to circumvent systems important to safety prematurely, but that he be adequately informed in order that unplanned actions can be taken when necessary.

Examples of serious events that could threaten safety if conditions degrade beyond those assumed in the Final Safety Analysis Report are loss-of-coolant accidents (LOCAs), overpressure transients, ATWSs reactivity excursions, and releases of radioactive materials.

Such events require that the operator under-stand, in a short time period, the ability of the barriers to limit radioactivity release, i.e., the potential for breach of a barrier, or an actual breach of a barrier by an accident in progress.It is essential that the required instrumentation be capable of surviving the accident environment in which it is located for the length of time its func-tion is required as defined by ANS-4.-5, Section 3.0. It could therefore either be designed to withstand the accident environment or be protected by a local protected environment.

If the environment surrounding an instrument component is the same for accident and normal operating conditions (e.g., some instrumen-tation components outside of containment or those in the main control room powered by a Class lE source), the instrumentation components need no special environmental qualification.

It is important that accident-monitoring instrumentation components and their mounts that cannot be located in other than non-Seismic Category I build-ings be conservatively designed for the intended service.1.97-3 Parameters selected for accident monitoring can be selected so as to permit relatively few instruments to provide the essential information needed by the operator for postaccident monitoring.

Further, it is prudent that a limited number of those parameters (e.g., containment pressure, primary system pressure)be monitored by instruments qualified to more stringent environmental require-ments and with ranges that extend well beyond that which the selected parameters can attain under limiting conditions.

It is essential that the range selections not be arbitrary but sufficiently high that the instruments will always be on-scale; for example, a range for the containment pressure monitor extending to the burst pressure of the containment in order that the operator will not be blind as to the level of containment pressure.

Provisions of such instruments are important so that responses to corrective actions can be observed and the need for, and magnitude of, further actions determined.

On the other hand, we should also make sure that when a range is extended, the sensitivity and accu-racy of the instrument are within acceptable limits.Normal power plant instrumentation remaining functional for all accident conditions can provide indication, records, and (with certain types of instru-ments) time-history responses for many parameters important to following the course of the accident.

Therefore, it is prudent to select the required accident-monitoring instrumentation from the normal power plant instrumentation to enable the operator to use, during accident situations, instruments with which he is most familiar.

Since some accidents impose severe operating requirements on instrumen-tation components, it may be necessary to upgrade those instrumentation components to withstand the more severe operating conditions and to measure greater variations of monitored variables that may be associated with the accident if they are to be 1.97-4 used for both accident and normal operation.

However, it is essential that instru-mentation so upgraded does not compromise the accuracy and sensitivity required for normal operation.

In some cases this will necessitate use of overlapping ranges of instruments to monitor the required range of the parameter to be monitored.

Draft Standard ANS-4.5, "Functional Requirements for Post Accident Monitoring Capability for the Control Room Operator of a Nuclear Power Generating Station," dated September 1979, delineates criteria for determining the variables to be monitored by the control room operator, as required for safety, during the course of an accident and during the long-term stable shutdown phase followng an accident.Draft Standard ANS-4.5 was prepared by ANS 4 Working Group 4.5 with two primary objectives, (1) to address that instrumentation which permits the operator to monitor expected parameter changes in an accident period, and (2) to address extended range instrumentation deemed appropriate for the possibility of encounter-ing previously unforeseen events.The standard defines four classifications of variable types for the purpose of aiding the designer in his selection of accident monitoring instrumentation and applicable criteria. (A fifth type (Type E) has been added by this regula-tory guide.) The types are, (1) Type A -those variables that provide-informa-tion needed for pre-planned operator actions, (2) Type B -those variables that provide information to indicate whether plant safety functions are being accom-plished, (3) Type C -those variables that provide information to indicate the potential for being breached or the actual breach of the barriers to fission product release, i.e., fuel cladding, primary coolant pressure boundary., and containment, (4) Type D -those variables that provide information to indicate the performance of individual safety systems, and (5) Type E -those variables to be monitored as required to provide defense-in-depth and for diagnosis and 1.97-5 other useful purposes.

Type A variables have not been included in the listings of variables to be measured because they are plant specific and will depend upon the operations that the designer chooses for pre-planned manual action.The five classifications are not mutually exclusive in that a given variable (or instrument) may be included in one or more types, as well as for normal power plant operation.

Where such multiple listing occurs, it is essential that instrumentation be capable of meeting the most stringent requirements.

The time phases (Phases I, II, & III) delineated in ANS-4.5 are not speci-fied for each variable in this regulatory guide. These considerations are plant specific.

It is important that the required instrumentation survive the accident environment and function as long as the information it provides is needed by the plant operator.C. REGULATORY POSITION The criteria, requirements, and recommendations contained in Draft Standard ANS-4.5, "Functional Requirements for Post Accident Monitoring Capability for the Control Room Operator of a Nuclear Power Generating Station," dated September 1979, are considered by the NRC staff to be generally acceptable for providing instrumentation to monitor variables and systems for accident condi-tions and for monitoring the reactor containment, spaces containing components for recirculation of loss-of-coolant accident fluids, effluent discharge paths, and the plant environs for radioactivity that may be released during and follow-ing an accident from a nuclear power plant subject to the following:

(1) Section 2.0 of ANSI-4.5, defines the scope of the standard as contain-ing criteria for determining the variables to be monitored by the control room operator during and following an accident that will need some operator action.1.97-6 Consideration should be given to the additional requirements (e.g., emergency planning) of variables to be monitored by the plant operator (licensee) during and following an accident.

Instrumentation selected for use by the plant opera-tor for monitoring conditions of the plant are useful in an emergency situation and for other purposes and therefore should be factored into the emergency plans action level criteria.(2) In Section 3.0 of ANS-4.5, the definition of "Type C" includes two items, (1) and (2). Item (1) includes those instruments that indicate the extent to which parameters, which indicate the potential for a breach in the containment, have exceeded the design basis values. In conjunction with the parameters that indicate the potential for a breach in the containment, the parameters that have the potential for causing a breach in the fuel cladding (e.g., core exit temperature) and the reactor coolant pressure boundary (e.g., reactor coolant pressure) should also be included.

References to Type C instru-ments, and associated parameters to be measured, in Draft Standard ANS-4.5 should include this expanded definition, e.g., Section 4.2, Section 5.0c, Section 5.1.3, Section 5.2.2, Section 6.3.(3) Section 3.0 of ANS-4.5 defines design basis accident events. In conjunction with the design basis accident events delineated in the standard, those events which are expected to occur one or more times during the life of a nuclear power unit and include but are not limited to loss of power to all recirculating pumps, tripping of the turbine generator set, isolation of the main condenser, and loss of all offsite power, should be included.(4) Section 4.2 of ANS-4.5, discusses the various types of variables.

With regard to the discussion of Type D variables, Type 0 variables and instru-ments are within the scope of Accident Monitoring Instrumentation, although 1. 97-7 they are not addressed in Oraft Standard ANS-4.5. They are, however, along with an additional type, Type E, included in this regulatory guide. (See Tables 1, 2 and 3)(5) Section 5.2.1(5) of ANS-4.5 pertains to the delineation of the local environment in which instruments must operate. Section 5.2.1(5) should be understood to require identification of the range of the local physical and electrical environments (e.g., normal, abnormal, accident, and post-accident) in which all of the various instrumentation components are required to operate (e.g., sensors, cables, signal conditioning equipment, indicators).

(6) Section 5.2.2 of ANS-4.5 pertains to the performance requirements for Type C instrumentation.

