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U.S. Nuclear Regulatory Commission Meeting \jWREcKj with Nuclear Energy Institute, Material Reliability Program, and Operating Pressurized Water Reactor Licensees' 0 (nlal C Thursday, November 8, 2001 1:00 p.m. - 5:00 p.m. Commissioners'HearingRoom Purpose: To discuss NRC staff's technical assessment for vessel head penetration nozzle cracking associated with NRC Bulletin 2001-01, "Circumferential Cracking of Reactor Pressure Vessel Head Penetration Nozzles." Success: NEI, MRP, and external stakeholders have a clear understanding of the staff's technical assessment and its' basis. Introduction: Jake Zimmerman 1:00 p.m. - 1:10 p.m. Bulletin 2001-01 Overview: Allen Hiser 1:10 p.m. - 1:30 p.m. Discussion of Crack Growth Rate: Dr. William Shack 1:30 p.m. - 2:00 p.m. Discussion of Crack Initiation: Dr. William Shack 2:00 p.m. - 2:30 p.m. - BREAK 2:30 p.m. - 2:45 p.m. - Discussion of Stress Analysis and Crack-Driving Force: Dr. Gery Wilkowski 2:45 p.m. - 3:15 p.m. Discussion of Critical Crack Size: Dr. Gery Wilkowski 3:15 p.m. Discussion of Deterministic Assessment: Allen Hiser 3:45 p.m. - 4:15 p.m. Discussion of Probabilistic Assessment: Allen Hiser 4:15 p.m. - 4:30 p.m. Discussion of Inspection Timing: Allen Hiser 4:30 p.m. - 4:45 p.m. 4:45 p.m. - 5:00 p.m. Comments/Questions from External Stakeholders: 3:45 p.m. - The NRC staff will be available immediately following the meeting to speak with members of the public. Attachment 1 OVERVIEW OF BULLETIN 2001-01: "CIRCUMFERENTIAL CRACKING OF REACTOR PRESSURE VESSEL HEAD PENETRATION NOZZLES" Allen Hiser Nuclear Regulatory Commission Office of Nuclear Reactor Regulation Division of Engineering November 8, 2001 Attachment 2 Typical Reactor Vessel Head - Oconee Unit 1 (Babcock & Wilcox) CRDM Insulation .Thermocouple Typical Location of PWSCC / •.•Vessel Head z -1- Schematic View of B&W Design CRDM Nozzle Area SA-182 F304 ERNiCr-3 (Alloy 82) SB-167 UNS N06600 (Alloy 600) - > Outer Surface of RPV Head RPV Head (SA-533 Gr. B CI. 1) Shrink Fit Cladding) -J-Groove Weld EniCrFe-3 (Alloy 182) -2- OVERVIEW OF BULLETIN 2001-01 Bulletin was issued on August 3, 2001 Bulletin requested information on: * All plants: Plant-specific susceptibility ranking • VHP nozzles (number, type, ID and OD, materials of construction) • RPV head insulation type and configuration , Recent VHP nozzle and RPV head inspections • Above the head structures, missile shield, cabling, etc. "* Plants that have found cracking or leakage: N Extent of cracking and leakage Inspections, repairs and other corrective actions • Plans and schedule for future inspections How plans will meet regulatory requirements "* Other plants: N Plans and schedule for future inspections • How plans will meet regulatory requirements -3- QUALIFICATION OF EXAMINATION METHODS "* Verify compliance with regulatory requirements through QUALIFIED examinations o. Graded approach depending on PWSCC likelihood ,0 Examinations of 100% of all VHP nozzles 4 Based on statistics and no identified preferential cracking tendencies 4 All VHPs - similar materials, etc., only failure consequences vary "* Effective Visual Examination ,. Capable of detecting small amounts of boric acid deposits and discriminating deposits from VHP nozzle and other sources "* Plant-Specific Visual Examination Qualification Plant-specific demonstration that VHP nozzle cracks will lead to deposits on the RPV head (interference fit measurements, etc.) , Must be capable of reliable detection and source identification of leakage (insulation, pre existing deposits, other impediments) "* Volumetric Examination Qualification , Demonstrated capability to reliably detect cracking on the OD of VHP nozzles Appropriate if Visual Examination cannot be Qualified -4- REVIEW OF BULLETIN 2001-01 RESPONSES Bulletin places PWR plants into 4 groups based on relative susceptibility ranking: "* Plants that have found Cracking or Leakage - 5 plants Suggests qualified volumetric examination by end of 2001 ,. Staff accepted qualified visual examination at last outage "* Plants with High Susceptibility (within 5 EFPY of Oconee 3) - 7 plants Suggests qualified visual examination by end of 2001 - Staff accepted qualified visual examination at last outage "* Plants with Moderate Susceptibility (between 5 and 30 EFPY of Oconee 3) - 32 plants Suggests effective visual examination