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ELSEVIER www.elsevier.com/locate/pnucene Progress in Nuclear Energy, Vol. 44, No. 3, pp. 191-213, 2004 Available online at www.sciencedirect.com © 2004 Elsevier Ltd. All rights reserved Printed in Great Britain sc,~.cE D,.ECV" 0149-1970/$ - see front matter doi: 10.1016/j.pnucene.2003.12.001 FUZZY FMEA APPLIED TO PWR CHEMICAL AND VOLUME CONTROL SYSTEM Antonio C6sar Ferreira Guimar~es* and Celso Marcelo Franklin Lapa a Instituto de Engenharia Nuclear (IEN-CNEN) - Divis~o de Reatores / Programa de P6s-Gradua@o, Ilha do Fund~o s/n, Rio de Janeiro, Brazil, Zip Code: 21945-970, Po. Box: 68550 E-mail: *[email protected] or l [email protected] ABSTRACT In this paper, a fuzzy inference system (FIS) modeling technique is introduced to treat a nuclear reliability engineering problem. This method uses the concept of a pure fuzzy logic system where the fuzzy rule base consists of a collection of fuzzy IF-THEN rules. The fuzzy inference engine uses these fuzzy IF-THEN rules to determine a mapping of the input universe of discourse over the output universe of discourse based on fuzzy logic principles. The risk priority number (RPN) (typical of a traditional Failure Mode & Effects Analysis - FMEA) is calculated and compared to fuzzy risk priority number (FRPN), obtained by the use of the scores from expert opinion. These scores are opinions about probabilities of Occurrence, Severity and not Detection of a failure of the studied system. The Chemical and Volume Control System was adopt as practical example in the study of case. The results demonstrated the potential of the inference system to this problem clas s . © 2004 Elsevier Ltd. All rights reserved. Keywords: Expert Opinion, FMEA, Fuzzy Logic, CVCS 191
Transcript
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ELSEVIER www.elsevier.com/locate/pnucene

Progress in Nuclear Energy, Vol. 44, No. 3, pp. 191-213, 2004

Available online at www.sciencedirect.com © 2004 Elsevier Ltd. All r ights reserved Printed in Great Britain

sc ,~ . cE D , .ECV" 0149-1970/$ - see front matter

doi: 10.1016/j.pnucene.2003.12.001

FUZZY FMEA APPLIED TO PWR CHEMICAL AND VOLUME CONTROL SYSTEM

Antonio C6sar Ferreira Guimar~es* and Celso Marcelo Franklin Lapa a

Instituto de Engenharia Nuclear (IEN-CNEN) - Divis~o de Reatores / Programa de P6s-Gradua@o, Ilha do Fund~o s/n, Rio de Janeiro, Brazil, Zip Code: 21945-970, Po. Box: 68550

E-mail: *[email protected] or l [email protected]

ABSTRACT

In this paper, a fuzzy inference system (FIS) modeling technique is introduced to treat a nuclear reliability engineering problem. This method uses the concept of a pure fuzzy logic system where the fuzzy rule base consists of a collection of fuzzy IF-THEN rules. The fuzzy inference engine uses these fuzzy IF-THEN rules to determine a mapping of the input universe of discourse over the output universe of discourse based on fuzzy logic principles. The risk priority number (RPN) (typical of a traditional Failure Mode & Effects Analysis - FMEA) is calculated and compared to fuzzy risk priority number (FRPN), obtained by the use of the scores from expert opinion. These scores are opinions about probabilities of Occurrence, Severity and not Detection of a failure of the studied system. The Chemical and Volume Control System was adopt as practical example in the study of case. The results demonstrated the potential of the inference system to this problem clas s . © 2004 Elsevier Ltd. All rights reserved.

Keywords: Expert Opinion, FMEA, Fuzzy Logic, CVCS

191

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192 A. C. F. Guimar~es and C. M. F. Lapa

1. INTRODUCTION

In recent study, the effect of aging on the Chemical and Volume Control System (CVCS) of a pressurized water reactor (PWR) has been evaluated (Grove and Travis, 1995). Since the CVCS provides many normal and emergency operating functions, it is important to understand the effect of aging in order to detect and correct these instances prior to component failures. A detailed review of the Nuclear Plant Reliability Data System (NPRDS) and Licensing Events Report (LER) databases for the 1988-1991 time period, together with a review of industry and NRC experience and research, indicate that age-related degradations and failures have occurred. These failures had significant effects on plant operation, including reactivity excursions, and pressurizer level transients. The majority of these component failures resulted in leakage of reactor coolant outside the containment.

Grove and Travis (1995) visited a representative plant of PWR design Westinghouse to obtain specific information on system inspection, surveillance, monitoring, and inspection practices. The results of these visits indicate that adequate system maintenance and inspection is being performed. In some instances, the frequencies of inspection were increased in response to repeated failure events. Also, a parametric study was performed to assess the effect of system aging on Core Damage Frequency (CDF). This study showed that as MOV operating failures increased, the contribution of the High Pressure Injection to CDF also increased. Failure mode and effects analysis (FMEA) is an important technique (Stamatis, 1995) that is used to identify and eliminate known or potential failures to enhance reliability and safety of complex systems and is intended to provide information for making risk management decisions. A modified failure mode and effects analysi s (FMEA) and knowledge base system (KBS) are proposed here to estimate the risk using scores from experts. Fuzzy logic systems (Zadeh, 1987) is a name for the systems which have relationship with fuzzy concepts (like fuzzy sets, linguistic variables, and so on) and fuzzy logic. The most popular fuzzy logic systems in the literature may be classified into three types: pure fuzzy logic systems, Takagi and Sugeno's fuzzy system, and fuzzy logic systems with fuzzifier and defuzzifier (Wang, 1993). The methodology used in this paper was the fuzzy logic systems with fuzzifier and defuzzifier, as used in the most investigations e.g. Pillay and Wang (2003), Xu et al. (2002) and Guimarfies (2003).

The knowledge-based fuzzy systems allows for descriptive or qualitative representation of expressions such as "remote" or "high", incorporate symbolic statements that are more natural and intuitive than mathematical equation. A direct method with one expert (Klir and Yuan, 1995) was used to aggregate opinion of individual expert.

This work investigates the potential application of knowledge-based fuzzy systems in a case study. The Chemical Volumetric Control System (CVCS) was chosen for this study.

2. DESCRIPTION OF CHEMICAL VOLUME CONTROL SYSTEM (CVCS)

A simplified CVCS system schematic is shown in Figure 1. The primary sub-systems included in this study are:

• letdown cooling system, • demineralizers, • boron thermal regeneration,

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Fuzzy FMEA 193

• volume control storage tank, • boric acid supply, • charging pumps, and • Reactor Coolant Pump (RCP) seal water injection

Most of the components are located outside of containment, so aging degradations may result in external leakage of the reactor coolant. To fully understand the effect of system aging, specific information on the system's operating characteristics, material and design function is presented in the next description.

COMPONENT COOLING

~ , ~ WATER SYSTEM REGENEF~TIVE ''~.."~,~ " I

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Figure 1 - Chemical and volume control system.

The Chemical and Volume Control System (CVCS) for Pressurized Water Reactor (PWR) Westinghouse plant provides both normal and emergency operation functions. During normal operation, the three primary functions are to purify the reactor coolant, control reactor coolant system (RCS) inventory (pressurizer level control), and provide the reactor coolant pump (RCP) seal water injection. During an emergency, the primary functions for the majority of PWR plants are to provide high-pressure safety injection, RCP seal injection, and emergency boration. In addition, the containment isolation system, which includes CVCS valves, isolates the letdown and charging lines.