In conjunction with Section 5.2.2, there should be:.(1) Identification of the range of the process variable. (Note -the range selected should extend well beyond that which the variable value can attain under limiting conditions)

(2) Identification of the required accuracy of measurement (3) Identification of the required response characteristics (4) Identification of the time interval beginning with initiation of an accident to as long as the measurement is needed (5) Identification of the local environment (including energy supply) in which the various instrumentation components are required to operate.(7) Section 6.1.1 of ANS-4.5, pertains to seismic qualification criteria.In conjunction with Section 6.1.1, those instrumentation components which should be seismically qualified are identified in Table 1 of this regulatory guide.(8) Section 6.1.1 of ANS-4.5, pertains, in part, to the consideration of vibrational loads. TIn conjunction with Section 6.1.1, those instrumentation 1.97-8 components which are subjected to vibrational loads that occur as a result of plant system operation during any phase for which the instrumentation is required should be qualified to function during and/or following such vibrational loads.(9) Section 6.1.2 of ANS-4.5, pertains to the duration that instrumentation is qualified to function.

In conjunction with Section 6.1.2, Phase II instrumen-tation should be qualified to function for not less than 200 days unless a shorter time, based on need or component accessability for replacement or repair, can be justified.

(10) Section 6.1.6 of ANS-4.5 pertains to instrumentation location and identification.

In conjunction with Section 6.1.6, accident monitoring instru-mentation displays should be located in direct view of the plant operator and be distinguished from other displays.

Other accident monitoring instrumentation components should be accessible to the plant operator for maintenance and repair although this may not be possible for some components in some accident conditions.

(11) Section 6.2.1 of ANS-4.5 pertains to general requirements for Type B instruments.

In conjunction with Section 6.2.1, Type B instruments are essen-tial to meeting the requirements of Criterion 13 and Criterion 64 of Appendix A to 10 CFR Part 50 and are not considered to be an "extra set of instruments which result in an additional layer of protection." Type B instruments are essential to the monitoring of variables and systems during accident conditions and in following the course of an accident.(12) Section 6.2.2, 6.2.3, 6.2.4, 6.2.5, 6.2.6, 6.3.2, 6.3.3, 6.3.4, and 6.3.5 of ANS-4.5 pertain to variables and variable ranges for monitoring.

In conjunction with the above sections, Tables 1, 2 and 3 of this regulatory guide (which includes those parameters mentioned in the above sections) should be used in developing the minimum set of instruments and their respective ranges for accident monitoring instrumentation for each nuclear power plant.1.97-9 (13) Sections 6.3.2.3, 6.3.3.3, 6.3.3.4, 6.3.4.3, 6.3.4.4, 6.3.5.2, 6.3.5.3, and 6.3.5.4 of ANS-4.5 pertain, in part, to instrument transient response and relate this to compatability with recorder capabilities.

In conjunction with the above sections, the transient response requirements of each measurement should be determined on a case-by-case basis by analysis of the event and operator response capabilities.

(14) Sections 6.3.3.3, 6.3.3.4, and 6.3.4.3 of ANS-4.5, pertain, in part, to measurement accuracy.

In conjunction with the above sections, the accuracy of each measurement should be consistent with the requirements as established by analysis of the event being monitored.

(15) Section 6.3.6.1.1 ANS-4.5 pertains, in part, to the qualification of Type C instrumentation components.

In conjunction with Section 6.3.6.1.1, the environmental envelope for qualification should be the extreme value of each environmental parameter, except the variable being monitored, as determined by the accident analysis for all accidents evaluated in the safety analysis of the plant.(16) Table 6.4.1 of ANS-4.5 pertains to design criteria for accident monitoring instrumentation.

In conjunction with Table 6.4.1, the provisions as indicated in Table 1 of this regulatory guide should be used.D. IMPLEMENTATION This proposed revision has been released to encourage public participation in its development.

Except in those cases in which an applicant proposes an acceptable alternative method for complying with specified portions of the Commission's regulations, the method to be described in the active guide reflect-ing public comments will be used in the evaluation of the following applica-tions that are docketed after the implementation date to be specified in the guide: 1. 97-10

  • 0 P 1. Preliminary Design Approval (PDA) applications and Preliminary Duplicate Design Approval (PDA) applications.
2. Final Design Approval, Type 2 (FDA-2), applications and Final Duplicate Design Approval, Type 2 (FDDA-2), applications.
3. Manufacturing License (ML) applications.
4. Construction Permit (CP) applications except for those portions of CP applications that reference standard designs (i.e., PDA, FDA-1, FDA-2, PDDA, FDDA-1, FDDA-2, or ML) or that reference qualified base plant designs under the replication option.In addition, the NRC staff intends to implement part or all of this guide for all operating plants, plants under construction, all PDA's and FDA's, all PDDA's and all FDDA's which may involve additions, elimination, or modification of structures, systems, or components of the facility after the construction permit, or design approval has been issued. All backfitting decisions in accordance with the positions stated in this guide will be determined by the staff on a case-by-case basis.The implementation date of this guide will in no case be earlier than 1. 97-11
  • TABLE 1 -DESIGN CRITERIA' 0 INSTRUMENTATION TYPES 2 CRITERIA A 1. Seismic Qualification per Reg Guide 1.100 2. Single Failure Criteria per Reg Guide 1.53 3. Environmental Qualification per Reg Guide 1.89 4. Consider loss of off-site power 5. Power source 6. Out of service interval before accident 7. Portable 8. Quality assurance level 9. Display type 1 2 10. Display method 11. Unique identification
12. Periodic testing per Reg Guide 1.118 NOTES for Table 1: (1) Unless guide, Specif Instru monito efflue for me yes yes yes yes Emr 5 7 no 11 Con 1 3 Rec 1 5 yes yes B yes yes yes yes CB 6 7 no 11 Con 1 3 Rec1 6 yes yes C yes yes yes 3 yes CB 6 7 no 1 0 1 1 Con 1 3 Rec 1 6 yes yes D no no yes yes Emr 5 8 no 1 0 11 OD14 Ind 1 7 no yes E no no no4 yes Emrs 13 nolo 11 OD14.Ind7, 18 no no different specifications are given in this regulatory the specifications in ANSI N320-1979, "Performance

'ications for Reactor Emergency Radiological Monitoring mentation," apply to the high-range containment area rs, area exposure rate monitors in other buildings, ent and environmental monitors, and portable instruments asuring radiation or radioactivity.

(2) Type A -Those instruments which provide information required to take pre-planned manual actions.Type B -Those instruments which provide information to monitor the process of accomplishing critical safety functions.

Type C -Those instruments that indicate the potential for breach-ing or the actual breach of the barriers to fission pro-duct release.Type D -Those instruments that indicate the performance of in-dividual safety systems.Type E -Those instruments that provide information for defense-in-depth and for diagnosis or other useful purposes.1.97-12 0 NOTES for Table 1 continued:

(3) -See Paragraph 6.3.6 of Draft Standard ANS-4.5.(4) Qualified to the conditions of fts operation.(s) Emergency power source.(6) Critical Instrument Buss -Class 1E Power.(7) IEEE 279-1971 Paragraph 4.11, "Exemption".

(8) Based on normal tech spec requirements on out-of-service for the safety system it serves.(9) Not necessary to include in tech specs.(10) Radiation monitoring outside containment may be portable if as designated.

(11) Level of quality assurance per 10 CFR Part 50, Appendix B.(12) Continuous indication or recording displays a given variable at all times; intermittent indi-cation or recording displays a given variable periodically; on demand indication or recording displays a given variable only when requested.

13 ) Continuous display.(14) Indication on demand.(15) Where trend or transient information is essential to planned operator actions.(16) Recording.

(1?) Dial or digital indication.

CIS) Effluent release monitors require recording, in-cluding effluent radioactivity monitors, environs exposure rate monito-rs, and meteorology monitors.1.97-13 TABLE 2 -P':!R VIARIABLES Measured Variable CORE: Core Exit Temperature Control Rod Position Neutron Flux REACTOR COOLANT SYSTEM: RCS Hot Leg Temper-ature RCS Cold Leg Temper-ature RCS Pressure Pressurizer Level Degree of Subcooling

-- § Buy- ! r puz 150 0 F to 2300aF Full in in or not full 1 c/s to 1% power (at least one fission counter)150 0 F to 750aF 130*F to 750 0 F 15 psia to 4000 psig Bottom tangent to top tangent 200OF subcooiing to 3 5 0 F superheat B,C D E B BC B,D ANS-4.5, Section 6.2.3 Provide incore temperature measurements to identify localized hot areas.(Approximately 50 measurements)

Provide positive indication that the con-trol rods are fully inserted.(Minimum 5 days after accident)ANS-4.5, Section 6.2.2 For indication of approach to criticality.