at next RFO • Staff accepted effective visual examination at next RFE "* Plants with Low Susceptibility (more than 30 EFPY of Oconee 3) - 25 plants Suggests no additional actions required No requirement to provide plans or schedule Staff has addressed clarifications to Bulletin responses, and numerous licensees have provided revised or supplemented Bulletin responses -5- PLANTS THAT HAVE PERFORMED "BARE METAL" VISUAL INSPECTIONS Most Recent Inspection Plants Summary of Cracked or Leaking CRDM Nozzles I N Circumferential Number T NNozzle Cracks Repaired Date Method & Scope Oconee 1 11/2000 Qualified Visual - 100% 1* 0 1 Oconee 3 02/2001 Qualified Visual - 100% 9 3** 3 ANO-1 03/2001 Qualified Visual - 100% 1 0 1 Oconee 2 04/2001 Qualified Visual - 100% 5 1 5 Robinson 04/2001 Qualified Visual - 100%*** 0 0 0 North Anna 1 09/2001 Qualified Visual - 100%*** 8 0 0 Crystal River 3 10/2001 Effective Visual - 100%**** 1 1 1 TMI-1 10/2001 Qualified Visual - 100% 8* 0 6 Surry 1 (in progress) 10/2001 Qualified Visual - 100%*** 10 TBD 5 North Anna 2 10/2001 Qualified Visual - 100%*** (3) TBD TBD (inprogress) *k ** Thermocouple nozzles also cracked/leaking: Oconee 1 (5 out of 8), TMI 1 (8 out of 8) The size of 2 out of 3 circumferential flaws were identified from destructive examination. Pending acceptability of licensee's supplemental response **** The highest ranked MODERATE susceptibility plant. Moderate susceptibility plants that have completed effective visual examinations in Fall 2001 with no evidence of boric acid deposits: Beaver Valley 1, Farley 1, Kewaunee, and Turkey Point 3 -6- OVERVIEW OF STAFF PRELIMINARY TECHNICAL ASSESSMENT Summarizes available data and evaluations related to: "* "* "* "* * Environment in CRDM annulus region Crack initiation Crack growth rate Stress analyses and crack-driving force Critical crack size Deterministic assessment Probabilistic assessment Inspection timing -7- CRDM SUPPORT STUDIES W. J. Shack Argonne National Laboratory November 8, 2001 * Technical Issues addressed by ANL - Distribution of crack growth rates in Alloy 600 nozzle materials - Impact of potential crevice environments on expected crack growth rates - Probabilistic models for initiation of cracks in CRDM nozzles - Conditional probability of failure for nozzles - Integrated models to estimate probability of failure including initiation and growth Argonne National Laboratory Crack Growth Rates in Alloy 600 "* Scott's results on SG tubes suggest strong heat-to-heat variations in CGR are likely. Measurements on nozzle materials support this expectation. "* Critical issue is to estimate range of CGRs that will be encountered in the population of materials in service, not the range of CGRs in the limited number of heats being tested - "Weighting" the data by heat gives a better picture of CGRs of population than counting all data points as equal (or even weighting data by quality) - Better to determine dependence on basic parameters like K, T, by examining individual tests and test series with better controlled variables than statistical analysis of too large a data bin Argonne National Laboratory 1-9 -I Heat 69 0 0 Crack growth rate as a function of stress intensity factor K for Alloy 600 Heat 69. For this heat Scott A = 5.54 x 10-12. A is chosen as the parameter to characterize a heat. Scott A=5.54 x 1012 10-10 E (.) 10-11 ..0I 10 0 10 I.. 20 I . . I K (MPa.m 1- L a 0 E. I I I I 11 2 I, 70 60 50 40 30 . I . .. ... I da- A(K- 9)1.16 dt , 80 ) /•IIlI /// I I 0.8 /13 0.6 Cumulative distributions of A at 325 0C for Alloys 600 and 182 =1 0 0.4 3 /0 0 E 0).2 o0 1 o/ S- -- 00 I I I 0-1 10-12 I I Alloy 600 Alloy 182 I0 10-11 Scott A Argonne National Laboratory 4d 1 U- 0.8 LL .0 . • " 0.6 0.6 a a) 0.4 I 1 E, E 0 0.2 Q 0.8 0 1I I I I I I III 0.2 10.11 0 1011 0-12 10 1o12 0.4 Scott A Scott A "U. 0.8 Monte Carlo analysis performed to assess effect of uncertainties. Changes in distribution of A are .0 • 0.6 0.4 E 0.2 E 0.2- 0 Ayrelatively 600 MVC /Alloy Alloy r I I I I i 182 MC small especially in region of greatest interest. iil 10.11 10.12 Scott A Scott A parameter for Alloy 600 nozzle materials at 325 0C ,JAraonne SJ National Laboratory Confidence Level 50 67 90 95 1.8 2.3 4.2 5.6 Population 90 1.2 x 10-11 1.5 x 10-11 2.4 x 10-11 3.1 x 10-11 95 x 10-11 x 10-11 x 10-11 x 10-11 Percentage 67 5.1 x 10-12 5.8 x 10-12 7.5 x 10-12 8.4 x 10-12 3.1 3.5 4.4 4.8 50 x 