The typical system design used in the majority of plants is shown schematically in Figure 2. More detail about description of CVCS system can be found in Grove and Travis (1995).

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194 A. C. E Guimar6es and C. M. F. Lapa

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3. DESCRIPTION OF FUZZY INFERENCE SYSTEM APPROACH

The "pure fuzzy logic system" is the system where the fuzzy rule base consists of a collection of fuzzy IF-THEN rules, and the fuzzy inference engine uses these fuzzy IF-THEN rules to determine a mapping from fuzzy sets in the input universe of discourse U C R " to fuzzy sets in, the output universe of discourse V C R based on fuzz3; logic principles. ~rhe fuzzy IF-THEN rules are of the following form:

R ~0 • IF xl is Fll and ... x , is F%

T H E N y is G l (1)

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Fuzzy FMEA 195

where Fli and G t are fuzzy sets, x = (xl,. ..... , Xn) T ~ U and y ~ V are input and output linguistic variables, respectively, and l = 1,2, .. . , M. Practice has shown that these fuzzy IF-THEN rules provide a convenient framework to incorporate human experts' knowledge. Each fuzzy IF-THEN rule (Eq. 1) defines fuzzy set F~ x ... xF ln ~ G 1 in the product space U x V. In order to use the "pure fuzzy logic system" in engineering systems where inputs and outputs are real-valued variables. The most straightforward way is to add a fuzzifier to the input and a defuzzifier to the output of the pure fuzzy logic system. The fuzzifier maps crisp points in U to fuzzy sets in U, and the defuzzifier maps fuzzy sets in V to crisp points in V. The fuzzy rule base and fuzzy inference engine are the same as those in the pure fuzzy logic system. In the literature, this fuzzy logic system is often called the fuzzy logic controller since it has been mainly used as a controller. It was first proposed by Mamdani and Assilian (1974), and has been successfully applied to a variety of industrial process and consumer products. A detailed description of this fuzzy logic system can be found in Wang (1993).

4. APPLICATION OF THE PROPOSED APPROACH TO CVCS

Initially, an "expert" with knowledge domain on the analyzed system was adopted. The selected specialist belongs to the reliability engineering and can participate in other domains. A traditional FMEA using the risk priority number (RPN) ranking system is carried out in the first moment. Mathematically, RPN is represented as:

R P N = O x S x D (2)

where, "O" represents the probability of occurrence, "S" represents the severity of the failure and "D" represents the probability of not detecting of the failure. The values for O, S, and D are obtained by using the values scaled presented in Table 1 (Xu et al., 2002 and Pillay and Wang, 2003). The expert in the FMEA analysis was the same as in the proposed.

Table 1 - Traditional FMEA scales for RPN.

Occurrence (O)

Severity (S)

Not Detection (D)

Rating Possible failure rate (operating days) Probability Range (%)

Remote 1 < 1:20,000 0-5/6-15

Low 2 / 3 1:20,000/1:10,000 16-25/26-35

Moderate 4 / 5 / 6 1:2000/1:1000/1:200 36-45/46-55/56-65

High 7 / 8 1:100/1:20 66-75/76-85

Very High 9 / 10 1:10/1:2 86-100

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196 A. C. F. Guirnaraes and C. M. F. Lapa

As presented in Figure 2, the primary functions of the CVCS are letdown, purification, boration and chemical addition, boron regeneration, charging, RCP seal injection and safety injection. The system consists of the mechanical components (pumps, valves, heat exchangers, volume control tanks, and de!onizers), instrumentation, and controls, necessary to perform these functions.

A Failure Modes and Effects Analysis (FMEA) was performed to determine the effects of failure of the major system components. Each FMEA included the following items: (a) Failure Mode: the basic manner(s) which a component may fail or cease to perform as design. The failure modes for these components were consistent with those used in industry reliability; (b) Failure Cause: the particular type of degradation mechanisms, which may cause the component to failure (stresses); (c) Failure Effects: the effects on the CVCS system due to the component failure; (d) Detection Methods: functional indicators or system and plant operating characteristics, which would alert the operator of component degradation and/or failure.

An important system function in many PWR plants is to provide High Pressure Injection under certain accident conditions. Since this function was previously evaluated (Meyer, 1989), it was not included in these FMEAs. However, it is important to recognize that many of the CVCS components that provide reactor charging are used for High Pressure Injection. Aging degradation and failures of these components, which result from normal plant operation, will also affect their ability to provide high-pressure injection. It is essential that system aging be understood, and detected, before it results in the inability of the system to perform its safety-related function.

The FMEA analysis for Chemical Volumetric Control System (CVCS) is summarized in Appendix 01. Grove and Travis (1995) developed the FMEA and the "expert" the numbers for O, S and D.

4.1 - Fuzzy membership function

Making use of the toolbox simulator of Matlab (2000), the expert was invited to define each membership function and the values in the universe of discourse using the interpretations of the linguistic terms described in Table 2 (Pillay and Wang, 2003). The expert chose the triangular membership function (a, b, c). After that, the following question may be answered by the expert: "Which elements x (a,b,c) have the degree of membership ~ a = zero, ab = one and ~tc= zero". Direct methods with one expert (Klir and Yuan, 1995) were used. The five linguistic terms describing the input are Remote (R), Low (L), Moderate (M), High (H) and Very High (VH), and for output are lowly (LL), Low (L), Fairly Low (FL), Moderate (M), Fairly high (FH) and High (H). The membership functions of the five linguistic terms to input are shown in the Figure 3. The six membership functions for output in Figure 4. The graphical representation of membership function to occurrence, severity and not detection are identical and only one, occurrence was shown.

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198 AI C. E Guimar6es and C. M. F. Lapa

4.2 - Fuzzy rule base application

Since there are three factors, occurrence, severity and not detection, and five linguistic terms describing each factor, the total number of rules is 125. The total number of rules in the fuzzy rules base is reduced to 14 rules for this system analyzed with extensive FMEA after some simplifications to reduce the numbers of rules of the fuzzy rule base. These rules can estimate the results and are presented

1. If (Occurrence is M) and (Severity is VH) and (Not detection is VH) then (Risk is H) (1)

2. If (Occurrence is M) and (Severity is H) and (Not detection is M) then (Risk is H) (1)

32 If (Occurrence is M) and (Severity is M) and (Not detection is M) then (Risk is FL) (1)

4. If (Occurrence is L) and (Severity is VH) and (Not detection is M) then (Risk is FL) (1)

5. If (Occurrence is L) and (Severity is H) and (Not detection is H) then (Risk is FL) (1)

6. If (Occurrence is M) and (Severity is M) and (Not detection is L) then (Risk is L) (1)

7. If (Occurrence is M) and (Severity is H) and (Not detection is L) then (Risk is L) (1)

8. If (Occurrence is L) and (Severity is M) and (Not detection is M) then (Risk is L) (1)

9. If (Occurrence is L) and (Severity is M) and ~Not detection is M) then (Risk is FL) (1)

10. If (Occurrence as L) and (Severity is R) and (Not detection is L) then (Risk is LL) (1)

11. If (Occurrence as L) and (Severity is L) and (Not detection is L) then (Risk is LL) (1)

12. If (Occurrence as L) and (Severity is M) and (Not detection is L) then (Risk is L) (1)

13. If (Occurrence as R) and (Severity is M) and (Not detection is M) then (Risk is LL) (1)

14. If (Occurrence is R) and (Severity is VH) and (Not detection is M) then (Risk is FL) (1)

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Fuzzy FMEA

Table 2 - Interpretations of the linguistic terms for developing the fuzzy rule system.

iiiiiii!iiiiiiii!iiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiii•iiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiii•iii

to be observed

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than once

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performance, the

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cause slight

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operator, but that

cause no deterioration

to the system

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cause a high degree

of operator

dissatisfaction or that

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undetected until the

system performance

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completed.