ANS-4.5, Section 6.2.3 To aid in determining reactor system sub-cooling and to provide indication of natural circulation.

ANS-4.5, Section 6.2.3 To provide indication of natural circula-tion; to provide input for heat balance calculations; for direct indication of ECCS injection.

AVNS-4.5, Sections 6.2.3 and 6.2.4 For indication of an accident and to in-dicate that actions must be taken to mitigate an event.ANS-4.5, Section 6.2.3 Level indication is required to assure proper operation of the pressurizer and to assure safe operation of heaters. It is also used in conjunction with changes in reactor pressure to determine leak and void sizes.For indication of margin in core cooling and the need for emergency coolant addi-tions or reductions as the margin changes and to obviate the necessity to consuit steam tables.1.97-14 0 Tvne I Rance D. *t -

TABLE 2 -PWR VARIABLES continued

-Measured Variable REACTOR COOLANT SYSTEM CONTINUED:

Reactor Flow Coolant Loop Primary System Safety Relief Valve Posi-tions or Flow Through or Pressure In Relief Valve Lines Radiation Level in Primary Coolant Watei CONTAINMENT:

Containment Pressure Containment Atmos-phere Temperature Containment Hydrogen Concentration Containment Isola-tion Valve Position Range--1 e P urwnw 0 to 120%]] des-20% to 20%J' flogw Closed-not closed 10 uCi/g to 10 Ci/g 10 psia pressure to 3 times design press-ure 2 for concrete; 4.times design pressure for steel 40*F to 400*F 0 to 10%(capable from 10 I maximum c ure 2 of operating Dsia to design press-Closed-not closed B,D B,D C B,C E B,C B,D To provide indication being cooled.that the core is By these measurements the operator knows if there is a path open for loss of cool-ant and that an event may be in progress.ANS-4.5, Section 6.3.2 For early indication of fuel cladding failure and estimate of extent of damage.ANS-4.5, Sections 6.2.5, 6.3.3, 6.3.4, and 6.3.5 For indication of the integrity of the primary or secondary system pressure boundaries.

To indicate the potential for leakage from the containment; to indicate integrity of the containment.

For indication of the performance of the containment cooling system and adequate mixing.ANS-4.5, Sections 6.2.5 and 6.3.5 For indication of the need, and to meas-ure the performance of the containment hydrogen recombiner.

ANS-4.5, Section 6.2.3 To indicate the status of containment isolation and to provide information on the status of valves in process lines which could carry radioactive materials out of containment.

1. 97-15 Type Piirnnose TABLE 2 -PWR VARIABLES continued

-Measured Variable CONTAINMENT CONTINUED:

Containment Sump Water Level High Range Contain-ment Area Radiation SECONDARY SYSTEMiS: Steam Generator Pressure Steam Generator Level Auxiliary Flow Feedwater Main Feedwater Flow Safety/Relief Valve Positions or Main Steam Flow Radiation in Condenser Air Removal System Radioactivity in Efflu-ent from Steam Gener-ator Safety Relief Valves or Atmospheric Dump Valves Range Narrow range (sump)Wide range (bottom of containment to 600,000 gallon level equiva-lent)1 to 107 R/hr (60 keV to 3 MeV photons with +20% accuracy for photons of 0.1 to 3 MeV)[107 R/hr for pho-tons is approximately equivalent to 108 rads per hour for betas and photons]From pressure for safety valve setting to plus 20% of safety valve setting From tube sheet separators to 0 to 110% design flow 1 0 to 110% design flow 1 Closed-not closed 10-7 to 105 Ci/cc 10-7 to lo05 ;1Ci/cc I Type BC B,C D D D E B,D B,C , r To indicate leakage from the primary to the secondary system and measure of noble gas release rate to atmosphere.

An indication of release from the secondary system and measure of noble gas release rate to atmosphere.

1.97-16 For indication of leakage within the containment and to assure adequate in-ventory for performance of the ECCS.For implementation of GDC 64 and to help identify if an accident has degraded be-yond calculated values and to indicate its magnitude to determine action to protect the public.For indication of integrity of the sec-ondary system, and an indication of cap-ability for decay heat removal.For indication of. integrity of the sec-ondary system, and an indication of cap-ability for decay heat removal.To indicate an adequate source of water to each steam generator upon loss of main feedwater.

To indicate an adequate source of water to each steam generator.

To Indicate integrity of secondary system (vis--a-vis pipe break).I Type Puroose TABLE 2 -POR VARIABLES con Olued -Measured Variable AUXILIARY SYSTEMS: Containment Spray Flow Flow in HPI System Flow in LPI System Emergency Coolant Water Storage Tank Level Accumulator Tank Level Accumulator Isolation Valve Positions RHR System Flow RER Heat Exchanger Out Temperature Component Cooling Water Temperature Component Cooling Water Flow Flow in UHS Loop Temperature in Ulti-mate Heat Sink Loop Ultimate Heat Sink Level Eeat Removal by the Containment Fan Coolers Boric Acid Charging Flow Range O to 110% design flow 2 0 to 110% design flow'0 to 110% design flow 1 Top to bottom Top to bottom Closed-not closed 0 to 110% design flow 1 32 0 F to 350 0 F 32 0 F to 200*F 0 to 110% design flow 1 0 to 110% design flow 1 30°F to 150 0 F Plant specific Plant specific 0 to 110% design flow 1 T ; ;I;o -D D D D D D D D D D D D D B B For indication of system operation.

For indication of system operation.

For indication of system operation.

To determine the amount of water dis-charged by the ECCS. This provides in-dication of the nature of the accident, indication of the performance of the ECCS, and indication of the necessity for operator action.To indicate whether the tanks have in-jected to the reactor coolant system.To indicate state of the isolation valves. (Per Regulatory Guide 1.47)For indication of system operation.

For indication of system operation.

For indication of system ope.ration For indication of system operation.

For indication of system operation.

For indication of system operation.

To ensure adequate water.source of cooling to indicate system operation To provide indication of reactor cooling and inventory control and maintain ade-quate concentration for shutdown margin.1.97-17.Type Purcose S TABLE 2 -PWR VARIABLES continued

-Measured Variable Ranqe I --_ _ -f I -. --~W41 0 AUXILIARY SYSTEMS CONTINUED:

Letdown Flow Sump Level in Spaces of Equipment Required for Safety RADWASTE SYSTEMS: High Level Radioactive Liquid Tank Level Radioactive Gas Hold-up Tank Pressure VENTILATION SYSTEMS: Emergency Ventilation Damper Position Temperature of Space in Vicinity of Equip-ment Required for Safety POWER SUPPLIES: Status of Class IE Power Supplies and Systems Status of Non-Class lE Power Supplies and Systems 0 to 110% design flowl To corresponding level of safety equipment failure Top to bottom 0 to 150% of design pressure 2 Open-closed status 30 0 F to 180°F Voltages and currents Voltages and currents D D E D D D K For indication of reactor coolant inven-tory control and boron concentration control.To monitor environmental conditions of equipment in closed spaces.Available volume to store primary coolant-Available capacity to store waste gases.To ensure proper ventilation under accident conditions.

