Lecture 5 Probability
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1 Lecture 5 Probability Dr. V.G. Snell Nuclear Reactor Safety Course McMaster University vgs 1
2 Probability Basic Ideas P(A)/probability of event A 'lim n64 ( x n ) (1) (Axiom #1) 0 # P(A) #1 (1) (Axiom #2): P(A)%P(Ā) ' 1 where Ā means "not A". (1) vgs 2
3 Intersection A 1 _ A 2 or A 1 A 2 or A 1 AND A 2 (This is not A 1 times A 2 ) (1) (Axiom#3) P(A 1 A 2 ) ' P(A 1 A 2 ) P(A 2 ) ' P(A 2 A 1 ) P(A 1 ) (1) vgs 3
4 In Pictures If the events are independent: P(A2 A1) = P(A2) vgs 4
5 Probability of Two Shutoff Rods Failing P(A1) = P (A2) = If independent, P(A1A2) = (0.001) 2 = 10-6 Suppose there is a common cause failure 10% of the time P(A1) = P(A2) = (random) (CC) Common cause vgs 5
6 Two Shutoff Rods cont d P(A1 A2) = 0.9 * * 1 = P(A1A2) = * = ~ 10-4 A 10% common cause probability has increased the combined failure by a factor of 100! vgs 6
7 Generalization P(A 1 A 2...A N ) ' P(A 1 )P(A 2 A 1 )...P(A N A 1 A 2...A N&1 ) (1) If the events are independent: P(A 1 A 2...A N ) ' P(A 1 )P(A 2 )...P(A N ) (1) For example: Probability of flipping heads twice in succession = (1/2) * (1/2) vgs 7
8 Union A 1 ^ A 2 or A 1 %A 2 or A 1 OR A 2. (1) P(A 1 %A 2 ) ' P(A 1 ) % P(A 2 ) & P(A 1 A 2 ) (1) Why subtract P(A1A2)? Think of probability of getting one head when you flip two coins: P(first head OR second head) = P(first head) + P(second head) P(both heads) = = 0.75 vgs 8
9 Generalizing N N&1 N P(A 1 %A 2 %...%A N ) ' j P(A N ) & j j P(A n A m ) n'1 n'1 m'n%1 ±...%(&1) N&1 P(A 1 A 2...A N ) (1) For independent events 1 & P(A 1 %A 2 %...%A N ) ' k N n'1 [1&P(A N )] (1) vgs 9
10 Rare Independent Events P(A 1 %A 2 %... A N ) j N n'1 P(A N ) (1) P(A 1 A 2...A N ) ' P(A 1 )P(A 2 )...P(A N ) (1) vgs 10
11 Bayes Theorem Start from event B and A n mutually exclusive events or hypotheses, where n = 1,,N P(A n B) ' N j m'1 P(A n ) P(B A n ) P(A m ) P(B A m ) (1) vgs 11
12 Bayes with Known Statistics Radiographing a Class I pipe for a defect Known likelihood of a defect is one per 100,000 radiographs Known likelihood of instrument giving false positive is 1% Known accuracy or likelihood of indicating a defect when there is a defect is 99%. One test indicates a defect What is the probability that the pipe actually has a defect? vgs 12
13 Working it out A: pipe has a defect, so P(A) = B: instrument says that pipe has a defect, so P(B)=0.01 approx. B A: instrument says pipe has a defect when it has a defect, so P(B A) = 0.99 Want likelihood of a defect when instrument gives a positive P(A B) = [P(B A)][P(A)]/P(B) = 0.99 x / 0.01 = How worried should you be if you get a positive test for a rare disease? vgs 13
14 Bayes with Unknown Statistics How to determine the frequency of an event which has not occurred Take a number of possibilities for frequency Assign (guess) a likelihood of each possibility being correct Use Bayes theorem to see if your guesses are sensible Problem: bad guess = silly result vgs 14
15 Probabilities for OR ed Events Take two dice. What is the probability that die 1 shows a six OR die 2 shows a six? Recall P(A 1 +A 2 ) = P(A 1 ) + P(A 2 ) - P(A 1 A 2 ) vgs 15
16 Work it out Since P(A 1 ) = P(A 2 ) =1/6, and P(A 1 A 2 ) = 1/36, then P(A 1 +A 2 ) = 1/6 + 1/6-1/36 = 11/36. vgs 16
17 Table of Combinations Die 1 Die 2 Number of Cases showing six 1 1,2,3,4,5, ,2,3,4,5, ,2,3,4,5, ,2,3,4,5, ,2,3,4,5, ,2,3,4,5,6 6 Total Combinations Showing six 11 vgs 17
18 Another Way P(at least one six) = 1 - P(no sixes) Probability of no sixes for each die = [1 - the probability of getting a six] Probability of getting no sixes for both dies = the product of the probability of getting no six for each die P(no six for die 1) = 1 - P(six for die 1) P(no six for die 2) = 1 - P(six for die 2) P(no six for die 1 AND no six for die 2) = [1 - P(six for die 1)][1 - P(six for die 2)] vgs 18
19 Numbers P(at least one six) = 1 - P(no sixes) = 1 - [1 - P(six for die 1)][1 - P(six for die 2)] = 1 - [1-1/6][1-1/6] = 1-25/36 = 11/36 1 & P(A 1 %A 2 %...%A N ) ' k N n'1 [1&P(A N )] (1) vgs 19
20 Why bother? Examples drive theory and understanding, not the reverse Often using P(not A) or is more useful P(A) Which would you use for 1000 dice? vgs 20
21 Demand and Continuous Examples of demand systems Shutdown, stepback ECC initiation Containment box-up Examples of continuous systems HTS pump motor Air coolers Reactor control system vgs 21