10-12 x 10-12 x 10-12 x 10-12 10.8 109 E v10-11 10-11 10-12 L 0 20 40 60 K (MPa .m11 2) Argonne National Laboratory 80 100 lu 0 10 1 60 40 K (MPa.m 50 20 /2 ) Intensity Stress 30 70 80 Crevice chemistries and head form a tight crevice. FEA analysis suggests 0-4 mil gaps at pressure. Deposits suggest leakage even for a nozzle with a 1650 crack was less than 1 gallon over the cycle. Depending on the tightness of the crack, the tightness of the interference fit, and blockage by deposits or corrosion products environment can be steam, close to primary water, or concentrated solutions "* Nozzle - pH changes are limited by precipitation of insoluble species. Industry calculations with MULTEQ show that depending on location of boiling pH can become alkaline (~8.6) or acid (~4.6). - Because MULTEQ models don't deal with reactions with iron and nickel components these calculations probably overestimate pH shifts - Samples from actual crevices are needed to substantiate these preliminary conclusions. shifts can accelerate CGRs by a factor of ~2. This can affect initiation and throughwall growth of cracks. Once a significant throughwall crack has formed, crevice has good communication with bulk and water chemistry is even more likely to be close to primary water. "* Predicted Argonne National Laboratory 7 ý`-z Probabilistic initiation models o Mechanistic initiation models require more knowledge of local stresses and material microstructure. Probabilistic models use inspection data I 1 a ! 0.8 ~I .0 I Il I, I IlI~ I I I I, I I , , II 0 E~ b , • F median ranks Weibull fit - --.... 0.4 { Lognormal fit 0.2 0 0 b(x p(t)= - x) expQ - -QJb 1-exp F(t) = 0.6 U- b Il L, 0 II I 1 i . I 2 . . . I 3 i b-1 Argonne National Laboratory I 4 ii , ii i 5 . . ii 6 Weibull probability density and cumulative probability functions. Distribution of the Weibull slope b for cracking of steam generator tubes. * Estimates of Weibull parameters for plants that have been inspected and an associated distribution of values Plant 95th Median 5th Leaks 0.4 2.0 9.3 EFPY at 6000F 20 20 20 EFPY at 1st initiation b=3 23 13 8 b=1 .5 28 12 10 0 608.5 209.8 72.3 * Choice of b has impact on when 1st initiation occurs and the credit that can be expected for shorter operating times Plant Argonne National Laboratory Number of leaks expected 5th Median 95th b=1.5 5 10 0.05 0.15 5 10 0.01 0.06 0.25 0.71 b=3 0.03 0.27 1.24 3.46 0.17 1.33 NRC-FUNDED CRDM STRESS ANALYSIS, CRACK-DRIVING FORCE, AND LEAK-RATE ANALYSES by Engineering Mechanics Corporation of Columbus* G. Wilkowski, D. Rudland, and Z. Feng and ORNL R. Bass and P. Williams Presented by Gery Wilkowski 11/8/01 - NRC/Industry meeting Involvement to Date (1) Expert panel assistance on CRDMs started in late June. Work involved reviewing industry documents and assisting NRC staff with technical information. Emc 2 technical efforts involved: "* Stress analysis aspects - weld residual stress "* Crack-driving force and crack-opening displacement "* Leak-rate analyses "* Critical crack length calculations ORNL technical efforts involved: "* Stress analysis aspects "* Crack-driving force and crack-opening displacement (2) Technical assistance for plant specific assessments (3) Future CRDM efforts 4TU4•2- 1 Initial Stress Analysis Efforts Residual Stresses Some aspects of the review of work to date: "* The residual stress analysis for this problem is complicated by highly 3D aspect of the geometry. Industry efforts to date are good considering the time frame of efforts. " Some suggested improvements are; • Weld simulation created a whole ring of elements (one pass) instantaneously. (Traveling arc has heat sink in all directions not just normal to weld path.) * Using elastic-perfectly plastic stress-strain curve will give lower residual stresses than one with strain-hardening. Distribution of stresses also affected as well as peak values. &_ MC'2 3 Initial Stress Analysis Efforts Residual Stresses Some suggested improvements, continued; Effect of weld sequencing is not explored. Sequencing could be; the tube to the head in the radial direction (forces stresses in the weld to be higher either closer to the tube or the head), which could also affect OD axial cracking. •.Welding around the. circumference or from uphill to either continuously downhill side in two half circumferential steps on opposite sidc of the tube. (Higher stresses at stop Single