To monitor environmental conditions of equipment in closed spaces.To ensure an adequate source power for safety systems.of electric It indicate an adequate source of elec-tric power.1.97-18 Tvop Plirmnen TABLE 2 -PWR VARIABLES continued

-Measured Variable RADIATION EXPOSURE RATES INSIDE BUILDINGS OR AREAS WHERE ACCESS IS REQUIRED TO SERVICE SAFET7 RELATED EQUIPMENT Radiation Exposure Rates Ranqe 10-1 to 104 R/hr for photons (permanently install-ed monitors)AIRBORNE RADIOACTIVE MAT.ERIALS RELEASED FROM THE PLANT: Effluent Radioactiv-ity -Noble Gases-Containment-Secondary Contain-ment-Auxiliary Building including building containing primary system gases, eg.waste gas decay tank.Other Release Points (including fuel handling area if separage from auxiliary building Effluent Radioactiv-ity -High Range Radiohalogens and Particulates-Untreated Effluents.HEPA Filters, min-imum of 2" of TEDA impregnated char-coal, non-ESF sys-tems.HEPA Filters, min-imuni of 4" of TEDA impregnated char-coal, ESF systems (Normal plus accident range for noble gas)-7 to 105 .Ci/cc Xe-133 calibration 10-7 to 104 11Ci/cc Xe-133 calibration 10-7 to 103 uCi/cc 10-7 to 102 vICi/cc (permanently install-ed monitors)10-3 to 102 4Ci/cc'0-3 to 10 .Ci/cc 10-3 to 1 .Ci/cc (permanently install-ed monitors)I I T v o- e I ma -P For measurement of high-range radiation exposure rates at various locations.

ANS-4.5 Section 6.2.6 To provide operator with information regarding release of radioactive noble gases on a continuous basis.To provide the operator with information regarding release of radioactive halogens and particulates.

Continuous collection of representative samples followed by monitoring (measurements) of samples for radiohalogens and for particulates.

1. 97-19..Tvoe Piirnmca TABLE 2 -PWR VARIABLES con*ued -Measured Variable I _ _ __ _ __I _ _ _ ,, A- I
  • u I uz e AIRBORNE RADIOACTIVE MAT-ERIALS RELEASED FROM THE PLANT CONTINUED:

Environs Radioactiv-ity -High Range Exposure Rate Environs Radioactiv-ity -Radiohalogens and Particulates AIRBORNE RADIOACTIVE MATERIALS RELEASES FROM THE PLANT CONTINUED:

Plant and Environs Radioactivity (portable instruments lO3 to 102 R/hr (60 keV to 3 MeV)(permanently install-ed monitors)10-9 to 10-3 4Ci/cc for both radiohalogens and particulates (permanently install-ed monitors)Normal Range 0.1 to 104 mR/hr photons 10-9 to O14 4C4/cc particulates 10-9 to 10-4 UCi/cc iodine High Range 0.1 to 104 R/hr photo-as 0.1 to 104 rads/hr betas and low energy photons lO-channel gamra-ray spectrometer E For estimating release rates of radio-active materials released during an accident from unidentified release paths (not covered by effluent monitors)

-continuous readout capability, approxi-mately 16 to 20 locations

-site de-pendent.For estimating releases rates of radio active materials released during an accident from unidentified release oaths (not covered by effluent monitors).

Continuous collection of representative samples followed by monitoring (measure-ments) of the samples. (Approximately 16 to 20 locations)

During and following an accident, to mc-.itor radiation and airborne radioactivi concentrations in many areas throughout the facility where is impractical to install stationary monitors capable of covering both normal and accident level: During and following an accident to rap-idly scope the composition or ga-a-emitting sources.1.97-20 I Tvn0a Rance* oe TABLE 2 -PWR VARIABLES contoed -Measured Variable POST-ACCIDENT SAMPLING CAPABILITY:

Primary Coolant Sumps Containment Air POST-ACCIDENT ANALYSIS CAPABILITY (ONSITE): ifETEOROLOGY:

Wind Direction Wind Speed Vertical Temperature Difference Precipitation I I- -j 'Al IJS.JQ, I -As required based on Reg Guide 1.4 guide-lines 1.2.3.4.S.gamma-ray spectrum pH hydrogen oxygen boron 0 to 360° (+/-5' accur-acy with a deflection of 15G. Starting speed 0.45 mps (1 mph)0 to 30 mps (67 mph)(*0.22 mps (0.5 mph)accuracy for wind spee less that 11 mps (25 m ph), with a starting threshold of less than 0.45 mps (1 mph)-90F to +9 0 F accuracy per intervals (+/-0.3 0 F 164 foot Recording rain gage with range sufficient to assure accuracy of total accumulation within iO% of record-ed value -0.01" resolution ZWA E E I Provide means for safe and convenient sampling.

These provisions should include: 1. shielding to .maintain radiation doses ALARA, 2. sample containers with container-sampling port connector comnatibili

'3. capability of sampling under primary system pressure and negative pressur 4. handling and transport capability, a: 5. pre-arrangement for analysis and interpretation.

For determining affluent transport direc-tion for emergency planning, dose assess-ment, and source estimates.

For determining effluent travel speed anc dilution for emergency planning,, doses assessments and source estimates.

For determining effluent diffusion rates for emergency planning, dose assessments and source estimates.

For determining effluent transport and ground deposition for emergency planning.Notes for Table 2 -(1) Design flow -the maximum flow anticipated in normal operation.

(2) Design pressure -that value corresponding to AS1LE code values which are obtained at or below code allowable material design stress values.1. 97-21 Range Tvaho pi 1on ,

TABLE 3 -BWR VARIABLES Measured Variable CORE: Control Rod Position Neutron Flux REACTOR COOLANT SYSTEM: RCS Pressure Coolant Level in the Reactor Main Steamline Flow Main Steamline Isola-tion Valves' Leakage Control System Press-ure Primary System Safety Relief Valve Posi-tions including ADS or Flow Through or Pressure in Valve Lines Radiation Level in Coolant Range I -. i Full in in or not full 1 c/s to 1% power (at least one fission counter)15 psia to 2000 psig Bottom of core support plate to above top of discharge plenum 0 to 120% design flow 1 0 to 15" of water 0 to 5 psid Closed-not closed or 0 to 30 psig 10 pCi/g D B B,C B B B B,D to 10 Ci/g C Provide positive indication that the control rods are fully inserted.(Minimum of 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br /> after accident)ANS-4.5, Section 6.2.2 For indication of approach to criticality ANS-4.5, Sections 6.2.3, 6.2.4, 6.3.3 and 6.3.5 For indication of an accident and to in-dicate that actions must be taken to mitigate an event.ANS-4.5, Section 6.2.3 For indication of fuel submergency for a LOCA event.To provide an indication of the integrity of the pressure boundary.To provide an indication of the pressure boundary and containment integrity.

By these measurements the operator knows if there is a path open for loss of cool-ant and that an event may be in progress.ANS-4.5, Section 6.3.2 For early indication of fuel cladding failure and estimate of extent of damage.1.97-22 0.Ty pe Puirnnos

TABLE 3 -BWR VARIABLES continued

-Measured Variable CONTAINMENT:

Primary Containment Pressure Containment and Dry-well Hydrogen Concentration Containment Isolation Valve Position£Suppression Pool Water Level Suppression Pool Water Temperature Drywell Pressure Drywell Drain Sumps Level (Identified and Unidentified Leakage)High Range Contain-ment Area Radiation Range 10 psia pressure to 3 times design press-ure 2 for concrete; 4 times design pressure for steel 0 to 10%(capability of oper-ating from 12 psia to maximum design press-ure 2 Closed-not closed Top of vent to top of weir well 50 0 F to 250 0 F 12 psia to 3 psig o to 110% design pressure Bottom to top 1 to 107 R/hr (60 keV to 3 MeV pho-tons with +/-20% acc-uracy for photons of 0.1 to 3 MeV)[ 10'R/hr for photons is approximately equiva-lent to 108 rads/hr for betas and photons]T -Ir--o BC B,C B,D B 3 B E B,C B,C ANS-4.5, Sections 6.2.5, 6.3.3, 6.3.4, and 6.3.5 For indication of the intergrity of the primary containment pressure boundary;to indicate the potential for leakage from the containment.

ANS-4.5, Sections 6.2.5, and 6.3.5 For indication of the need for, and a measurement of the performance of the containment hydrogen recombiner and to verify the operation of the mixing system ANS-4.5, Section 6.2.5 To indicate the status of containment isolation and to provide information on the status of valves in process lines which could carry radioactive materials out of containment.

ANS-4.5, Section 6.3.3 To assure proper temperature~for NPSH of ECCS. To verity the operation of the makup system.ANS-4.5. Section 6.3.3 Diagnosis of impact of accident on dr7-well structure.

