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| number = ML14315A087 | | number = ML14315A087 | ||
| issue date = 11/04/2014 | | issue date = 11/04/2014 | ||
| title = | | title = NRR E-mail Capture - STP Slides for 11/6/14 Public Phone Call | ||
| author name = Harrison A | | author name = Harrison A | ||
| author affiliation = South Texas Project Nuclear Operating Co | | author affiliation = South Texas Project Nuclear Operating Co | ||
| addressee name = Singal B | | addressee name = Singal B | ||
| addressee affiliation = NRC/NRR/DORL | | addressee affiliation = NRC/NRR/DORL | ||
| docket = 05000498, 05000499 | | docket = 05000498, 05000499 | ||
| Line 15: | Line 15: | ||
=Text= | =Text= | ||
{{#Wiki_filter: | {{#Wiki_filter:1 NRR-PMDAPEm Resource From: | ||
Sent:Tuesday, November 04, 2014 4:45 PM To:Singal, Balwant; Stang, John | Harrison Albon [awharrison@STPEGS.COM] | ||
Sent: | |||
Tuesday, November 04, 2014 4:45 PM To: | |||
Singal, Balwant; Stang, John | |||
==Subject:== | ==Subject:== | ||
| Line 22: | Line 25: | ||
STP Head-Loss Testing for Addressing GSI-191 - 110614 - Final.pdf | STP Head-Loss Testing for Addressing GSI-191 - 110614 - Final.pdf | ||
Hearing Identifier: | Hearing Identifier: | ||
NRR_PMDA Email Number: | |||
1681 Mail Envelope Properties (8C918BCF8596FB49BD20A610FA5920CF02182452) | |||
==Subject:== | ==Subject:== | ||
STP Slides for 11/6/14 Public Phone Call | STP Slides for 11/6/14 Public Phone Call Sent Date: | ||
Tracking Status: None | 11/4/2014 4:44:54 PM Received Date: | ||
Tracking Status: None Post Office: | 11/4/2014 4:46:33 PM From: | ||
Harrison Albon Created By: | |||
awharrison@STPEGS.COM Recipients: | |||
"Singal, Balwant" <Balwant.Singal@nrc.gov> | |||
Tracking Status: None "Stang, John" <John.Stang@nrc.gov> | |||
Tracking Status: None Post Office: | |||
CEXMBX04.CORP.STPEGS.NET Files Size Date & Time MESSAGE 3 | |||
11/4/2014 4:46:33 PM STP Head-Loss Testing for Addressing GSI-191 - 110614 - Final.pdf 668820 Options Priority: | |||
Standard Return Notification: | |||
No Reply Requested: | |||
No Sensitivity: | |||
Normal Expiration Date: | |||
Recipients Received: | |||
STP Strainer Testing to Address GSI-191 South Texas Project Nuclear Operating Company Alion Science and Technology University of New Mexico Thursday, November 6, 2014 1 | |||
Desired Outcome | Desired Outcome | ||
*Establish common understanding of STP strainer tests | * Establish common understanding of STP strainer tests | ||
-Purpose and scope | - Purpose and scope | ||
-Procedures | - Procedures | ||
-Facility and diagnostics | - Facility and diagnostics | ||
*Identify and understand NRC staff issues with test plan | * Identify and understand NRC staff issues with test plan | ||
*Focus continued discussion for resolution of issues in follow-on public meeting 2 | * Focus continued discussion for resolution of issues in follow-on public meeting 2 | ||
Review of STP RIR Head Loss Approach | |||
Review of STP RIR Head Loss Approach Current Licensing Amendment Request | |||
-Modified NUREG/CR-6224 correlation for | - Modified NUREG/CR-6224 correlation for conventional P | ||
*Challenged on bases for: | * Challenged on bases for: inconsistent derivation, inconsistent prediction, uncertainty assessment (x5) | ||
-Exponential factors for chemical | - Exponential factors for chemical P | ||
*Challenged on multiplicative effect and bases for S,M,L magnitude | * Challenged on multiplicative effect and bases for S,M,L magnitude Requests for Additional Information | ||
- HTVL data used for initial calibration of VISTA correlation | |||
-HTVL data used for initial calibration of VISTA correlation | * Reynolds scaling illustrates wider relevance of available data | ||
*Reynolds scaling illustrates wider relevance of available data | * Alternate quantification of realistic response for model uncertainty | ||
*Alternate quantification of realistic response for model uncertainty | - Strainer performance data used for initial L* (L-star) | ||
-Strainer performance data used for initial L* (L-star) | * Additive description of chemical head loss | ||
*Additive description of chemical head loss | * New interpretation of limited data Audit | ||
*New interpretation of limited data | - STP committed to develop and apply L* additive chemical approach | ||