stop-start Separate stop-start positions & ,2 4 2 Initial Stress Analysis Efforts Residual Stresses - Some suggested improvements, continued; *:. Mesh refinement in the weld bead could perhaps be finer SInformal survey of international weld stress analysts showed they typically used a minimum of 12 to 20 element in a single weld bead 2 cross-section. (Consistent with Emc experience.) Industry analyses Example of ultra-fine T" mesh - Emc2 fAV , N Total of 3,000 elements in weld TUC,2 t~g5 Recent Stress Analysis Efforts Thermal Expansion Stresses Thermal expansion and RPV hole expansion from pressure loads increase the annular clearance • * Good from leakage viewpoint, but Contributes to crack-driving force at the root of weld Coounterbore 6 3 Recent Emc 2 Stress Analysis Efforts Thermal Expansion Stresses Stresses from thermal expansion and pressure without residual stresses - simple axisymmetric model. S22 K1 = 18 ksi-in°-5 K2 = 12 ksi-in 0 5 & 411',2C Recent Emc 2 Stress Analysis Efforts Thermal Expansion Stresses Stresses from thermal expansion and pressure without residual stresses Principal stress direction at angle through the thickness? 5 K45 . = 12 ksi-in° 8 411.,C,2 8 4 Initial Stress Analysis Efforts Cyclic Thermal Stresses From analysis at Ringhals in early 1990's, there was concern of cyclic temperatures from water going up and down the nozzle region. It was expected that the thermal stresses may not be large enough to cause fatigue by themselves, but "may be a contributor to cracking in cold heads". 0 Past gas pipeline work on SCC showed that small cyclic stresses (R=0.95) can increase the crack growth rate. & M41 2 9 Initial Crack-Driving Force Analyses Efforts conduced both at Emc 2 and ORNL to examine K and COD. COD used for leak-rate analyses. "* Emc 2 analysis was elastic conditions with pressure only, and examined the effect of restraining the pressure-induced bending from the presence of a circumferential through-wall crack. No pressure on crack faces. "* K and COD much lower in restrained condition that simulates CRDM behavior. 0.o45 - 0.040 i0"035 -Unrestraineddi / .- •U-usd -U-Outside 0.030 6 _ 0.025 U-Middle ...--'"U-Inside 0.020 - ---- R-Outside e R-Middle R-Inside estraned 0015 "0.010 r0.005 o 0.000 0 50 100 150 200 Crack Length , degrees 250 300 M 10 (9010 5 Initial Crack-Driving Force Analyses Efforts conduced both at Emc 2 and ORNL to examine K and COD, continued " ORNL effort used gap elements to restrain bending and was elastic-plastic with pressure loading only, including full pressure on crack faces. " Similarly showed lower COD and K values with restrained bending particularly for longer cracks. Refinr.d Men. B 8015 elemnents ,31,.629 80 70 .-d. ORNL E=2E (Unrestrainedcase and no pressure on crack face) 60 7 ORNL (Restrained case and p=2.250 psig on crack face) 50 5• -Ec (Restrained case and 30 no pressureoncrackface) 20 0 0 50 100 150 200 250 2 300 Total Crack Angle, degrees 1l Initial Crack-Driving Force Analyses Efforts conduced both at Emc 2 and ORNL to examine K and COD, continued - ORNL also examined effect of applying a residual stress equal to yield in a simplistic manner, i.e., displacement-controlled axial tension stress on tube ;residual+ pressure 'r ':pressure J.... only~ (9 V, 12 6 Initial Leak-Rate Analyses Efforts at Emc 2 using COD from Emc 2 and ORNL, continued oFirst calculated a leak-rate for a circumferential through-wall crack "Used statistical mean crack morphology parameters (roughness, number of turns) for an IGSCC "- Assumes no back pressure at exit plane " Determined leak-rate (0.22 to 0.44 gpm) as well as pressure and temperature of water exiting the crack plane for 180-degree crack. (127 psig and 347 F) 1.4 1 ORNL analysis -- -$---2,250 psi crck-lace pressure -1 - no crack-face pressure 1.2 El Emc2 analysis 0.6 -j 0.4 0.2 0 4_.•1,Z 360 270 180 90 Circumferential Crack Angle, degrees 0 2 13 Initial Leak-Rate Analyses, continued Calculated the leak-rate through the annular region (0.1 to 0.3 gpm) Assumed 180-degree crack exit plane water is entrance water in annular plane SAssuming a radial gap of 1.2 mils on diameter (close to industry stated value) SUsed roughness for either drilled or reamed holes in annular area. -- - 1em. 34SF S3rrrc,127psi.34SF Fps.. - .