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reduced.

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undetected until system

performance is affected

1 9 9

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200 A. C. F. Guimaraes and C. M. E Lapa

iHigh:: : : I Near certain to occur at I A failure that causes

............ least once s;on~f;cant I ' ~ r : ! : i i i r

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carried out

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seriously affect the

ability to complete

the task or cause

damage, serious

injury or death

Failure remains

undetected; such a

defect would almost

certainly be detected

during inspection or test.

5. RESULTS

In the Table 3 are presented the results for RPN and fuzzy approach. "ID" is component event, RPN and Fuzzy are the risk numbers and Rankingrpn and Ranking_fuzzy are the ranking of RPN and fuzzy methodology, respectively. For example, the components 33, 52, 53, 54, 66, 68, and 69 produce a result of 144 for RPN method and the same Rank_rpn of value 12. Fuzzy approach produces for component 66 the highest risk priority number followed of events 33, 52 and 53 and the lowest risk priority number for events 33, 52 and 53. For events 9, 10, 11 and 12, the defuzzified ranking is 2 and the four events should be given the same fuzzy risk priority number 5. The RPN method, produces a result of 45, 75, 60 and 100 for events 9, 10, 11 and 12, respectively. This means that event 12 has the highest priority followed by event 12, 10 and 9, respectively. High level of uncertainty in the safety analysis data could be representing a problem.

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Fuzzy FMEA 203

6. CONCLUSION

In this paper a new approach was proposed using the "Fuzzy Inference System" (FIS) applied to estimate "Fuzzy Risk Priority Number" (FRPN) using the expert opinion for quantify linguistic variables. This article introduces in the nuclear area a capable methodology to subsidize new reactor projects through of the fuzzy identification of critical systems and components and possible failure modes.

Another important contribution of this approach to nuclear area is propitiate the building of a linguistic knowledge bases for studies of extension of residual life in aging components. Is important to mention that, the population of commercial nuclear power plants has matured and its principal safety and operational components are under aging process. By the year 2014, forty-eight of the wide world plants will have been operating for forty years (design life expectance).

In this paper, to exemplify the methodology, the extensive Failure Mode & Effects Analysis (FMEA) of Chemical and Volume Control System (CVCS) was used as nuclear power plant application. This was a simple and complete example, where a reduced number of rules in the knowledge base ware necessary to mapping all analysis situations.

According to Table 3, different ranking are obtained using the fuzzy approach proposed in a case of the same value of RPN but with different values assigned for occurrence, severity and not detection. The risk implication may be very different (Bem-Daya and Raouf, 1993 and Gilchrist, 1993). The advantages of the proposed fuzzy rule base for application to FMEA of CVCS can be summarized as follows:

• This fuzzy approach combines (i) expert knowledge and experience for use in an FMEA study,

and (ii) can be used for systems where safety data is unavailable or unreliable.

Converting the scale of RPN traditional in (i) variable linguistic with values defined as input by expert is the great situation and (ii) not force precision and use the system by people without knowledge about interpretations of these linguistic terms. Permitting to use the fuzzy system in a simple way.

ff some change is made in part of system component or sub-component of system analyzed as result of FMEA study, new ranking results after improvements can be obtained so quickly using the "Fuzzy Inference System" (FIS).

In accordance with Grove and Travis (1995) the results of this NPAR (Nuclear Plant Aging Research program) study show that aging degradation and failures has occurred in the CVCS. These failures have not prevented the system from responding as designed in an emergency, but have resulted in normal plant operation perturbations. These occurrences have resulted in unnecessary actuation and operation of other system components in response, cause unnecessary stresses. The results of the plant visits indicate that significant attention is being concentrated on the CVCS, and that maintenance practices are being employed in response to specific component failure histories. However, the larger number of failure events reported to the databases (NPRDS and LER),

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204 A. C. E Guimaraes and C. M. F. Lapa

indicating that: system failures are still occurring, highlights the need for continued attention to the Operation and aging of the system.

Future work for risk is the "control system" that can be developed with "Simulink" using FIS and the factor values; occurrence, severity and not detection, where recommendations are used for control factors values.

REFERENCES

Ben-Daya M. and Raouf A. (1993), A Revised Failure Mode and Effects Analysis Model. Int. Journal Quality Reliability Mgmt. v.3 (1), pp. 43 - 47.

Gilchrist W. (1993), Modeling Failure Modes and Effects Analysis. Int. Journal Quality Reliability Mgmt, v.10(5), pp. 11 - 23.

Grove E. J. and Travis, R. J. (1995), Effect of Aging on the PWR Chemical and Volume Control System, NUREG/CR - 5954, BNL - NUREG - 52410, June.

Guimar~es A C. F. (2003), A New Methodology for the Study of FAC Phenomenon Based on a Fuzzy Rule System, Annals of Nuclear Energy, v. 30/7, pp. 853 - 864.

Klir G.J. and Yuan B. (1995), Fuzzy Sets and Fuzzy logic: Theory and Application. New Jersey: Prentice Hall.

Mamdani E.H. and Assilian S. (1975), An Experiment in Linguistic Synthesis with a Fuzzy Logic Controller. International Journal of Man-Machine Studies, v.7, No. 1, pp. 1 - 13.

MatLab 6 (2000), Users Guide of the Fuzzy Logic Toolbox.

Meyer L.C. (1989), Nuclear Plant Aging Research on High Pressure Injection Systems, NUREG/CR-4967. August.

l

Pillay A. and Wang J. (2003), Modified Failure Mode and Effects Analysis Using Approximate Reasoning. Reliability Engineering and System Safety. v.79, pp. 69 - 85.

Page 15: Zip Code: 21945-970, Po. Box: 68550 E-mail: *tony@ien.gov ...read.pudn.com/downloads190/ebook/896218/Fuzzy FMEA... · reliability engineering problem. This method uses the concept

Fuzzy FMEA 205

Stamatis D. H. (1995), Failure Mode and Effects Analysis - FMEA from Theory to Execution. New York; ASQC Quality Press.

Xu K., Tang L. C., Xie M., Ho S. L. and Zhu M. L. (2002), Fuzzy Assessment of FMEA for Engine Systems. Reliability Engineering and System Safety. v.75, pp.17- 29.

Wang Li-Xin (1993). Adaptive Fuzzy Systems And Control - Design And Stability Analysis, University of California at Berkeley. PTR Prentice Hall.

Zadeh L. A. (1987), Fuzzy Sets and Applications: Selected Papers. New York: Wiley.

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App

endi

x 01

- C

VC

S Fa

ilure

Mod

e an

d E

ffec

t Ana

lysi

s (F

ME

A)

ID

1,2

Com

pone

nt

Fai

lure

mod

e F

ailu

re C

ause

s F

ailu

re E

ffec

t

1. F

ails

Ope

n M

echa

nica

l Bin

ding

L

etdo

wfi

Flo

w C

ontr

ol

Val

ves

3,4,

5,6

Reg

ener

ativ

e H

eat

Exc

hang

er

7,8

Ori

fice

Iso

latio

n V

alve

s

9,10

11,1

2

13,

14,

15,

2. F

ails

Clo

se

3. P

lugg

ed T

ubes

4. I

nsuf

fici

ent

heat

tr

ansf

er

5. E

xter

nal

leak

age

6. T

ube

Lea

kage

7. F

ails

Ope

n

8. F

ails

Clo

sed

Los

s o

f ai

r or

ele

ctri

cal

pow

er. S

puri

ous

sign

al.