- NRC emphasized need for head-loss data under representative performance conditions 3 | |||
-NRC emphasized need for head-loss data under representative performance conditions 3 | |||
=== | |||
Background=== | |||
* LAR calculates Total Head Loss (THL) head loss as follows: | |||
THL = 5 X H X M; where: | |||
- H is from NUREG/CR-6224 using theoretical compression | |||
- M is a chemical effects multiplier conditioned on break size, bed thickness, and sump temperature | |||
* Revised approach THL = NCHL + CHL; where: | |||
- NCHL is calculated using VISTA head loss | |||
- CHL is chemical head loss based on L* head loss 4 | |||
High-Level Plan for Test and Analysis | High-Level Plan for Test and Analysis | ||
*New horizontal flume at UNM to test full-scale strainer module (January shakedown) | * New horizontal flume at UNM to test full-scale strainer module (January shakedown) | ||
*Four, multi-day tests (finished end of March) | * Four, multi-day tests (finished end of March) | ||
*Data refine and validate L* additive chemical *Data calibrate VISTA correlation of strainer response*Schedule supports current resolution plan 5 | * Data refine and validate L* additive chemical P | ||
* Data calibrate VISTA correlation of strainer response | |||
* Schedule supports current resolution plan 5 | |||
Application of Test Results | Application of Test Results | ||
*STP closure path is based on analytic evaluation of full accident spectrum with quantitative understanding of uncertainty | * STP closure path is based on analytic evaluation of full accident spectrum with quantitative understanding of uncertainty | ||
*VISTA correlation of HTVL data will be compared to nonchemical strainer response | * VISTA correlation of HTVL data will be compared to nonchemical strainer response | ||
-Porosity controlled by compaction is the only factor lacking direct measurement (dominant uncertainty) | - Porosity controlled by compaction is the only factor lacking direct measurement (dominant uncertainty) | ||
*Refined L* for chemical head-loss increment will be added to VISTA predictions to obtain total head loss | * Refined L* for chemical head-loss increment will be added to VISTA predictions to obtain total head loss | ||
*Tests provide calibration of L* and validation of VISTA to STP strainer response | * Tests provide calibration of L* and validation of VISTA to STP strainer response | ||
*Tests provide validation of composite analytic evaluation to actual STP strainer response 6 | * Tests provide validation of composite analytic evaluation to actual STP strainer response 6 | ||
Available Test Data | Available Test Data | ||
*Existing STP HTVL tests (Alion) | * Existing STP HTVL tests (Alion) | ||
-fiber and particulates only | - fiber and particulates only | ||
*Existing STP flume tests (ARL) | * Existing STP flume tests (ARL) | ||
-fiber, particulates and WCAP surrogate | - fiber, particulates and WCAP surrogate | ||
*Existing and planned Vogtle HTVL tests (UNM) | * Existing and planned Vogtle HTVL tests (UNM) | ||
-fiber, coatings and WCAP surrogate | - fiber, coatings and WCAP surrogate | ||
*Existing | * Existing Sv characterization (UNM) | ||
*Planned STP strainer tests (UNM) 7 Available Data Assessment | * Planned STP strainer tests (UNM) 7 | ||
*Previous strainer qualification testing | |||
-Some tests meet debris transport goals | Available Data Assessment | ||
-No tests with revised mass ratios | * Previous strainer qualification testing | ||
-All tests with 120F tap water | - Some tests meet debris transport goals | ||
-All tests with WCAP-16530 surrogate chemical | - No tests with revised mass ratios | ||
*Alion HTVL tests with diverse loading | - All tests with 120F tap water | ||
-Used for initial calibration of VISTA correlation | - All tests with WCAP-16530 surrogate chemical | ||
-Concerns about | * Alion HTVL tests with diverse loading | ||
*No chemical products of concern were identified during prototypical testing 8 | - Used for initial calibration of VISTA correlation | ||
- Concerns about nonprototypic bed formation | |||
* No chemical products of concern were identified during prototypical testing 8 | |||
Motivation for Testing | Motivation for Testing | ||
*Additional data needed to support L*, additive chemical head loss method | * Additional data needed to support L*, additive chemical head loss method | ||