- CflokodF-* 1.a cŽ. L/rcmkefcmked-- //C 0.co 0D.6c 0 0.OcS s.c1 0ccl2 c.cc14 0=cc6 Radial Cleaar-e Beteeeta Rod and Head.Inch 9 IYUC,2 14 7 Initial Leak-Rate Analyses, continued * Determined that for this crack size the annular leakage was limiting * The calculated leakage rate, however, was about 24,000 time greater than the Oconee 165-degree crack * Could be explained if the 165-degree crack all the way through the thickness or only over a short length? Leakage only at a few small locations along crack, rather than whole 165 degree length? • Residual stresses causing crack faces to rota e, and hence pinch off flow? • Plugging occurring at low leak rates? 15 Initial Review of Industry Work "•Industry efforts underway are impressive and involve a significant undertaking considering the time frame involved. "*Some suggested improvements if more time was available Redistribution of residual stresses may not be properly handled by putting load-controlled stresses on the crack faces from the uncracked model. • Need to map 3D stress and strain field from weld model onto the fracture model to properly determine the redistribution of stresses with crack growth. MAC, • 16 8 Review of Industry Work Some suggested improvements if more time was available, continued It appears that longitudinal (axial stresses) in tube were applied to crack face. . • Crack was in helical direction, so stresses normal to that direction should be used. Examination of weld model may show that crack growth may not be in a plane normal to the thickness, i.e., the principal stresses may be different than the axial direction or normal to the helical plane of the crack. •4'Y-C 2 17 Review of Industry Work Some suggested improvements if more time was available, continued " Weld sequencing effects on crack-driving force not examined * Could have high stress spots at 0 and 180 degree locations "Needto examine K from toe of weld as well as K from through wall crack. "* Will there be multiple initiation sites? "* What is the crack growth rate in the radial versus circumferential directions? "* Could a complex crack form (long surface crack with through wall crack of shorter length)? "•t~c" 2 18 9 NRC-FUNDED CRDM CRITICAL CRACK SIZE ANALYSES by Engineering Mechanics Corporation of Columbus* G. Wilkowski, D. Rudland, and Z. Feng Presented by Gery Wilkowski 11/8/01 - NRC/Industry meeting Involvement to Date (1) Expert panel assistance on CRDMs started in late June. Work involved reviewing industry documents and assisting NRC staff with technical information. Emc 2 technical efforts involved: * * * * Critical crack length calculations Stress analysis aspects - weld residual stress Crack-driving force and crack-opening displacement Leak-rate analyses ••~2 I Critical Crack Analysis Limit-load analyses examined to; "* Determine proper limit-load boundary conditions, "* Determine flow-stress definition? " Determine if toughness of Inconel 600 is sufficient for limit-load to be used? " Conduct analyses for CRDMs with ideal '. through-wall crack, surface crack, and complex crack. ,, N rnm-ArrOd CroackFbmd m Service & -1,2 3 Determine Proper Limit-Load Conditions Solutions exist for axial tension on a cylinder with a circumferential crack • End-capped solution most common, but allows for free rotation of cylinder ends due to pressure-induced bending from presence of crack. CRDM tube restrained from bending by RPV head ....... ....... ....... ............. .... .. . & 4ThC 4 2 Determine Flow-Stress Definition Axial tension tests with restrained-bending on circumferential through-wall-cracked 4" diameter stainless steel pipe conducted in past. • Flow stress = (yield + ultimate)/2.4, which is less than average Flow strml empirically determined to be (yleld+ ultimaNey2.4 ýeY,ga -FR ~ det. *0 0.7 0.6 ~o 0.1 02 0 45 130 90 180 225 360 315 270 Total crack length, degrees---- 2 5 Determine if Inconel 600 Has Enough Toughness to Use Limit-Load Solution " Dimensionless Plastic-Zone Screening criterion developed to determine toughness requirement for using limit-load analyses. " From PIFRAC database Inconel 600 JIC = 9,310 in-lb/in 2 (1.63 MJ/m 2), which give plastic-zone parameter of 3.5 and limit-load should work. - .. S-- .- D--:,. N9 4TUC,26 3 Limit-Load Analysis with Crack-Face Pressure Longer cracks are more affected by crack-face pressure idealized through-wall crack example. 40.000 Using Inconel 600 properties 35.000 Using typical at 0F properties actual strength 30,.000- crack length at 2•.000Critical 3 times operating pressure 0. crack lesign Crtia............. 