22 Mixed Systems e.g., ECC Initiation demand Switch from HPECI to MPECI to LPECI demand Crash cooldown - demand MPECI and LPECI Operation continuous Heat exchangers, pumps Limited mission time vgs 22
23 Demand Systems Dn = n th demand P(D n ) = probability of success on demand n P( D n ) ' probability of failure on demand n W n = system works for each demand up to and including demand n. ˆ P(W n&1 ) ' P(D 1 D 2 D 3... D n&1 ) (1) P( D n W n&1 ) ' P( D n W n&1 ) P(W n&1 ) (2) So P(D 1 D 2 D 3...D n&1 D n ) ' P( D n W n&1 ) P(W n&1 ) ' P ( D n D 1 D 2...D n&1 ). P (D n&1 D 1 D 2...D n&2 )...P(D 2 D 1 ) P(D 1 ) (3) If all demands are alike and independent, this reduces to: P(D 1 D 2...D n&1 D n ) ' P( D) [1&P( D)] n&1 (4) vgs 23
24 Failure Dynamics f(t)dt ' probability of failure in the interval dt at time t F(t) ' accumulated failure probability t ' f(t ) )dt ) m 0 Assuming that the device eventually fails the reliability, R(t) is defined as (1) R(t) ' 1 & F(t) 4 t ' f(t ) )dt ) & f(t ) )dt ) m m 0 ' m 4 t 0 (1) f(t ) )dt ) vgs 24
25 Conditional Failure Rate - 1 f(t) ' & dr(t) dt ' df(t) dt (1)?(t) =failure rate at time t given successful operation up to time t f(t)dt '?(t) dt R(t) or f(t) '?(t) R(t) ' & dr dt (1) vgs 25
26 Conditional Failure Rate 2 t R(t) ' exp&?(t)dt (1) m 0 If l is constant (random failures) R( t) = λ e t vgs 26
27 Summary of Terms Figure A summary of equations relating?(t), R(t), F(t), and f(t) vgs 27
28 Mean Time to Failure MTTF 0 tf ( t) dt = = tλe dt = 0 (for random failures) f ( t) dt 0 λt 1 λ vgs 28
29 Typical Behaviour of λ? (t) Typical mechanical equipment Typical electrical equipment Life expectancy Random failure rate Burn-in or debugging period time Useful life period Wear-out period Figure Time dependence of conditional failure (hazard)rate [Source: Ref. 1, page 26] vgs 29
30 Availability Availability = Reliability + effect of repair R(t) A(t) 1 With no repair, R(t) = A(t) vgs 30
31 Continuous Operation 1 For random failures R R(t) = e -λt time F(t) = 1 R(t) 1 F vgs time 31
32 With Repair In any time interval 0 < t < τ between repairs F(t) = λt F Average is <F> = λτ/2 J time vgs 32
33 Example One Shutoff Rod Suppose λ = 0.02 / year Want Unavailability A = λτ/2 So τ 1 year A (1-A) F 10-3 (per demand) vgs 33
34 Meeting Reliability Targets Increase repair frequency τ until <F> meets the target Increase test frequency and fix if it fails on test vgs 34
35 Event trees and Fault Trees Simplified treatment Fault tree frequency of an initiating event Focus on how an event can occur Event tree frequency of core damage Focus on mitigating systems, given an event vgs 35
36 Event Tree vgs 36
37 Fault Tree vgs 37
38 Fault Tree Symbols - Events Basic Event Undeveloped Event Intermediate or Top Event vgs 38
39 Fault Tree Symbols - Gates AND Gate OR gate INHIBIT Gate vgs 39
40 Steps in Creating a Fault Tree Define top event E.g. system failure Write down the immediate causes of the top event If more than one, decide whether they are joined by AND or OR gates For each of these lower events, expand them similarly Continue until you can no longer break the event down, or you know the probability of failure vgs 40
41 Example Fault Tree vgs 41
42 Evaluation Top X Y X1 Y1 = X Y = A+X1 = D+Y1 = B+C = B+E Therefore: X Y TOP = A+B+C = D+B+E = (A+B+C) (D+B+E) = AD+AB+AE+BD+BB+BE+CD+CB+CE = B+AD+CD+AE+CE vgs 42
43 Develop a Fault Tree for This S S V1 P1 S Water tank S S V2 V1 V3 Reactor P2 Demand failure probabilities for each component: Pump (P): 0.01 Valve (V): 0.01 Signal (S): vgs 43
44 Minimal Cut Set Cut set = any basic event or combination of basic events that will cause the top event to occur Minimal cut set = the smallest combination of events which, if they all occur, will cause the top event to occur vgs 44
45 Minimal Cut Set Gives Reduced Fault Tree vgs 45
46 Event Tree Exercise A LOCA in a CANDU calls on the following safety functions to prevent a release of radioactivity to the environment: Shutdown (either of two shutdown systems) Emergency Core Cooling Containment (box-up and cooling) If ECC fails, the moderator can prevent fuel melting If the demand unavailability of each of the four safety systems is 10-3 and of the moderator is 10-2, draw the event tree and determine: The frequency of severe core damage The frequency of a large release vgs 46
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