-Most likely, low chemical loads not well characterized | - Most likely, low chemical loads not well characterized | ||
-Additional debris + chemical combinations needed | - Additional debris + chemical combinations needed | ||
*Demonstrate physical connection between Reynolds scaling of VISTA and plant flow conditions | * Demonstrate physical connection between Reynolds scaling of VISTA and plant flow conditions | ||
-Measure Re of debris-loaded strainer (with uncertainty) | - Measure Re of debris-loaded strainer (with uncertainty) | ||
-Identify any gaps in HTVL database | - Identify any gaps in HTVL database | ||
*Quantify magnitude and causes of uncertainty between analytic head-loss evaluation and strainer module performance | * Quantify magnitude and causes of uncertainty between analytic head-loss evaluation and strainer module performance | ||
*Obtain performance data at the transition to potential strainer failure (most effect on risk) 9 Current L* Additive | * Obtain performance data at the transition to potential strainer failure (most effect on risk) 9 | ||
Current L* Additive Chem Head Loss 10 0 | |||
1 2 | |||
3 4 | |||
*Focus batch resolution on low concentrations | 5 6 | ||
*Check L* envelope with alternate conventional | 7 8 | ||
9 10 0 | |||
500 1000 1500 2000 2500 3000 CHL (ft) | |||
L* (g/m2) | |||
-Calibrate factor of 5 to actual percentiles of variation | STP strainer test data Correlation Illustrates analytic methodology for data interpretation Prior tests useful for uncertainty quantification Not based on current debris loads Not designed to support L* quantification | ||
Generate Additional L* Data | |||
* Focus batch resolution on low concentrations | |||
* Check L* envelope with alternate conventional beds 11 0 | |||
1 2 | |||
*Model for conventional debris head loss | 3 4 | ||
*Familiar scaling for a range of flow conditions | 5 6 | ||
*In a flume test: | 7 8 | ||
-Constant particle-to-fiber mass ratio | 9 10 0 | ||
-Water properties known from in-situ characterization | 500 1000 1500 2000 2500 3000 CHL (ft) | ||
-Velocity known by pump flow measurement | L* (g/m2) | ||
-ONLY average bed porosity and bed thickness across strainer are UNKNOWN | STP strainer test data Correlation Hypothetical Trends | ||
*Formal uncertainty propagation can be used to calibrate the uncertainty factor applied to all predictions (like defining the | |||
*FTA-000 (Shakedown) | Purpose of VISTA Reynolds scaling provides common basis for comparing all available data Common basis essential to select, define, defend desired tests Common basis essential to demonstrate testing sufficiency Rigorous treatment of residual uncertainty (compression) | ||
*FTA-100 (Clean Strainer) | - Calibrate factor of 5 to actual percentiles of variation Provides correlation to strainer data under representative performance conditions Addresses recognized analytic deficiencies of NUREG/CR-6224 Provides alternate view of real behavior to judge model uncertainty Correlation is essential to diagnose and evaluate subtle interactions in accident space Correlation is essential to accurately associate infinite debris combinations Final application to risk quantification will fully acknowledge uncertainties 12 | ||
*FTA-200 (1/ | |||
*FTA-300 (1/ | VISTA Uncertainty Quantification | ||
*FTA-400 (DBA load) | * Model for conventional debris head loss | ||
*Exact loads to be determined by CASA Grande spectrum analysis | * Familiar scaling for a range of flow conditions | ||
*Intermediate batches in FTA-200 will help define threshold for FTA-300 14 High-Level Test Description | * In a flume test: | ||
*Strainer module testing using protocols similar to those used in the STP 2008 flume tests | - Constant particle-to-fiber mass ratio | ||
*4 tests with an STP module in a flume facility | - Water properties known from in-situ characterization | ||
-1 clean strainer + 3 debris/ | - Velocity known by pump flow measurement | ||
*Target steady state test conditions emphasize maximum plant vulnerability (minimum NPSHmargin)-Maximum flow rate and temperature similar to time of recirculation | - ONLY average bed porosity and bed thickness across strainer are UNKNOWN | ||
*Two Steps: (1) conventional debris + (2) chemical product | * Formal uncertainty propagation can be used to calibrate the uncertainty factor applied to all predictions (like defining the 95th percentile) 13 | ||