ANS-4.5, Section 6.3.3 To help identify if an accident has de-graded beyond calculated values and in-dicate its magnitude and to determine action to protect the public.1.97-23 Type Purnosp TABLE 3 -8WR VARIABLES contin 9 d -Measured Variable I Range POWER CONVERSION SYSTEMS Main Feedwater Flow Condensate Storage Tank Level AUXILIARY SYSTEMS: Containment Spray Flow Steam Flow to RCIC RCIC Flow RHR System Flow RHR Heat Exchanger Outlet Temperature Service Cooling Water Temperature Service Cooling Water Flow Flow in UHS Loop Temperature in Ulti-mate Heat Sink Loop Ultimate Heat Sink Level -SLCS Storage Tank Level Sump Level in Spaces of Equipment Required for Safety O to 110% design flow 1 Bottom to top O to i10% design flow 1 O to 110% design flowl 0 to 0 to 32 0 F 110% design flow 1 110% design flow 1 to 350 0 F 32 0 F to 200 0 F O to 0 to 30 0 F Tvoe v tI E E D 110% design flow 1 110% design flow 1 to 150 0 F Plant specific Bottom to top To corresponding level of safety equipment failure To indicate an adequate source of water to the reactor.To indicate available water for core cooling.For indication of system operation.

To verify that adequate steam is avail-able for the system to perform its function.For indication of system operation.

For indication of system operation.

For indication of system operation.

For indication of system For For For indication indication indication of of of system sys tem system operation.

o ai operation.

operation.

operation.

To ensure adequate source of cooling water.To provide indication of inventory fcr boron injection for shutdown.To monitor potential for failure of equipment in closed spaces due to flooding.1.97-24 Piironca TABLE 3 -BWR VARIABLES co nued -Measured Variable RADWASTE SYSTEMS: High Radioactivity Liquid Tank Level Charcoal Delay Gas System Gas Flow or Radioactivity Level VENTILATION SYSTEMS: Emergency Ventilatioi Damper Position Temperature of in Vicinity of pment Required Safety Space Equi-for POWER SUPPLIES: Status of Class lE Power Supplies and Systems Status of Non-Class lE Power Supplies and Systems RADIATION EXPOSURE RATES INSIDE BUILDINGS OR AREAS WHERE ACCESS IS REQUIRED TO SERVICE SAFETY RELATED EQUIP-MENT: Radiation Zxposure Rates Range; --d __I -_ _ _ .I I I I Top to bottom As required Open-closed status 30 0 F to 130 0 F Voltages and currents Voltages and currents 101- to 10 R/hr for photons (permanently install-ed monitors)Available volume to store primarv coolant.To monitor performance of system.To ensure proper ventilation under accident conditions.

To monitor environmental conditions of equipment in closed spaces.To ensure an adequate source power for safety systems of electric To indicate an adequage source of electric power.For measurement of high-range radiation exposure rates 2a various locations.

1.97-25 Type Piurnnca TABLE 3 -BWR VARIABLES coriued -Measured Variable AIRBORNE RADIOACTIVE MATERIALS RELEASES FROM THE PLANT: Effluent Radioactiv-ity -Noble Gases.Containment Exhaust Vent and St andby Gas Treatment Sys-tem Vent-Other Release Points [including fuel handling bui-lding, auxiliary building, and tur-bine building]Effluent Radioactiv-ity -High Range Radiohalogens and Particulates.Untreated EffluentE.HEPA Filters, min-imum of 2" *of TEDA impregnated char-coal, non-ESF sys-tems.HEPA Filters, min-imum of 4" of TEDAi impregnated char-coal, ESF systems Environs Radioactiv-ity -High Range Exposure Rate Environs Radioactiv-ity -Radiohalogens and Particulates Range (Normal plus accident range for noble gas)10-7 to 105 llCi/cc Xe-133 calibration l0-7 to Xe-133 102 PCi/cc calibration (permanently install-ed monitors)10-3 to 102 lCi/cc 10-3 to 10 vCi/cc 10-3 to 1 PCi/cc (permanently install-ed monitors)10-3 to 102 R/hr (60 keV to 3 MeV)(permanently install-ed monitors)10-9 to 10-3 Ci/cc for both radiohalogens and particulates (permanently install-ed monitors)Type E E Pu ro as e ANS-4.5, Section 6.2.6 To provide operator with information re-garding release of radioactive noble gases on a continuous basis.To provide the operator with information regarding release of radioactive halogens and particulates.

Continuous collection of representative samples followed by monitoring (measurements) of samples for radiohalogens and for particulates.

For estimating release rates of radio-active materials released during an accident from unidentified release paths (not covered by effluent monitors)

-continuous readout capability, approxi-mately 16 to 20 locations

-site de-pendent.For estimating releases rates of radio-active materials released during an accident from unidentified release paths (not covered by effluent monitors).

Continuous collection of representative samples followed by monitoring (measure-ments) of the samples. (Approxi ately 16 to 20 locations)

1. 97-26 Puroose TABLE 3 -BWR VARIABLES co ued -Measured Variable AIRBORNE RADIOACTIVE MATERIALS RELEASES FROM1 THE PLANT CONTINUED:

Plant and Environs Radioactivity (portable instruments POST-ACCIDENT SAMPLING CAPABILITY:

Primary Coolant Suppression Pool Containment Air POST-ACCIDENT ANALYSIS CAPABILITY (ONSITE): METEOROLOGY:

Wind Direction Wind Speed Range Normal Ranae 0.1 to 10mR/hr photons 10-9 to 10-4 11Ci/cc particulates 10-9 to 10-4 4Ci/cc iodine High Range 0.1 to 104 R/hr photons 0.1 to 104 rads/hr betas and low energy photons 100-channel gamma-ray spectrometer As required based on Reg Guide 1.3 guide-lines 1.-2 .3 .4.gamma-ray spectrum pH hydrogen oxygen 0 to 360° (+/-50 accur-acy with a deflection of 150. Starting speed 0.45 mps (1 mph)0 to 30 mps (67 mph)(+/-0.22 mps (0.5 mph)accuracy for wind speeI less that 11 mps (25 m on), with a starting threshold of less than 0.45 mps (1 mph)Type E N/A N/A E E S Pu ro Os e During and following an accident, to mon-itor radiation and airborne radioactivity concentrations in many areas throughout the facility where is impractical to install stationary monitors capable of covering both normal and accident levels.During and following an accident to rap-idly scope the composition of gamma-emitting sources.Provide.means for safe and convenient sampling.

These provisions should include: 1. shielding to maintain radiation doses ALARA, 2. sample containers with container-sampling port connector compatibility.

3. capability of sampling under primary system pressure and negative pressure 4. handling and transport capability, ark 5. pre-arrangement for analysis and interpretation.

For determining affluent transport direc-tion for emergency planning, dose assess-ment, and source estimates.

For determining effluent travel speed and dilution for emergency planning,, doses assessments and source estimates.

1.97-27 Puroose TABLE 3 -8WR VARIABLES cifinued -Measured Variable MEETEOROLOGY CONTINUED:

Vertical Temperature Difference Precipitation Range 0 I__ _ _ _ _ __ -I -I WI U CZ I-9*F to +9 0 F (tO.307 accuracy per 164 foot intervals Recording rain gage with range sufficient to assure accuracy of total accumulation within 1O% of record-ed value -0.01" resolution E For determining effluent diffusion rates for emergency planning, dose assessment C and source estimates.