Cor

rosi

on p

rodu

ct

build

up. B

orn

Bui

ldup

. F

orei

gn m

ater

ial

in R

CS.

S

cale

bui

ldup

on

tube

s.

Cas

ing

crac

k. V

ent v

alve

se

at le

akag

e.

Cor

rosi

on.

Man

ufac

turi

ng.

Mec

hani

cal B

indi

ng

Los

s of

redu

ndan

cy.

Una

ble

to te

rmin

ate

letd

own

flow

.

Los

s of

redu

ndan

cy.

Los

s o

f no

rmal

let

dow

n fl

ow

path

thro

ugh

rege

nera

tive

heat

exc

hang

er.

Red

uced

let

dow

n fl

ow.

Tem

pera

ture

of l

etdo

wn

flow

may

exc

eed

desi

gn

limits

, re

sulti

ng i

n po

ssib

le

dam

age

to d

owns

trea

m

com

pone

nts.

R

educ

ed le

tdow

n fl

oe.

Prim

ary

cool

ant r

elea

se.

No

effe

ct

Los

s of

redu

ndan

cy.

Los

s o

f no

rmal

let

dow

n fl

ow

path

. L

oss

of a

ir o

r el

ectr

ical

B

lock

age

of fl

ow to

VC

T.

pow

er.

Spur

ious

sig

nal

Con

tain

men

t Is

olat

ion

9. F

ails

Ope

n M

echa

nica

l Bin

ding

V

alve

10. F

ails

Clo

sed

Los

s o

f ai

r or

ele

ctri

cal

pow

er. S

puri

ous

sign

al

Los

s of

redu

ndan

cy.

Deg

rade

d co

ntai

nmen

t is

olat

ion.

L

oss

of re

dund

ancy

. L

oss

of n

orm

al l

etdo

wn

flow

pa

th.

Let

dow

n li

ne r

elie

f 11

. Fai

ls O

pen

Set

poin

t dri

ft.

• Pr

imar

y co

olan

t di

scha

rged

va

lve

Mec

hani

cal

failu

re,

to p

ress

uriz

er r

elie

f tan

k.

12. F

ails

Clo

sed

Set

poin

t dri

ft.

Los

s o

f ov

erpr

essu

re

Mec

hani

cal

failu

re,

prot

ectio

n.

13. P

lugg

ed T

ubes

R

educ

ed l

etdo

wn

flow

N

on-r

egen

erat

ive

heat

ex

chan

ger

Cor

rosi

on p

rodu

ct

build

up.

Bor

on b

uild

up.

For

eign

mat

eria

l in

RC

S.

Fai

lure

Det

ecti

on

Met

hods

R

emot

e va

lve

posi

tion

in

dica

tion.

Dow

nstr

eam

fl

ow a

nd t

empe

ratu

re

indi

cato

rs.

Rem

ote

valv

e po

siti

on

indi

catio

n. L

etdo

wn

flow

an

d pr

essu

re in

dica

tors

.

Flo

w in

dica

tor

Reg

ener

ativ

e he

at

exch

ange

r out

let

tem

pera

ture

ind

icat

ors.

Exc

essi

ve m

akeu

p fl

ow

rate

. C

onta

inm

ent

radi

atio

n m

onit

ors

Rem

ote

valv

e po

siti

on

indi

cato

r. L

etdo

wn

flow

an

d pr

essu

re in

dica

tors

. R

emot

e va

lve

posi

tion

in

dica

tor.

Let

dow

n fl

ow

and

pres

sure

indi

cato

rs.

Rem

ote

valv

e po

siti

on

indi

cato

r. A

ppen

dix

J L

eak

test

ing.

R

emot

e va

lve

posi

tion

in

dica

tor.

Let

dow

n fl

ow

and

pres

sure

indi

cato

rs.

Exc

essi

ve u

se o

f m

akeu

p w

ater

. D

owns

trea

m lo

w

flow

and

pre

ssur

e A

SM

E S

ecti

on X

I te

stin

g.

Dow

nstr

eam

flow

and

pr

essu

re in

dica

tors

.

Not

es

Val

ves

are

desi

gned

to

fail

clos

ed u

pon

loss

of

pow

er (o

r ai

r su

pply

)

Sam

e.

Val

ves

desi

gned

to fa

il cl

osed

upo

n lo

ss o

f po

wer

(or

air

supp

ly)

O 3 5

D 5 8

4 5

3

3 4

5

3 4

5

3 8

7

10

10

3 5

3

5 5

3

3 5

4

5 5

4

4 9

3

t~

O E.

Page 17: Zip Code: 21945-970, Po. Box: 68550 E-mail: *tony@ien.gov ...read.pudn.com/downloads190/ebook/896218/Fuzzy FMEA... · reliability engineering problem. This method uses the concept

ID

16

17,

18,

19

20,2

1

227

23,

24

I Com

pone

nt

Fai

lure

mod

e F

ailu

re C

ause

s F

ailu

re E

ffec

t F

ailu

re D

etec

tion

N

otes

M

etho

ds

Scal

e bu

ildup

on

tube

.

Pres

sure

Con

trol

Val

ve

3 W

ay T

empe

ratu

re

cont

rol

Val

ve

Dem

iner

aliz

ers

14. I

nsuf

fici

ent

Hea

t T

rans

fer.

15. T

ube

Lea

k.

16. E

xter

nal

leak

age

17. F

ails

Ope

n

18. F

ails

Clo

sed

19. F

ails

to O

pen

prop

erly

20.

Fai

ls o

pen

for

flow

on

ly to

VC

T.

21.

Fails

ope

n fo

r fl

ow

only

to d

emin

eral

izer

s.

22. I

neff

ecti

ve io

n or

bo

ron

rem

oval

23. P

lugg

ed

24.

Ext

erna

l L

eaka

ge

Cor

rosi

on.

Man

ufac

turi

ng

defe

ct.

Cas

ing

crac

k. V

ent v

alve

se

at le

akag

e.

Val

ve o

pera

tor

mal

func

tion.

Mec

hani

cal

bind

ing.

L

oss

of

air

or e

lect

rica

l po

wer

. Spu

riou

s si

gnal

.

Val

ve o

pera

tor

mal

func

tion.

Mec

hani

cal

bind

ing.

Val

ve o

pera

tor

mal

func

tion.

Mec

hani

cal

failu

re.

Val

ve o

pera

tor

mal

func

tion.

Mec

hani

cal

failu

re.

Deg

rade

resi

n. I

ncor

rect

re

sin.

Part

icul

ate

cont

amin

atio

n

Cra

cked

ves

sel.

C

orro

sion

. M

anuf

actu

ring

def

ect.

Hig

h ex

it te

mpe

ratu

re m

ay

exce

ed d

esig

n lim

its,

resu

lting

in

dow

nstr

eam

co

mpo

nent

dam

age.

C

onta

min

atio

n o

f C

CW

co

olin

g w

ater

.

Red

uced

letd

own

flow

. [ P

rim

ary

cool

ant

rele

ase.

L

oss

of

redu

ndan

cy.

Los

s of

pre

ssur

e. C

ontr

ol .t

o ] p

reve

nt s

team

flas

hing

. L

oss

of

redu

ndan

cy.

Los

s of

letd

own

flow

. Pos

sibl

e I R

CS

over

pres

suri

zatio

n.

Pres

sure

inc

reas

e in

non

- re

gene

rativ

e he

at

exch

ange

r. R

educ

ed

letd

own

flow

. O

peni

ng o

f do

wns

trea

m re

lief

val

ve.

Pos

sibl

e R

CS

ov

erpr

essu

riza

tion.