-Temperature and velocity sweep before chemical addition | |||
*Debris tests incorporate prototypical amounts of particulate (e.g. paint from STP reduced inventory) | Planned FIESTA Tests | ||
*Debris tests use incremental additions of WCAP chemicals based on 30 days of precipitate formation | * FTA-000 (Shakedown) | ||
-L* head loss per area per chemical added across full conc. range 15 Typical Flow Sweep 16 | * FTA-100 (Clean Strainer) | ||
* FTA-200 (1/4th inch contiguous bed) | |||
*Standard external preparation will be adopted for consistency with industry practice | * FTA-300 (1/16th inch thin bed) | ||
-Standard external preparation is not likely to produce realistic chemical products or quantities -difficult to judge uncertainty | * FTA-400 (DBA load) | ||
*Standard room temperature settling/ storage/mixing procedures | * Exact loads to be determined by CASA Grande spectrum analysis | ||
*Introduction to higher temperature flume | * Intermediate batches in FTA-200 will help define threshold for FTA-300 14 | ||
-Bench tests will quantify possible redissolution | |||
-Compensate mass inventory to preserve total solid 17 Chemical Corrosion Inventory | High-Level Test Description | ||
*Chemical batches added to pre-established fiber and particulate bed | * Strainer module testing using protocols similar to those used in the STP 2008 flume tests | ||
*Batches provide incremental response independent of total inventory added | * 4 tests with an STP module in a flume facility | ||
*Finer batch resolution will capture: | - 1 clean strainer + 3 debris/chem series | ||
-First 2-3 days of potential passivation (UNM) day inventory (UNM corrosion) | * Target steady state test conditions emphasize maximum plant vulnerability (minimum NPSHmargin) | ||
*Coarse batch resolution will capture: day inventory (x5 UNM corrosion) day inventory (WCAP corrosion) 18 External Chemical Preparation 19 FIESTA Facility Description | - Maximum flow rate and temperature similar to time of recirculation | ||
*Use of STP strainer module | * Two Steps: (1) conventional debris + (2) chemical product | ||
*Polycarbonate channel custom-built to achieve representative approach velocity*Procedures to encourage near 100% | - Temperature and velocity sweep before chemical addition | ||
*Dimensions: 32 (L) x 6 (H) x 4 (W)*Polycarbonate walls with steel structure and support system | * Debris tests incorporate prototypical amounts of particulate (e.g. paint from STP reduced inventory) | ||
*Inline heating | * Debris tests use incremental additions of WCAP chemicals based on 30 days of precipitate formation | ||
*Multiple drains on flume floor to track debris | - L* head loss per area per chemical added across full conc. range 15 | ||
*Temperature Range: 25 C to 85 C (nominal test operation at 55 C) | |||
-Temperature cycling possible | Typical Flow Sweep 16 Rates based on flume heat exchange Min/max P variation limited to 25% of steady Add more debris if bed does not return to prior P | ||
*Prepared chemical precipitates added via inline system from auxiliary tank | |||
*Debris added using industry standard methods*Intent to achieve near 100% debris transport 22 FIESTA Primary | WCAP-16530 Surrogate | ||
* Standard external preparation will be adopted for consistency with industry practice | |||
- Standard external preparation is not likely to produce realistic chemical products or quantities - difficult to judge uncertainty | |||
*Instrument operation/calibration | * Standard room temperature settling/ | ||
*Perfect and train debris preparation/storage | storage/mixing procedures | ||
*Perfect and train | * Introduction to higher temperature flume | ||
*Perfect and train cleaning procedures | - Bench tests will quantify possible redissolution | ||
*Demonstrate near 100% debris transport | - Compensate mass inventory to preserve total solid 17 | ||
-Narrow flume | |||
-Mild agitation | Chemical Corrosion Inventory | ||
-No bed disturbance | * Chemical batches added to pre-established fiber and particulate bed | ||
-Post test fiber recovery for transport calibration 24 FTA-100 (Clean Strainer) | * Batches provide incremental response independent of total inventory added | ||
*Objectives: | * Finer batch resolution will capture: | ||