For determining effluent transport and ground deposition for emergency planning Notes for Table 3 -(1) Design flow -the maximum flow anticipated in normal operation.(z) Design pressure -that value corresponding to ASM code values which are obtained at or below code allowable material design scress values.1. 97-28 IT/Os of1'M en ft 0 0 ANS-4. 5 Draft 3 September, DRAFT CAUTION NOTICE: This Standard is being prepared or reviewed and has not been approved by ANS. It is subject to revision or withdrawal before issue.DRAFT American National Standard FUNCTIONAL REQUIRE1ENTS FOR POST ACCIDENT MONITORING CAPABILITY FOR THE CONTROL ROOM OPERATOR OF A NUCLEAR POWER GENERATING STATION Assigned Correspondent

-T. F. Timmons Westinghouse Electric Corporation Power Systems Company P.O. Box 355, MNC-410 Pittsburgh, PA 15230 1979 09 Writing Group ANS 4.5 Standards Committee NUPPSCO Secretariat ANS 0 0 TABLE OF CONTENTS FOREWORD 1.0 Introduction 2.0 Scope 3.0 Definition 4.0 Discussion 5.0 Design Basis 6.0 Design Criteria -Phase I and Phase II FOREWORD ANS 4 established Working Group 4.5 in late July 1979 to prepare a draft standard on Accident Monitoring Instrumentation which would complement other standards, but be broader in nature by including economic consid-erations.

Two primary objectives were 1) to address that instrumenta-tion which permits the operator to monitor expected parameter changes in the accident period, and 2) to address extended range instrumentation deemed appropriate for the possibility of encountering previously unforeseen events.ANS 4.5 began work on July 30th and met for 13 working days in a seven week period. In addition, a Design Criteria subgroup met for two days in this same period.As presented, this draft standard provides: 1. a list of functions to be performed (design basis section 5.0)2. a framework to determine those variables to be monitored (design basis section 5.0)3. an identification of three time periods of interest (definitions 3.0)4. an identification of four variable types (definitions 3.0)5. a delineation of applicable design criteria for the variables to be monitored (design criteria section 6.0)No identification of specific Type A monitored variables is provided in this standard.

Recommendations for Type 3 and Type C monitored vari-ables are provided in Section 6.0.i The significant issues in the development of this standard have been: 1. the scope of the document in terms of applicability to the control room operator or the plant operator (licensee).

The work group chose a control room operator scope.2. the pre-planned operator actions designated by the accident analyses in Chapter 15 of a plant's FSAR and the not previously planned operator action that may be required during unforeseen events. The Working Group established Type A instrumentation for the former, and Type B or C instrumentation for the latter.3. The monitoring of actual fission product barrier integrity and the potential for breach of a given barrier. The work group chose monitoring of actual breach for the fuel, reactor coolant system, and containment barrier, but only the potential breach of the con-tainment barrier.4. the degree of alignment of accident monitoring instrumentation with IEEE Class .E (ANS Class EC-3) and whether an intermediate class is needed between 1E and non-1E.5. whether a list of variables should be included as an appendix to the standard: a. a list of only Type C parameters

b. a list of Type A, 3, C and 0 parameters
6. the definition of instrument types 3 and 0 and whether these types should be included in the standard.The membership of the Working Group is as follows: L. Stanley, Chairman T. Timmons, Vice Chairman and Correspondent ii
0. Scmmers E. Wenzinger 0. Lambert R. Bauerle J. Castanes M. Wolpert H. Mumford X. Polanski E. Oowling Additional input has been provided to the Working Group by industry, university, and government participants throughout the meetings.

The Work Group is very appreciative of this assistance.

A iii 1.0 introduction The Code of Federal Regulations requires that instrumentation be provided to monitor variables and systems over their anticipated ranges for acci-dent conditions as appropriate to assure adequate safety. The purpose of this standard is to establish criteria for the selection of that instru-mentation.

These criteria are based on the sequence and duration of the phases through which an accident progresses.

The control room operator may have different information requirements for each phase of an accident.This standard presents criteria for monitoring the response of the plant to design basis events. It also presents criteria for monitoring the integrity of fission product barriers under conditions which have degraded beyond the design bases. This fission product barrier monitoring is con-sidered to be an extra set of instrumentation beyond that required for satisfactorily monitoring accident scenarios postulated in the plant safety analysis.Throughout these criteria, three verbs have been used to indicate the degree of rigor intended by the specific criterion.

The word "shall" is used to denote a requirement; the word "should" to denote a recommenda-tion; and the word "may" to denote permission, neither a requirement nor a recommendation.

1 2.0 SCOPE This standard contains criteria for determining the variables to be moni-tored by the control room operator, as required for safety, during the course of an accident and during the long-term stable shutdown phase fol-lowing the accident.

Also included are criteria for determining the requirements for the equipment used to monitor those variables.

The scope of the standard is limited to onsite environment and process monitoring.

Emergency preparedness planning is, or 'will be, covered by other standards.

2 3.0 OEFINITIONS Phase I That portion of the accident extending from the initiation of the accident to that point at which the plant is in a con-trolled condition.

Phase II That portion of the accident extending from the time at which the plant is in a controlled condition to that point at which personnel access to the location of the accident is possible.Phase III That portion of the accident extending from the time at which personnel access to the location of the accident is possible to the time at which the plant has returned to operating status or been decommissioned.

Type A Instruments

-Those instruments which provide the information required to permit the control room operator to take the pre-planned manual actions to accomplish safe plant shutdown for design basis accident events and to maintain long term plant-stability.

Type B Those instruments which provide to the control room operator information to monitor the process of accomplishing critical safety functions, i.e., reactivity control, core cooling, maintaining reactor coolant system integrity, maintaining containment integrity and radioactive effluent control.Type C Those instruments that indicate in the control room (1) the extent to which parameters, which have the potential for causing a breach of the final fission product barrier (i.e., the containment), have exceeded the design basis values, or (2) that a fission product barrier (i.e., fuel clad, reactor coolant pressure boundary or the containment) has been breached.3 Type 0 Those instruments which indicate to the control room operator the performance of individual safety systems.Design Basis Accident Events Those events postulated in the plant safety analyses, any one of which may occur during the lifetime of a particular plant, excluding those events which are expected to occur during a calendar year for a particular plant;and those events that are not expected to occur but are postulated in the plant safety analyses because their consequences would include the poten-tial for the release of significant amounts of radioactive material.4 4.0 DISCUSSION It is the philosophy of this Standard that instrumentation is required to monitor plant performance during and after an accident.

The purposes of the accident monitoring instrumentation are enumerated in Section 5.0, Design Basis. This Standard specifies the plant safety functions to be performed and the criteria to be used by the designer in selecting the variables to be monitored.

Certain concepts have been established to aid the system designer in the selection of variables to monitor the course of an accident and to arrive at appropriate design criteria for instruments to monitor these variables.

4.1 Planned Versus Unolanned Operator Actions The plant safety analysis defines the accident scenarios from which the safety system design bases and the planned or anticipated operator actions are derived. Accident monitoring instrumentation is provided to permit the operator to take required actions to address these analyzed.situations.

However, instrumentation must also be provided for unplanned situations, (i.e., to ensure that, should plant conditions evolve differently than predicted by the safety analysis, the operator has sufficient information to monitor the course of the event). Instru-mentation must also be provided to indicate to the operator if fission product barrier integrity has degraded beyond the prescribed limits of the Safety Analysis.4.2 Variable Types Four classifications of variables have been identified.

Operator manual actions during accidents included in the plant safety analysis are anticipated or pre-planned.

Those variables that provide information needed by the operator to perform these manual actions are designated 5

Type A. Those variables needed to assess that the plant safety functions are being accomplished, as identified in the plant safety analysis, are designated Type S. Variables used to monitor for the actual gross breach of one of the fission product barriers or the potential breach of the final fission product barrier (containment) are designated Type C. Type C variables used to monitor the potential breach of containment have an arbitrarily-determined, extended range. The fourth classification, Type D, consists of those variables monitored to ascertain that the safety systems are performing as designed.

Type 0 variables are less important than Types A, B and C for accident monitoring since safety system per-formance only infers safety function accomplishment.

Type 0 variables and instruments are not considered to be within the scope of Accident Monitoring Instrumentation.

Guidance on the selection of Type 0 vari-ables and the specification of appropriate design criteria are not given in this standard.