31~~~~~ eraesUdeinpan.es.s0P5 sg< atsue(,O 25,000 t15.000 3.000 3Design pressure (2,5a0 psg) length, degrees 0 Total 40 0- 180 135 through-wall-crack 225 30 0 315 270 CRDM Critical Crack Length Calculations 20,000 Using Inconel 600 Code properties at 600F 18,000 16,000 . att=0.25 ••/ 10.000 . Idealized TWC Cornplexcracks. 14,000 12,000 "Q. () .- a/t-0.50 10,000 . .......... :......... "+............ . ........... 3 times designprsre(,0psg ............................ ... .... .... ... ...................... 2 .... sas -" .... ......... ............. 6.000 400 aAt=0.75 L/"' 2.. M.++ ---------- 4,000 200 0 45 +o+ +o& 90 135 180 225 270 315 360 Total through-wall-crack length, degrees 4 CRDM Critical Crack Length Calculations 0.7 4. 0.6 ") 0.5 0.4 Q t 0.3 0.00 45.00 g0.00 135.00 180.00 225.00 270.00 Total through-wall-crack length, degrees 315.00 ;;; 'Y1" 360.00 2 Critical Crack Length Analyses Summary * * * * * * Restrained-bending limit-load solution is more appropriate for CRDMs. Flow stress = (Y+U)/2.4 from pipe tests with similar loading (lower than typical average of yield and ultimate definition). Pressure on crack-face important for longer cracks. Toughness of Inconel 600 high enough to use limit-load solution. Ideal TWC critical length at 3*design pressure = 262 to 269-degrees (slightly less than industry calculated value), but very fracture resistant material. Critical surface crack/complex crack/ideal through-wall crack lengths at design pressure given. Critical 360-degree surface crack of constant depth would be 90-percent of thickness. Difficult to get such a crack geometry without getting some through-wall component. & 41~L-to 5 DETERMINISTIC AND PROBABILISTIC ASSESSMENTS Allen Hiser Nuclear Regulatory Commission Office of Nuclear Reactor Regulation Division of Engineering November 8, 2001 STAFF CONCLUSIONS Annulus Environment "* Not expected to be highly aggressive - normal PWR reactor coolant "* Annulus deposits from leaking nozzles should be obtained and analyzed by industry to provide confirmation of the assumed annulus environment Crack Initiation "* The operating experience of leaking nozzles appears to be well modeled by the Weibull analysis with b = 1.5 "* New findings data will continue to be assessed Crack Growth Rate * Crack nrowth rate data for PWSCC is a reasonable annroximation for OD VHP nozzle cracking 0 Analysis of data provided in Table 3 is appropriate for use at 3250C (617'F) 0 The Arrhenius relation can be used for crack growth at other temperatures -2- STAFF CONCLUSIONS (cont.) Stress Analysis and Crack-Driving Force * A single estimate for K as a function of circumferential crack length was provided (with a value of 66 MPa /--m (60 ksiv/ in.) due to residual stresses for a crack angle of 900) Critical Crack Size "* Critical size with a safety margin of three on pressure is 2700 is 3240 "* Critical size for nozzle failure and possible ejection -3- DETERMINISTIC ASSESSMENT Base Case - Assumptions "* Critical Flaw Size ,. 2700 with a safety margin of three on pressure ,. 3240 for nozzle failure and possible ejection "* Crack Growth Rate ,. 95/50 statistical bound 3180C (6050F) A for Scott model is 1.303 x 10-11 • "* Initial Flaw Size 0. Unknown - basis for issuance of the Bulletin No. Used as a parameter Uncertainties and Sensitivity Studies "* "* "* Different statistical bounds to crack growth rate Effects of temperature on crack growth rate Initial flaw size as a parameter -4- 60 50 ", 0 *• 30 20 .,-- 200 10 0 o -,-" ....... K Estimated KSIA K ORNL pressure 0 0 50 100 150 200 Crack Half Angle Figure 15 Estimated stress intensity factor K for a CRDM nozzle based on SIA and ORNL results. -5- Table 4 Summary of OD Circumferential Flaws Identified in Spring and Fall 2001 Outages Plant * Nozzle Circumferential Through-Wall ID Crack Length Extent Oconee Unit 3 50 1650 100% Oconee Unit 3 56 1650 100% Oconee Unit 3 23 660 * 35% * 450* 18 Oconee Unit 2 900 * 32 Crystal River Unit 3 Crack dimensions estimated from UT data. 10% * 50% * -6- CRDM NOZZLE CRACK GROWTH RATE (Base Case, 3180C, 95/50) 3.0 cz 2.5 2E-9 - 2.0 ----- \,------- .. . . . -- - - - - - .-. --. .-. -. .-. -. .-. -. . . --------.. ----- ---- E ------- . . . . . -. . -. . -.',.. . . . . -------------- (I O1 M 0 1.5 -------------- 0. 