L

etdo

wn

prev

ents

from

fl

owin

g to

dem

iner

aliz

ers.

[ F

issi

on p

rodu

ct b

uild

up.

Con

tinuo

us l

etdo

wn

flow

to

dem

iner

aliz

ers.

Pos

sibl

e da

mag

e to

dem

iner

aliz

ers

] due

to

high

RC

S

tem

pera

ture

Pr

imar

y co

olan

t fi

ssio

n pr

oduc

t and

bor

on b

uild

up.

Dec

reas

ed le

tdow

n fl

ow

Prim

ary

cool

ant r

elea

se

outs

ide

of

cont

ainm

ent

Hea

t ex

chan

ger o

utle

t fl

ow te

mpe

ratu

re

indi

cato

r.

CC

W r

adia

tion

mon

itor.

E

xces

s us

e o

f m

akeu

p w

ater

. CC

W s

urge

tan

k le

vel

incr

ease

. L

ow f

low

in

dica

tion

Exc

essi

ve m

akeu

p fl

ow

rate

P

ress

ure

indi

catio

n al

arm

0

ow

pre

ssur

e, h

igh

tem

pera

ture

) R

emot

e pr

essu

re a

nd

flow

indi

cato

rs.

Rem

ote

valv

e po

siti

on in

dica

tor.

P

ress

ure

indi

catio

n al

arm

.

Rem

ote

valv

e po

sitio

n in

dica

tor.

Rem

ote

valv

e po

sitio

n in

dica

tor.

Pro

cess

radi

atio

n m

onito

r. P

roce

ss

sam

plin

g.

Dem

iner

aliz

er

diff

eren

tial

pres

sure

in

crea

se

Loc

al le

ak a

nd ra

diat

ion

mon

itor

s.

10

--..O

Page 18: Zip Code: 21945-970, Po. Box: 68550 E-mail: *tony@ien.gov ...read.pudn.com/downloads190/ebook/896218/Fuzzy FMEA... · reliability engineering problem. This method uses the concept

ID

Com

pone

nt

25,

VC

T le

vel D

iver

t 26

V

alve

27

Vol

ume

Con

trol

Tan

k

28,

VC

T R

elie

f Val

ve

29

30,

Che

mic

al A

ddit

ion

31

Con

trol

Val

ve

32,

VC

T D

egas

sifi

er V

alve

33

34,

VC

T v

olum

e C

ontr

ol

35

Val

ve

36

Bor

ic A

cid

Tan

ks

Fai

lure

mod

e F

ailu

re C

ause

s F

ailu

re E

ffec

t F

ailu

re D

etec

tion

N

otes

M

etho

ds

25.

Fails

Ope

n to

byp

ass

Val

ve o

pera

tor

Dec

reas

e in

VC

T le

vel.

VC

T le

vel

indi

cato

r.

posi

tion

m

alfu

nctio

n. S

puri

ous

Unp

lann

ed re

leas

e o

f R

emot

e va

lve

posi

tion

si

gnal

, pr

imar

y co

olan

t to

hold

up

indi

catio

n.

tank

s.

26. F

ails

ope

n to

VC

T

Val

ve o

pera

tor

Una

ble

to b

ypas

s.V

CT

for

VC

T le

vel i

ndic

ator

. m

alfu

nctio

n. M

echa

nica

l ad

ditio

nal

cool

ant

Rem

ote

valv

e po

siti

on

failu

re,

trea

tmen

t, in

dic

atio

n.

27.

Ext

erna

l L

eaka

ge

Rel

ease

of p

rim

ary

cool

ant

I VC

T le

vel

indi

catio

n.

outs

ide

of

cont

ainm

ent.

28. F

ails

to O

pen

29. F

ails

Clo

sed

30. F

ails

to O

pen

31. F

ails

Clo

sed

32. F

ails

Ope

n

33. F

ails

Clo

sed

Cor

rosi

on.

Man

ufac

turi

ng d

efec

t. S

etpo

int D

rift

. M

echa

nica

l fa

ilure

.

Setp

oint

Dri

ft.

Mec

hani

cal

failu

re.

Mec

hani

cal

bind

ing.

V

alve

ope

rato

r m

alfu

nctio

n.

Los

s o

f ai

r su

pplie

s.

Spur

ious

sig

nal.

Mec

hani

cal

bind

ing.

V

alve

ope

rato

r m

alfu

nctio

n.

Los

s o

f ai

r su

pplie

s.

Spur

ious

sig

nal.

VC

T li

quid

ven

ted

to

nucl

ear

drai

n sy

stem

. L

oss

of

VC

T c

onte

nts.

D

egra

ded

syst

em

oper

atio

n.

Ove

rpre

ssur

izat

ion

of

VC

T.

Ove

rpre

ssur

izat

ion

of

VC

T

wit

h H

ydro

gen

or

Nitr

ogen

. L

oss

of

Hyd

roge

n an

d N

itro

gen

flow

to V

CT

re

sult

ing

in R

CS

fiss

ion

prod

uct i

ncre

ase.

L

oss

of

over

pres

suri

zatio

n o

f V

CT

Los

s o

f ven

ting

VC

T g

as

mix

ture

to b

oron

recy

cles

de

gass

ifie

r.

VC

T le

vel

decr

ease

. ] H

oldu

p ta

nk le

vel

incr

ease

.

I VC

T p

ress

ure

indi

cato

r

VC

T p

ress

ure

indi

cato

r

VC

T p

ress

ure

indi

cato

r an

d lo

w p

ress

ure

alar

m.

VC

T p

ress

ure

indi

cato

r

VC

T p

ress

ure

indi

cato

r an

d re

mot

e hi

gh-p

ress

ure

alar

m.

34. F

ails

Ope

n M

echa

nica

l bi

ndin

g.

Hig

h pr

imar

y m

akeu

p fl

ow

Low

bor

on

Val

ve o

pera

tor

tO V

CT

. P

ossi

ble

RC

S co

ncen

trat

ion.

Hig

h fl

ow

mal

func

tion,

de

bora

tion

an

d V

CT

leve

l in

dica

tors

. ! 3

5. F

ails

Clo

sed

Sha

ft b

indi

ng.

Val

ve

Low

pri

mar

y m

akeu

p fl

ow

Hig

h bo

ron

oper

ator

mal

func

tion,

to

VC

T.

Pos

sibl

e R

CS

conc

entr

atio

n. L

ow f

low

de

bora

tion,

in

dica

tion

s to

VC

T.

36. E

xter

nal

Lea

kage

C

orro

sion

. L

oss

of

all,

or p

artia

l, T

ank

leve

l m

onit

ors

Man

ufac

turi

ng d

efec

t, vo

lum

e o

f ta

nks.

Los

s of

bo

ric

acid

sup

ply

to V

CT

an

d R

CS

0 3

10

8 10

D 5

to

Page 19: Zip Code: 21945-970, Po. Box: 68550 E-mail: *tony@ien.gov ...read.pudn.com/downloads190/ebook/896218/Fuzzy FMEA... · reliability engineering problem. This method uses the concept

ID

37,

38,

39

Com

pone

nt

Fai

lure

mod

e F

ailu

re C

ause

s F

ailu

re E

ffec

t F

ailu

re D

etec

tion

N

otes

M

etho

ds

Bor

ic A

cid

Tra

nsfe

r 37

. Fai

ls to

Ope

rate

Sh

aft

shea

r. S

haft

L

oss

of

boro

n ad

ditio

n L

ow f

low

and

pre

ssur

e Pu

mp

seiz

ure.

Mot

or fa

ilure

, ca

pabi

lity.