This guidance is provided in standards for design of safety systems (e.g. IEEE-603, ANSI N1S.2, etc). The four classifica-tions are not mutually exclusive in that a given variable (or instrument) may be included in one or more types. This differentiation by variable type is intended only to guide the designer in his selection of accident monitoring variables and applicable criteria.4.3 Accident Phases The typical accident sequence has been subdivided into three phases: Phase I covers the initial portion of the accident, Phase II covers the stable long-term cooling portion of the accident up to the time where personnel access is possible, and Phase III addresses the period follow-ing personnel access to the accident area. This sub-division has been made so that variable selection and design criteria application can reflect the differing conditions which characterize these three phases.For example, Phase I can be anticipated to be of relatively short dura-tion, having relatively severe plant conditions, and allowing no person-nel access to the accident area. Phase II is expected to be of longer duration, to require a significant number of operator actions, under milder plant conditions, but with still no personnel access to the acci-dent area. Phase III is expected to be of even longer duration where 6 personnel access is possible.

Oifferent design criteria are then appro-priate for each of the three phases. In this Standard, guidance and criteria are provided for Phases i and Ii.7 5.0 Oesign Basis The plant designer shall perform and document an analysis to select acci-dent monitoring instruments.

He shall identify instruments required by his design to enable the control room operator to: A. Perform pre-planned manual actions.B. Ascertain the performance of: (1) Reactivity control (2) Reactor core cooling (3) Reactor coolant system integrity (4) Containment integrity (5) Radioactive effluent control C. Ascertain the extent to which parameters, which have the potential for causing a breach of the containment, have exceeded the design basis values and to ascertain that a fission product barrier (i.e. fuel clad, reactor coolant system pressure boundary or the containment) has been breached.5.1 Variable Selection for Phases I and II The process for selection of the Accident'Monitoring Instrumentation vari-ables shall include: 5.1.1 For Type A 1) Identification of the postulated accidents for which manual action is required.2) Identification of planned operator actions 3) Identification of the monitored variables needed for planned operator actions.a 5.1.2 For Type B 1) identification of the monitored variables that provide the most direct indication needed to assess the accomplish-ments of: a. Reactivity Control b. Reactor Core Cooling c. Reactor Coolant System Integrity d. Containment Integrity e. Radioactive Effluent Control Guidance on the selection of these variables is provided in Section 6.0.5.1.3 For Type C 1) Identification of the monitored variables that provide the most direct indication of a gross breach of a fission product barrier or of an approach to breach of the con-taimment.

These instruments may have extended ranges.Guidance on the selection of these variables is provided in Section 6.0.5.1.4 Phase III Access Prior to the termination of Phase II, the ability to gain access to the location of the accident must be determined.

Instrumentation that indicates when conditions are acceptable for personnel access shall be identified.

5.2 PERFORMANCE REQUIREMENTS FOR PHASES I ANO I: The process for determining performance requirements of Accident Moni-toring Instrumentation shall include, as a minimum, the following con-siderations:

9 5.2.1 For Types A and 8 1) Identification of 2) Identification of 3) Identification of 4) Identification of ment is needed.5) Identification of ment must operate.the the the the expected range of the process variable.required accuracy of measurement.

required response characteristics.

time interval during which the measure-the local environment in which the instru-5.2.2 For Type C The performance requirements for these instruments are arbitrary.

Guidance on these requirements is provided in Section 6.0.10 6.0 DESIGN CRITERIA 6.1 GENERAL DESIGN CRITERIA 6.1.1 SEISMIC QUALIFICATIONS Accident monitoring instrumentation that is to be seismically qualified shall be qualified according to IEEE Standard 344-1975.

The instrumenta-tion shall be qualified to continue to function within the required accuracy following, but not necessarily during, a safe shutdown earth-quake. Vibration loads which occur as a result of plant system operation during any phase for which the instrument is required shall be considered.

6.1.2 DURATION Accident monitoring instrumentation shall be qualified for the length of time its function is required.

Unless other times can be justified, Phase II instrumentation shall be qualified to function for not less than 100 days. A shorter time may be acceptable if instrumentation equipment replacement or repair can be accomplished within an acceotable out-of-service time, taking into consideration the environment where the equip-ment is located.6.1.3 DIRECT MEASUREMENT To the extent practical, accident monitoring instrumentation inputs shall be from sensors that directly measure the desired variables.

6.1.4 MINIMIZING MEASUREMENTS To the extent practical, the same instruments shall be used for accident monitoring as are used for the normal operations of the plant to enable the operator to use, during an accident situation, instruments with which he is most familiar.

However, where the required range of accident moni-toring instrumentation results in a loss of instrumentation sensitivity in the normal operating rance, separate instruments shall be used.11 6.1.5 INSTALLATION Permanently installed instrument equipment is required for those instru-ments required to function during Phase I. Permanently installed instru-mentation systems need not be provided for those functions required only for Phases II and III providing it can be demonstrated that the instru-ment components can be installed when required, considering the local environment.

6.1.6 INSTRUMENTATION LOCATION AND IDENTIFICATION Accident monitoring instrumentation shall be located accessible to the operator and be distinguishable from other displays so that in an acci-dent situation, the operator can rapidly identify the accident monitoring instrumentation.

6.1.7 EQUIPMENT REPAIR, The accident monitoring instrumentation shall be designed to facilitate timely recognition, location, replacement, and repair or adjustment of malfunctioning equipment.

-6.1.8 TEST AND CALIBRATION 6.1.3.1 Test Capability shall be provided for testing, with a high degree of confi-dence, the operational availability of each instrument channel during plant operation.

This may be accomplished in various ways, for example: 1. By observing the effect of perturbing the monitored variable.2. By observing the effect of introducing and varying, as appropriate, a substitute inout to the sensor of the same nature as the measured variable.12

3. By cross-checking between channels that bear a known relationship to.each other.Where testing during reactor operation is not possible, it must be shown that there is no practical way of implementing such a requirement without adversely affecting plant safety or operability.

In addition, it must be shown that the probability of a failure of the component which is not periodically tested is acceptably low and that such testing can be rou-tinely performed when the reactor is shut down.6.1.8.2 Calibration Capability shall be provided for calibration of each instrument channel during normal plant operation or during shutdown as determined by the required interval between calibrations.

Equipment that does not require periodic calibration is exempt from this requirement.

5.1.9 DIVERSITY Diversity is preferred in fufilling redundancy requirements.

5.1.10 REDUNDANT READOUT AMBIGUITY Where a disagreement between redundant displays could lead the operator to defeat or fail to accomplish a required safety function, additional information shall be provided to allow the operator to deduce the actual conditions that are required for him to perform his role. This may be accomplished by providing an independent channel which monitors a dif-ferent variable bearing a known relationship to the redundant channel or by providing an additional independent channel of instrumentation of the same variable or by providing the capability for the operator to perturb the measured variable and determine by observation of the response which instrumentation display has failed.13

  • 0 6.2 TYPE B INSTRUMENTS 6.2.1 GENERAL REQUIREMENTS

-The number of instruments used shall be only that minimum set needed to adequately monitor the accomplishment of the following functions:

a. Reactivity Control b. Reactor Core Cooling c. Reactor Coolant System Integrity d. Containment Integrity e. Radioactive Effluent Control Type 3 instruments provide control room indication beyond that which may be required for any preplanned operator action and as such constitute an extra set of instrumentation which results in an additional layer of protection.

6.2.2 VARIABLES FOR REACTIVITY CONTROL MONITORING The measured variable shall indicate the accomplishment of control of reactivity in the core. The measured variable should be neutron flux.The range of measurement should extend from one count per second on the source range instrument to the intermediate range instrument value cor-responding to 1.5. of full reactor power. This range is intended to encompass all neutron flux levels at which the core can be subcritical.

6.2.3 VARIABLES FOR CORE COOLING MONITORING The measured variables shall indicate the accomplishment of core cool-ing. For the PWR, the measured variables should be TH, TC, pres-surizer level, and pressurizer pressure.

For the BWR, the measured variable should be reactor vessel water level. Incore thermocouple monitoring should be considered for inclusion as a desireable variable to ascertain cooling.14 6.2.4 VARIABLES FOR REACTOR COOLANT SYSTEM INTEGRITY The measured variable shall indicate the accomplishment of RCS inte-grity. The measured variable should be primary system pressure.6.2.5 VARIABLES FOR CONTAINMENT INTEGRITY The measured variables shall indicate the accomplishment of containment integrity.