1E-9 -----/---------- ------- -6 U 1.0 0.5 U.U 1 0 60 120 180 240 300 360 U Circumferential Crack Length (Degrees) Figure 18 Variation of crack growth rate with circumferential crack length for the base case of 318'C (605 'F) 95/50 curve. -7- FAILURE TIME EVALUATION (3180C, 95/50) (I) 360 0) ci) ci) 300 0) 240 0 -J 0 180 0 6 0 120 60 0 0 12 24 36 48 Operating Time (months) Figure 19 Variation of time to failure as a function of initial crack length, for the base case of 318 'C (605 TF), 95/50, crack growth rate. -8- 60 CRACK GROWTH EVALUATION Cl) 0.le (Base Case, 3180C, 95/50) 360 300 Q 240 0(D E) 180 0 12 24 36 48 60 Operating Time (months) Figure 20 Evaluation of operating time to reach critical flaw sizes at three times design pressure and at nozzle failure/ejection after development of a 1650 long circumferential through-wall flaw. -9- EFFECT OF OPERATING TEMPERATURE ON 'A' Operating Temperature (OF) 550 625 600 575 1.0 1.0 ) 0 LL 0 Cq coJ 0.8 0.8 0 © E, 0.6 0.6 < E I- N (0 0.4 0.4 0.2 0.2 0.0 C. E ( 0.0 280 290 300 310 320 330 Operating Temperature (°C) Figure 21 Lower operating temperature results in lower crack growth rates for VHP nozzle materials, within the operating temperature range of the nozzles. -10- CRDM NOZZLE CRACK GROWTH RATE 3.0 co 2E-9 0OC 318 0 C (B) -~ 0 o (5 .% 1.0 "E 0 / 1• 315 0C (M) I 0.5 0).0 0.0 ' 0 I 60 a I 120 , I I , 180 240 , I 300 , I 0 360 Circumferential Crack Length (Degrees) Figure 22 Variation of crack growth rates at several pertinent temperatures and using 95/50 ('B' on the curves) and mean values ('M' on the curves). -11 - CRACK GROWTH EVALUATION U, 360 a, 300 a, I- 240 180 0 12 24 36 48 60 72 84 96 Operating Time (months) Figure 23 Crack growth analysis using various crack growth rate assumptions, from an initial flaw size of 165(. Although decreasing the temperature has some effect, the most dramatic increases in failure times occur with the mean crack growth curve instead of the 95/50 curve. -12- TIME TO 3 X DESIGN PRESSURE C') 360 a) 0) 0 -0 -j C 300 240 180 120 C: 60 0 0 24 48 72 96 120 Operating Time (months) Figure 24 Comparison of time to reach the flaw size representing three times the design pressure, for a variety of crack growth rates and as a function of initial flaw size. -13- TIME TO NOZZLE FAILURE/EJECTION 360 (D 0) 300 240 180 0 CZ 120 60 0 0 24 48 72 96 120 Operating Time (months) Figure 25 Comparison of time to reach the flaw size representing three times the design pressure, for a variety of crack growth rates and as a function of initial flaw size. -14- CONCLUSIONS FROM DETERMINISTIC CALCULATIONS Results are very sensitive to: "* "* "* Initial flaw size Statistical bound on crack growth rate Temperature Traditional safety margins may not be sufficient to account for large variability in crack growth rates for Alloy 600 in PWSCC conditions -15- PROBABILISTIC ASSESSMENT "* A Complete Phenomenological Model 0. Requires a better understanding of the complete cracking process ,. Requires data to characterize critical parameters (means & bounds) "* Empirical Model , Based on reliable data on number and size of cracks found in service Qualification of NDE sizing an issue Cost of destructive confirmation large * Need to determine Frequency of Failure to estimate Core Damage Frequency -16- INSPECTION TIMING Likelihood of Circumferential Cracking High susceptibility plants - 8 out of 9 have identified cracking , Moderate susceptibility - effective visual examinations will provide additional data High Susceptibility Plants That Have Performed Effective Inspections , Can use Figures 23 to 25 New circumferential cracking can initiate High Susceptibility Plants That Have NOT Performed Effective Inspections ,. Need baseline inspection to provide basis for evaluation Inspection Method Qualified visual examination is appropriate , Surface or volumetric examinations Inspection Scope 100 percent of nozzles , Entire surface or metal volume of interest ", "Wetted surface" - J-groove weld, nozzle OD (below the weld), and nozzle ID to a location above the weld , Volumetric - OD of nozzle above the J-groove weld , Visual qualification analysis can occur ex-post facto after the inspection -17- FUTURE STAFF PLANS "* Continue development of probabilistic modeling "* Complete review of Bulletin supplemental responses "* Assemble findings from inservice inspections "* Issue NUREG report "* Long-term inspection plans -18- INDUSTRY INTERACTIONS "* Interactions on deterministic and probabilistic analyses "* Inspection methods and findings "* Destructive confirmations ,. Flaw sizes ,. Annular conditions -19-. -"P4- NRC Meeting with Nuclear Energy Institute, Materials Reliability Project Operating Pressurized Water Reactor Licensees .