Los

s o

f al

arm

s fr

om p

ump.

Bor

ic

Ele

ctri

cal

failu

re.

Los

s o

f re

dund

ancy

. B

oric

Aci

d A

cid

Tan

k le

vel

Hea

d.

crys

talli

zatio

n. F

ailu

re o

f in

dica

tors

. B

oric

Aci

d T

ank

heat

ers.

38

. Sp

urio

us S

tart

P

ossi

ble

exce

ssiv

e bo

ron

Pum

p di

scha

rge

pres

sure

ad

ditio

n,

and

flow

indi

cato

rs.

40

Che

mic

al M

ixin

g T

ank

41,

Bor

ic A

cid

Ble

nder

42

F

low

Con

trol

Val

ve

43,

Bor

ic A

cid

Ble

nder

44

O

utle

t F

low

Con

trol

V

alve

45,

46

39. F

alls

to p

rodu

ce

desi

gn o

utpu

t

40. E

xter

nal

Lea

k

41. F

ails

Ope

n

42. F

ails

Clo

sed

43.

Fai

ls O

pen

Spur

ious

ele

ctri

cal

sign

al.

Bor

on c

ryst

alliz

atio

n.

Failu

re o

f pi

ping

hea

t tr

ace.

C

orro

sion

. M

anuf

actu

ring

def

ect.

Mec

hani

cal

bind

ing.

V

alve

ope

rato

r fa

ilure

Los

s of

air

sup

plie

s.

Spur

ious

sig

nal.

Mec

hani

cal

bind

ing.

V

alve

ope

rato

r fai

lure

Los

s of

bor

on a

dditi

on

capa

bilit

y.

Che

mic

al s

olut

ion

spill

. R

educ

ed c

hem

ical

add

ition

ca

pabi

lity

Una

ble

to p

rovi

de re

quir

ed

wat

er m

akeu

p vo

lum

e re

quir

ed f

or n

orm

al p

lant

op

erat

ion.

U

nabl

e to

pro

vide

wat

er

mak

eup

requ

ired

for

no

rmal

pla

nt o

pera

tion.

U

nabl

e to

pro

vide

requ

ired

co

ncen

trat

ion

of b

oric

aci

d to

RC

S w

hen

atta

inin

g a

hot s

hutd

own.

Pum

p fl

ow a

nd d

isch

arge

pr

essu

re in

dica

tors

. R

CS

bo

ron

leve

l sa

mpl

ing.

R

CS

che

mic

al s

ampl

ing.

T

ank

leve

l ind

icat

ors.

Val

ve p

osit

ion

indi

catio

n. M

akeu

p w

ater

fl

ow in

dica

tor.

Val

ve p

osit

ion

indi

catio

n. M

akeu

p w

ater

fl

ow in

dica

tor.

V

alve

pos

itio

n in

dica

tor.

B

oric

aci

d fl

ow re

cord

er.

44. F

aiis

Clo

sed

Los

s of

air

sup

plie

s.

Una

ble

to p

rovi

de

Val

ve p

osit

ion

indi

cato

r.

Spur

ious

sig

nal,

conc

entr

atio

n bo

ric

acid

B

oric

aci

d fl

ow re

cord

er.

solu

tion

dur

ing

hot

shut

dow

n.

VC

T O

utle

t C

ontr

ol

45.

Fai

ls O

pen

Mec

hani

cal

bind

ing.

G

as b

indi

ng o

f ch

argi

ng

Val

ve p

osit

ion

indi

cato

r V

alve

V

alve

ope

rato

r fa

ilure

pu

mps

. H

ydro

gen

inje

ctio

n in

to R

CS.

46

. Fai

ls C

lose

d L

oss

of p

ower

, Spu

riou

s V

alve

pos

itio

n in

dica

tor.

si

gnal

. V

CT

leve

l in

dica

tor.

M

echa

nica

l bi

ndin

g.

47. F

ails

Ope

n 47

, E

mer

genc

y B

orat

ion

48

Val

ves

Los

s o

f fl

uid

flow

fro

m

VC

T t

o ch

argi

ng p

umps

. U

nabl

e to

iso

late

flo

w

from

bor

ic a

cid

tran

sfer

pu

mps

. Ove

r-bo

ratio

n of

R

CS.

Val

ve p

osit

ion

indi

cato

r.

Bor

ic a

cid

tank

lev

el

indi

cato

r.

48. F

ails

Clo

sed

Shaf

t bi

ndin

g. V

alve

U

nabl

e to

pro

vide

V

alve

pos

itio

n in

dica

tor.

op

erat

or m

alfu

nctio

n,

emer

genc

y bo

ratio

n.

Bor

ic a

cid

tank

lev

el

indi

cato

r.

Not

sto

rage

tan

k.

Che

mic

al s

olut

ion

mad

e an

d ad

ded

to R

CS

as

need

ed.

O

3 5 3

D 8

t,q

to

Page 20: Zip Code: 21945-970, Po. Box: 68550 E-mail: *tony@ien.gov ...read.pudn.com/downloads190/ebook/896218/Fuzzy FMEA... · reliability engineering problem. This method uses the concept

iD

49,

Cha

rgin

g P

umps

50

, I (

Cen

trif

ugal

and

51

po

siti

ve d

ispl

acem

ent

pum

ps)

Com

pone

nt

Fai

lure

mod

e F

ailu

re C

ause

s

52,

Cha

rgin

g P

umps

53

, i O

utle

t Che

ck V

alve

s 54

49. F

ailu

re to

ope

rate

co

ntin

uous

ly.

Sha

ft s

hear

. Sha

ft

seiz

ure.

Mot

or fa

ilure

.

55,

Cha

rgin

g Pu

mp

Flow

56

C

ontr

ol V

alve

57,5

8 C

harg

ing

Flow

.

Isol

atio

n V

alve

50. D

egra

ded

Ope

rati

on

51. S

puri

ous

Star

t.

52. F

ails

to o

pen

53. F

ails

to o

pen

full

y.

54. F

ails

to c

lose

.

55. F

ails

Ope

n.

56. F

ails

Clo

sed.

57. F

ails

Ope

n.

Los

s of

pow

er.

Los

s of

su

ctio

n he

ad.

Bor

on c

ryst

alli

zati

on.

Spur

ious

Sta

rt.

Bro

ken

inte

rnal

s.

Fati

gue.

Vib

rati

on.

Bro

ken

inte

rnal

s. R

CS

debr

is.

Bro

ken

inte

rnal

s.

Fati

gue.

Vib

rati

on. R

CS

debr

is.

Mec

hani

cal B

indi

ng.

Los

s of

air

or

elec

tric

al

pow

er.

Spur

ious

sig

nal.

Mec

hani

cal b

indi

ng.

Fai

lure

Eff

ect

Fai

lure

Det

ecti

on

Not

es

Met

hods

L

oss

of re

dund

ancy

. U

nabl

e to

pro

vide

cha

rgin

g fl

ow u

nder

nor

mal

op

erat

ing

cond

itio

ns (3

pu

mps

fai

l)

Los

s of

redu

ndan

cy.

Una

ble

to p

rovi

de p

rope

r ch

argi

ng fl

ow in

res

pons

e to

ope

rati

ons.

Los

s of

RC

P se

al w

ater

of

cool

ing.

Po

ssib

le e

xces

sive

RC

S ch

argi

ng fl

ow.

Los

s of

red

unda

ncy.

Fa

ilur

e to

pro

vide

des

ired

ou

tput

cha

rgin

g fl

ow a

nd

RC

P s

eal c

ooli

ng fl

ow.

Los

s of

red

unda

ncy.