The measured variables should be containment hydrogen con-centration, containment pressure and containment isolation valve posi-tions..6.2.6 VARIABLES FOR RADIOACTIVE EFFLUENT CONTROL The measured variables shall indicate the accomplishment of radioactive effluent control. The measured variables should be noble gas monitoring of the identified plant release points.6.3 TYPE C INSTRUMENTS 6.3.1 Type C instruments shall meet the following criteria: 5.3.1.1 The number of instruments used shall be only that minimum set needed to adequately monitor the three barriers;6.3.1.2- Each measurement shall be as direct as possible;6.3.1.3 Any chosen measurement shall detect a gross breach of one or more barriers (i.e., > 1 percent fuel clad failure, a RCS pressure boundary breach producing a loss of reactor coolant inventory in excess of the normal makeup capability, a con-tainment breach capable of producing radiation releases in excess of 10 CFR 100 at the site boundary using TID-14844 source terms); the ranges established for Type C instruments are not mechanistically related to a postulated accident scenario.15 6.3.1.4 During the period of need for Type C instruments, no other failures shall be assumed in the analysis beyond the assumed breach of a barrier coincident with loss of off-site power;0.3.2 Fuel Clad Barrier Monitoring 6.3.2.1 The measured variable shall detect and alarm the breach of the fuel clad barrier (i.e., > 1 percent fuel clad failure);6.3.2.2 Operator sampling of reactor coolant shall be used as the means to verify the measured variable alarm.6.3.2.3 The measured variable should be reactor coolant system radia-tion. The instrument range should be equivalent to the fuel clad gap activity corresponding to 0.5% to 5% failed fuel. A narrow accuracy band for this measured variable is not signi-ficant in achieving this function; for example, +50%, to +100%accuracy of reading should be acceptable.

instrument tran-sient response should be compatible with its recorder.5.3.3 Reactor Coolant System Pressure Boundary Monitoring 6.3.3.1 The measured variable(s) shall detect and alarm a breach of the reactor coolant system that produces a loss of coolant inventory in excess of normal makeup capability.

The spectrum of RCS pressure boundary breaches extends up to and includes the largest double-ended pipe break.0.3.3.2 The means used to detect RCS pressure boundary breach should include one RCS pressure boundary variable and one containment variable over the full spectrum of break sizes.6.3.3.3 The measured PWR variables should be RCS pressure and contain-ment pressure.

The instrument range should be the design pressure plus a specified margin (< 1O%). Normal instrument accuracy is acceptable for these monitors.

instrument tran-sient response should be compatible with its recorder.16 6.3.3.4 The measured BWR variables should be drywell pressure and containment sump level. The instrument range should be design values plus a specified margin (< 10%). Normal instrument accuracy is acceptable for these monitors.

Instrument tran-sient response should be compatible with its recorder.6.3.4 Containment Pressure Boundary Monitoring 6.3.4.1 The measured variable(s) shall detect and alarm a breach of the containment pressure boundary that is capable of producing radiation releases in excess of 10 CFR 100 at the site boundary using TID-14844 source terms.0.3.4.2 The means used to detect containment pressure boundary breach should include containment pressure (BWR and PWR), environs radiation monitoring for gross gamma (PWR), and secondary containment air space radiation monitoring for gross gamma (BWR).6.3.4.3 The instrument range for containment pressure should be design pressure plus a specified margin (< 10%). Normal instrument accuracy is acceptable for this monitor. Instrument transient response should be compatible with its recorder.6.3.4.4 The instrument range for environs radiation monitoring should be 10-3 to 102 R/hr. The instrument range for secondary containment air space radiation monitoring should correspond to the 10 CFR 100 value for off-site doses. Instrument accuracy should be + 1/2 decade (100 Kev-3 Mev). Instrument transient response should be compatible with its recorder.6.3.5 Potential Breach of the Final Fission Product Barrier 6.3.5.1 The measured variables should be containment pressure, con-tainment hydrogen concentration, and RCS pressure for indicating the potential for causing a breach of the final fission product barrier (i.e., containment).

17 0 0 5.3.5.2 An arbitrary range of 3 times design pressure for concrete and 4 times design pressure for steel should be used for contain-ment pressure.

Instrument accuracy should be + 10% of span.Instrument transient response should be compatible with its recorder.6.3.5.3 An arbitrary range of 0-10 volume percent hydrogen should be used for containment hydrogen concentration.

Instrument accuracy should be + 10% of span. Instrument transient response should be compatiable with its recorder.6.3.5.4 An arbitrary range of 1.5 times design pressure should be used for RCS pressure.

Instrument accuracy should be + 10% of span. Instrument transient response should be compatible with its recorder.6.3.6 INSTRUMENT QUALIFICATION 6.3.6.1 Type C instruments shall be qualified in the same manner as Type A instruments except: 6.3.5.1.1 For purposes of equipment qualification, the assumed maximum value of the monitored parameter shall be the value equal to the maximum range for the instrument.

The monitored parameter shall be assumed to approach this peak by extrapolating the most severe initial ramp associated with the Design Basis Accidents.

The decay for this parameter shall be considered proportional to the decay for this parameter associated with the Design Basis Accidents.

No additional qualification margin needs to be added to the extended range parameter.

See figure 6.3-1. All environmental envelopes except that per-taining to the parameter measured by the instrument shall be those associated with the Design Basis Accidents.

5.4 SPECIFIC DESIGN CRITERIA Design Criteria specific to particular accident phases and variable types are presented in Table 6.4-1.18 TABLE 6.4.1 DESIGN CRITERIA CRITERION l.. Qualify seismically to IEEE 344-75 (operate after SSE)2. Meet single failure per IEEE 379-77 3. Qualify environmen-tally to IEEE 323-74 4. Consider loss of off-site power 5. Power source, 6. Out of service interval-prior to accident 7. Otit of service inter-val -during accident PHASE 1 VARIABLE TYPE B A Yes Yes Yes Yes Yes Yes Yes Yes Emergency (2) .None Emerg.(2)None C No No A Yes Yes Yes(l)Yes Emerg.<72 fir(3)<2 hir Yes Yes Emerg.(2)(2)PHASE II VARIABLE TYPE B No Yes Yes No Normal(6)(2)(2)C No No Yes U )No Normal (6).<72 fIrs 3)<2 hIrs 0 0 TABLE 6.4-1 (Continued)

DESIGLN CRITERIA P11ASE 1 VARIABLE TYPE CRITERION A B 8. Portable instrumenta-No No t iol 9. Level of quality ANSI N45.2 ANSI t assurance 10. Display type(4) Continuous Contif 11. Display method Recording(5)

Record 12. Identification as Yes Yes accident monitoring type 13. Periodic Test per Yes Yes IEEE-338-1977 NOTES: (1) See Paragraph 6.3.6 of this Standard.(2) IEEE 279-1971 Paragraph 4.11 Exemuption C No(7)445.2 luou s di ng A Yes ANSI N45.2 Continuous Indicator Yes Yes ANSI N45.2 Continuous Recording(5)

Yes Yes PHASE I I VARIABLE TYPE B Yes ANSI N45.2 Continuous Indicator Yes Yes C Yes ANSI N45.2 On demand Indicator Yes Yes I NOTES TO TABLE 6.4-1 (Continued) 3? Based on normal tech spec requirements on out-of-service safety systems.4 Continuous indication or recording displays a given variable at all times; intermittent indication or recording displays a given variable periodically; on demand indication or recording displays a given variable only when requested.

(5) Where trend or transient information is essential to planned operator actions.(6) May be manually connected to emergency buss (7) Radiation monitoring outside containment may be portable.-4 Figure 6.3-1.Typical Environmental Qualification Envelope for Type C Instruments e- --t I I I i I I I I I k7 Assumied Parameter Environment

---3,rDesiqn Basis Accident Timee.Parameter 0 4