•and CO 0. rThursday, November 8, 2001 1:00P.M. - 5:00 P.M. 0 I'IUU IIh UlIIIIII I.IJIIIO Orcaanization/Title Name [llu0aa III1I rI"UII m Phone Number/Email Jake Zimmerman NRC/NRR/DLPM - Lead Project Manager (301) 415-2426, [email protected] Allen Hiser NRC/NRRIDE/EMCB - Lead Technical Reviewer (301) 415-1034, alhl @nrc.gov Jack Strosnider NRC/NRR/DE (301) 415-3298 Bill Bateman NRC/DE/NRR/EMCB (301) 415-2795 Keith Wichman NRC/NRR/DE/EMCB (301) 415-2757 Andrea D. Lee NRC/NRR/DE/EMCB (301) 415-2735, adwl @nrc.gov Jay Collins NRC/NRR/DE/EMCB (301) 415-1038 Nilesh Chokshi NRC/RES/DET/MEB (301) 415-0190 Ed Hackett NRC/RES/DET/MEB (301) 415-5650 Wallace Norris NRC/RES/DET/MEB (301) 415-6796 Shah Malik NRC/RES/DET (301) 415-6007 Jin Chung NRC/NRR/DSSA/SPSB (301) 415-1071 Ian Jung NRC/NRR/DSSA/SPSB (301) 415-1837 Giovanna Longo NRC/OGC (301) 415-3568 Darl Hood NRC/NRR/DLPM/PDIII-1 (301) 415-3049 Tim Colburn NRC/NRR/DLPM/PDI-1 (301) 415-1402 K.N. Jabbour NRC/NRR/DLPM/PDII-2 (301) 415-1496 John Goshen NRC/NRR/DLPM/PDII-2 (301) 415-1437 Dan Collins NRC/NRR/DLPM/PDI-1 (301) 415-1427 Brendan Moroney NRC/NRR/DLPM/PDII-2 (301) 415-3974 Ujagar Bhachu NRC/NRR/DLPM/PDII-2 (301) 415-3271 R.L. Clark NRC/NRR/DLPM/PDI-1 (301) 415-2297 Ray Wharton NRC/NRR/DLPM/PDIV-2 (301) 415-1396 Attachment 3 (614) 459-3200 Gery Wilkowski Engineering Mechanics Corp. of Columbus W.J. Shack Argonne National Lab Scot Greenlee American Electric Power (AEP) (616) 697-5728 Dan Garner AEP (616) 466-3419 S.P. Moffitt FENOC (419) 321-8222 Guy Campbell FENOC (419) 321-8588 David Lockwood FENOC (419) 321-8450 David Geisen FENOC (419) 321-8109 Ken Byrd FENOC (419) 321-7924 Robert Enzinna Framatome ANP (434) 832-2418 Stanley Levinson Framatome ANP (434) 832-2768 Peter Scott Framatome ANP (33) 147963577 Stephen Fyfitch Framatome ANP (412) 264-1610 Ken Youn Framatome ANP (434) 832-3280 Alex Marion NEI (202) 739-8080 Gretchen Testaye Calvert Cliffs (410) 495-3736 Dan Salter HGP, Inc. (864) 370-0213 Dick Labott PSEG - Salem (856) 339-1094 R. Hermann SIA (540) 710-6717 Bob Hardies CCNPPI (410) 495-6577 Jim Meister Exelon (630) 657-3800 Altheia Wyche SERCH Licensing/ Bechtel (301) 228-6401 Tom Harrison McGraw-Hill (202) 383-2165 Harold Chernoff CP&L (843) 857-1437 Shataro Mori The Konsai Electric Power (202) 659-1138 Paul Gunter NIRS (202) 328-0002 Deann Raleigh LIS, Scientech (301) 258-2557 Roger Huston Licensing Support Services (703) 671-9738 H. Fontecilla Dominion (703) 838-2314 Roy Lessy (202) 887-4500 Attachment 3 PHONE PARTICIPANTS Organization/Title Name Phone Number/Email Dick Mattson Structural Integrity Associates (408) 978-8200 Daniel Stenger Ballard, Spahr, Andrews & Ingersoll, LLP (202) 661-7617 Robert Lemberger Florida Power, Crystal River 3 (352) 795-6486, x3862 Stephen Collard FPL Michael Moran FPL Terry Pickens Nuclear Management Company, LLC Donald Bemis CMS Energy Richard Gerling CMS Energy Ed Siegel Westinghouse George Lavigne NAESCO Jeffrey Sbotka NAESCO Kevin Whitney NAESCO Scot Sulley NAESCO James Connolly NAESCO Yogen Garud APTECH Engineering Services, Inc (408) 745-7000, x3060 Mark Fleming Dominion Engineering, Inc.(DEI) (703) 790-5618, x239 Glenn White DEI John Crane Westinghouse Greg Gerzen Exelon (630) 657-3845 Christine King EPRI (650) 855-2605 (715) 377-3390 (603) 773-7126 Frank Ammirato fammirat@ epri.com Ron Baker [email protected] Warren Bamford bamforwh @westinqhouse.com Jim Bennetch jim [email protected] Dave Berko Daveberkode @inpo.orcq Prasanta Chowdhury pchowdh @enterqy.com Attachment 3 Kurt Cozens koc @ nei.org John Hall iohn.f.hall@ us.westinghouse.com John Hamilton [email protected] Craig Harrington charrinl @txu.com Larry Mathews [email protected] Gary Moffatt [email protected] Ben Montgomery [email protected] Donald Naylor [email protected] Raj Pathania RPATHANI@ epri.com Jeffrey Portney ilp4 @pge.com Mike Pugh [email protected] Eric Schoonover schoonei @ soncqs.sce.com Michael Shields mike shields@ rae.com William Sims [email protected] Ronald Swain rswainl @enterqy.com Chuck Tomes [email protected] Vaughn Wagoner vaughn.wagoner@ pgnmail.com Joseph Weicks iweicks@ enteroy.com Attachment 3