F

ailu

re to

pro

vide

ful

l flo

w

for

char

ging

and

RC

S co

olin

g B

ackf

low

to p

ump.

Una

ble

to p

rovi

de d

esig

n fl

ow.

Una

ble

to a

utom

atic

ally

ad

just

cha

rgin

g fl

ow

thro

ugh

cont

rol o

f pr

essu

rize

r wat

er le

vel,

char

ging

flow

, an

d R

CP

seal

flo

w.

Una

ble

to a

utom

atic

ally

ad

just

cha

rgin

g fl

ow

thro

ugh

cont

rol o

f pr

essu

rize

r wat

er le

vel,

char

ging

flow

, an

d R

CP

seal

flo

w.

Nor

mal

bor

atio

n fl

ow p

ath

unav

aila

ble.

L

oss

of r

edun

danc

y in

pr

ovid

ing

isol

atio

n of

ch

argi

ng li

ne d

urin

g ac

cide

nt c

ondi

tion

s.

Pum

p ou

tlet

flow

and

pr

essu

re in

stru

men

tati

on.

Cir

cuit

bre

aker

- m

onit

orin

g li

ght.

Pum

p ou

tlet

flow

and

pr

essu

re in

stru

men

tati

on.

Pum

p ou

tlet

flo

w a

nd

pres

sure

ins

trum

enta

tion

. C

ircu

it b

reak

er

mon

itor

ing

ligh

ts.

Cha

rgin

g pu

mps

out

put

flow

and

pre

ssur

e in

dica

tion

.

Cha

rgin

g pu

mps

out

put

flow

and

pre

ssur

e in

dica

tor.

Pum

p op

erat

ing

in

reve

rse.

Cha

rgin

g w

ater

flo

w

indi

cato

r.

Low

cha

rgin

g fl

ow

indi

catio

n.

Rem

ote

valv

e po

siti

on

indi

cati

on,

Onl

y no

rmal

ope

rati

on o

f ch

argi

ng p

umps

is

cons

ider

ed. H

igh-

pr

essu

re in

ject

ion

not

incl

uded

in th

is s

tudy

. S

ame

Sam

e

Val

ve n

orm

ally

full

op

en.

Mot

or o

pera

tor

ener

gize

d up

on

gene

rati

on o

f sa

fety

]i

njec

tion

O 5

D 6

tO

O

Page 21: Zip Code: 21945-970, Po. Box: 68550 E-mail: *tony@ien.gov ...read.pudn.com/downloads190/ebook/896218/Fuzzy FMEA... · reliability engineering problem. This method uses the concept

ID

59,6

0

61,6

2

63,6

4

65,6

6

67,6

8

Com

pon

ent

Fai

lure

mod

e F

ailu

re C

ause

s F

ailu

re E

ffec

t F

ailu

re D

etec

tion

N

otes

M

eth

ods

58.

Fai

ls C

lose

d.

Sam

e.

RC

P s

eal

wat

er f

low

co

ntro

l va

lve

59. F

ails

Ope

n

Los

s of

ele

ctri

cal

pow

er.

Spu

riou

s si

gnal

.

Mec

hani

cal

bind

ing.

L

oss

of a

ir o

r el

ectr

ical

po

wer

.

Los

s of

nor

mal

cha

rgin

g fl

ow p

ath

flow

bor

atio

n,

dilu

tion

and

coo

lant

m

akeu

p. L

oss

of c

ooli

ng

flow

to

rege

nera

tive

hea

t ex

chan

ger.

Una

ble

to p

rovi

de m

anua

l ad

just

men

t of

RC

P s

eal

wat

er f

low

.

Rem

ote

valv

e po

siti

on

indi

cato

r. L

etdo

wn

tem

pera

ture

flo

w

indi

cato

r. C

harg

ing

wat

er

flow

and

tem

pera

ture

in

dica

tion

VC

T l

evel

in

dica

tion

. R

CP

sea

l w

ater

flo

w

pres

sure

indi

cati

on.

Val

ve d

esig

ned

to f

ail

open

on

loss

of

air

or

elec

tric

al p

ower

to

ensu

re f

low

to

num

ber

1 R

CP

sea

ls.

60.

Fai

ls C

lose

d -

Spu

riou

s si

gnal

. U

nabl

e to

pro

vide

man

ual

RC

P s

eal

wat

er f

low

S

ame.

ad

just

men

t of

RC

P s

eal

pres

sure

ind

icat

ion.

w

ater

flo

w.

RC

P s

eal

wat

er m

otor

61

. F

ails

Ope

n M

echa

nica

l bi

ndin

g.

No

effe

ct o

ther

tha

n to

R

CP

sea

l w

ater

flo

w

oper

ated

val

ve

Los

s of

air

or

elec

tric

al

isol

ate

seal

wat

er f

low

. pr

essu

re i

ndic

atio

n.

9ow

er.

62.

Fai

ls C

lose

d S

puri

ous

sign

al.

I Los

s of

sea

l w

ater

to

RC

P

63.

Fai

ls O

pen

RC

P S

eals

Sta

nd P

ipe

Glo

be V

alve

Sea

l W

ater

R

etur

n H

eade

r R

elie

f V

alve

Mec

hani

cal

bind

ing.

Los

s of

pow

er.

Spu

riou

s si

gnal

. S

etpo

int

drif

t.

Mec

hani

cal

fail

ure

Set

poin

t dr

ift.

M

echa

nica

l fa

ilur

e

Mec

hani

cal

bind

ing.

L

oss

of e

lect

rica

l po

wer

. S

eal

Wat

er

Ret

urn

Hea

der

Glo

be

valv

e

64.

Fai

ls C

lose

d

seal

s. R

CP

d °

age.

P

rim

ary

cool

ant

leak

age.

N

one.

RC

P s

eal

wat

er r

etur

n fl

ow

and

exce

ss le

tdow

n fl

ow

bypa

ssed

to p

ress

uriz

ed

reli

ef t

ank.

Fai

lure

inh

ibit

s us

e of

exc

ess

letd

own

flui

d sy

stem

as

an a

lter

nate

m

eans

of

letd

own

flow

co

ntro

ls.

Los

s of

sea

l w

ater

ret

urn

head

er o

ver

pres

sure

pr

otec

tion

.

Los

s of

red

unda

ncy

of

prov

idin

g is

olat

ion

of s

eal

wat

er a

nd e

xces

s le

tdow

n fl

ow.

65. F

ails

Ope

n

66.

Fai

ls C

lose

d

RC

P s

eal

wat

er f

low

and

pr

essu

re in

dica

tion

. R

CP

ex

tern

al l

eaka

ge.

Val

ve p

osit

ion

indi

cati

on.

Sta

ndpi

pe

leve

l in

dica

tor

Pre

ssur

izer

rel

ief

tank

le

vel

and

pres

sure

in

dica

tion

. V

CT

lev

el

indi

cati

on.

VC

T l

evel

ind

icat

ion

pres

suri

zer

reli

ef ta

nk

leve

l an

d pr

essu

re

indi

cati

on.

Rem

ote

valv

e po

siti

on

indi

cati

on

! 67.

Fai

ls O

pen

Sta

ndpi

pe a

larm

set

to

allo

w a

ddit

iona

l R

CP

op

erat

ion

befo

re

com

plet

e lo

ss o

f se

al

wat

er f

low

.

Val

ve i

s no

rmal

ly o

pen.

M

OV

ene

rgiz

ed t

o cl

ose

the

valv

e up

on r

ecei

pt o

f E

SF

sig

nal

O 6

S 7

D 5

t,,i

Page 22: Zip Code: 21945-970, Po. Box: 68550 E-mail: *tony@ien.gov ...read.pudn.com/downloads190/ebook/896218/Fuzzy FMEA... · reliability engineering problem. This method uses the concept

t,~

t,~

ID

69,7

0

71,

72,

73,

74

75,7

6

Com

pon

ent

Seal

Wat

er H

eat

Exc

hang

er R

elie

f V

alve

Seal

Wat

er H

eat

Exc

hang

er

Exc

ess

Let

dow

n F

low

C

ontr

ol V

alve

FaiL

ure

mod

e

68. F

ails

Clo

sed

69. F

ails

Ope

n

70. F

ails

Clo

sed

71. P

lugg

ed tu

bes

72. I

nsuf

fici

ent H

eat

Tra

nsfe

r.

73.

Tub

e L

eak.

74. E

xter

nal

leak

age.

75.

Fail

s O

pen

76.

Fail

s C

lose

d.

FaiL

ure

Cau

ses

Spu

riou

s si

gnal

.

Set

poin

t dri

ft.

Mec

hani

cal

fail

ure.

Set

poin

t dri

ft.

Mec

hani

cal

fail

ure.

Cor

rosi

on p

rodu

ct

buil

dup.

B

oron

pre

cipi

tati

on.

For

eign

mat

eria

l in

RC

S.

Sca

le b

uild

up o

n tu

bes.

Cor

rosi

on.

Man

ufac

turi

ng d

efec

t.

No

effe

ct.

Mec

hani

cal

bind

ing

Los

s of

pow

er.

Spur

ious

si

gnal

.

Fai

lure

Eff

ect

Seal

wat

er r

etur

n an

d ex

cess

let

dow

n fl

ow

bloc

ked.

D

egra

ded

deal

-coo

ling

ca

pabi

lity

. P

orti

on o

f se

al w

ater

ret

urn

flow

and

cha

rgin

g pu

mp

min

-flo

w b

ypas

sed

to

VC

T.

Los

s of

sea

l wat

er h

eat

exch

ange

r ov

erpr

essu

re

prot

ecti

on.

Red

uced

sea

l wat

er r

etur

n fl

ow.

Hig

h ex

it te

mpe

ratu

re m

ay

exce

ed V

CT

des

ign

tem

pera

ture

.

Con

tam

inat

ion

of C

CW

sy

stem

. RC

S d

ilut

ion.

No

effe

ct.

Una

ble

to i

sola

te f

low

to

eith

er e

xces

ses

letd

own

heat

exc

hang

er o

r dr

ain

tank

s.

i Una

ble

to u

se t

he e

xces

s le

tdow

n fl

uid

syst

em a

s an

al

tern

ate

mea

ns o

f co

ntro

llin

g le

tdow

n fl

ow,

and

pres

suri

zer

leve

l co

ntro

l

Fai

lure

Det

ecti

on

Met

hods

R

emot

e va

lve

posi

tion

in

dica

tion

. Sea

l wat

er

retu

rn f

low

indi

cato

r.

Hig

h V

CT

tem

pera

ture

. H

igh

seal

wat

er h

eat

exch

ange

r tem

p.

Seal

wat

er h

eat

exch

ange

r pre

ssur

e an

d fl

ow in

dica

tor

Seal

wat

er h

eat

exch

ange

r fl

ow,

tem

pera

ture

, and

pr

essu

re i

ndic

ator

. Se

al w

ater

hea

t ex

chan

ger f

low

, te

mpe

ratu

re, a

nd

pres

sure

indi

cato

r.

Seal

wat

er h

eat

exch

ange

r fl

ow a

nd d

elta

pr

essu

re in

dica

tors

. C

CW

sur

ge t

ank

leve

l in

dica

tor.

P

ress

ure

diff

eren

tial

ac

ross

hea

t exc

hang

er.

Tem

pera

ture

ind

icat

ors.

R

emot

e va

lve

posi

tion

in

dica

tor.

Exc

ess

letd

own

pres

sure

and

te

mpe

ratu

re in

dica

tion

. V

alve

pos

itio

n in

dica

tor.

E

xces

s le

tdow

n pr

essu

re

and

tem

pera

ture

in

dica

tion

.

No

~s

O 6

D 4

Page 23: Zip Code: 21945-970, Po. Box: 68550 E-mail: *tony@ien.gov ...read.pudn.com/downloads190/ebook/896218/Fuzzy FMEA... · reliability engineering problem. This method uses the concept

ID

77,7

8

79,

80,

81,

82

Com

pone

nt

Fai

lure

mod

e F

ailu

re C

ause

s F

ailu

re E

ffec

t F

ailu

re D

etec

tion

N

otes

M

etho

ds

77. F

ails

Ope

n C

harg

ing

Syst

em

Isol

atio

n V

alve

s

Exc

ess

Let

dow

n H

eat

Exc

hang

er

78. F

ails

Clo

sed.

79. P

lugg

ed t

ubes

80. I

nsuf

fici

ent H

eat

Tra

nsfe

r

81. T

ube

Lea

k

82. E

xter

nal L

eaka

ge

Los

s of

ele

ctri

cal p

ower

. M

echa

nica

l bin

ding

Spur

ious

sig

nal.

Cor

rosi

on p

rodu

ct

buil

dup.

B

oron

pre

cipi

tati

on.

For

eign

mat

eria

l in

RC

S.

Scal

e bu

ildu

p.

Cor

rosi

on.

Man

ufac

turi

ng d

efec

t.

Cor

rosi

on.

Man

ufac

turi

ng d

efec

t.

For

nor

mal

ly o

pen

valv

es,

no e

ffec

t dur

ing

regu

lar

oper

atio

n. H

owev

er, u

nder

ac

cide

nt c

ondi

tion

s, fa

ilur

e re

sult

s in

sig

nal t

o is

olat

e ch

argi

ng li

ne. F

or n

orm

ally

cl

osed

val

ves

fail

ure

resu

lts

in in

adve

rten

t op

erat

ion

of a

uxil

iary

sp

ray

resu

ltin

g in

red

uced

pr

essu

rize

r pre

ssur

e.

For

nor

mal

ly o

pen

valv

es,

loss

of n

orm

al c

harg

ing

flow

pat

h. F

or n

orm

ally

cl

osed

val

ves,

loss

of

abil

ity

to p

rovi

de a

uxil

iary

sp

ray

if re

quir

ed r

esul

ting

I i

n pr

essu

rize

r ove

r-

pres

suri

zati

on.

Red

uced

let

dow

n fl

ow.

Hig

h ou

tlet

tem

pera

ture

.

J Con

tam

inat

ion

of C

CW

sy

stem

. RC

S di

luti

on.

No

effe

ct.

Val

ve p

osit

ion

indi

cati

on. C

harg

ing

flow

indi

cato

r.

Pre

ssur

izer

pre

ssur

e in

dica

tion

.

Val

ve p

osit

ion

indi

cati

on. C

harg

ing

flow

indi

cato

r.

Pre

ssur

izer

pre

ssur

e in

dica

tor a

nd le

vel.

Let

dow

n fl

ow, h

eats

ex

chan

ger

flow

, te

mpe

ratu

re, a

nd

pres

sure

ind

icat

ors.

L

etdo

wn

flow

, he

ats

exch

ange

r fl

ow,

tem

pera

ture

, and

pr

essu

re in

dica

tors

. L

etdo

wn

flow

, hea

ts

exch

ange

r fl

ow,

tem

pera

ture

, and

pr

essu

re in

dica

tors

. Pr

essu

re d

iffe

rent

ial

acro

ss h

eat e

xcha

nger

, te

mpe

ratu

re in

dica

tion

.

D 5

¢q

ba

t.aa


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