-VISTA correlation for clean strainer using different fluids | - First 2-3 days of potential passivation (UNM) day inventory (UNM corrosion) | ||
*Sequential phases of one test: | * Coarse batch resolution will capture: day inventory (x5 UNM corrosion) day inventory (WCAP corrosion) 18 | ||
-DI water-DI water + baseline | |||
-DI water + baseline + chem surrogate | External Chemical Preparation 19 | ||
*Procedure: | |||
-Establish fluid condition | FIESTA Facility Description | ||
-Vary temperature and velocity | * Use of STP strainer module | ||
*Benefit:-Reliable interpretation of composite head loss | * Polycarbonate channel custom-built to achieve representative approach velocity | ||
-Possible direct measurement of fluid viscosity and density 25 FTA-200 (1/ | * Procedures to encourage near 100% transport STP Strainer Module from Alden Test (2008) 20 | ||
*Objectives: | |||
-Strainer performance near lower limit of contiguous bed (most likely condition) | FIESTA Facility Description | ||
-Assess filtration transition during loading (use in FTA-300) | * Dimensions: 32 (L) x 6 (H) x 4 (W) | ||
-Establish L* for alternate bed configuration | * Polycarbonate walls with steel structure and support system | ||
*Sequential phases of one test: | * Inline heating | ||
-Batch addition of premixed fiber + particulate | * Multiple drains on flume floor to track debris transport UNM FIESTA Facility STRAINER POLYCARBONATE CHANNEL WALLS DRAINS 21 | ||
-Batch addition of prepared chemical surrogate | |||
*General Procedure: | FIESTA Facility Description | ||
-Establish fluid condition | * Temperature Range: 25 C to 85 C (nominal test operation at 55 C) | ||
-Incremental debris addition | - Temperature cycling possible | ||
-Flow sweep | * Prepared chemical precipitates added via inline system from auxiliary tank | ||
-Incremental chemical product addition 26 FTA-300 (1/ | * Debris added using industry standard methods | ||
*Objectives: | * Intent to achieve near 100% debris transport 22 | ||
-Dominant risk condition if adverse response | |||
-Establish L* for alternate bed configuration | FIESTA Primary Instrumentation Diagnostic Purpose Flume Sampling Frequency Mode Volumetric flow rate Face velocity on the test module 0.1 to 0.02 Hz (every 10 to 50s) | ||
*Sequential phases of one test: | Online Differential Pressure Array Hydraulic loss through the debris bed. Clean strainer response along the module. | ||
-Batch addition of premixed fiber + particulate | matched with flow samples Online Static pool pressure Fluid density in combination with level matched with flow samples Online Liquid Temperature Fluid properties, pH correction matched with flow samples Online Room Temperature Differential pressure correction matched with flow samples Online Atmospheric Pressure Pump NPSH Once per 4 hours or as specified in test plan Spot Read Liquid Level Fluid density, chemical conc, water make up. | ||
-Batch addition of prepared chemical surrogate | 4 times per hour or as specified in test plan Online or Spot Read Total pipe volume Chemical conc. | ||
*General Procedure: | NA once pH Chemical debris preparation and flume test conditions Once per 4 hours after first chemical add or as specified in test plan Bench Reading ICP Flume concentration for mass balance Once per 4 hours after first chemical add, or as specified in test plan Grab Sample Mass balance Milligram to kg accuracy for surrogate chemical preparation NA As needed Particle sizing Characterize surrogate chemical product NA As needed Light table Verify debris preparation NA Each debris batch 23 | ||
-Establish fluid condition | |||
-Incremental debris addition | FTA-000 (Shakedown) | ||
-Flow sweep | * Instrument operation/calibration | ||
-Incremental chemical product addition 27 FTA-400 (DBA Load) | * Perfect and train debris preparation/storage | ||
*Objectives: | * Perfect and train chem preparation/storage | ||
-Compare results to previous ARL test under similar conditions | * Perfect and train cleaning procedures | ||
-Assess degree of uncertainty in L* for extreme debris conditions | * Demonstrate near 100% debris transport | ||
*Sequential phases of one test: | - Narrow flume | ||
-Batch addition of premixed fiber + particulate | - Mild agitation | ||
-Batch addition of prepared chemical surrogate | - No bed disturbance | ||
*General Procedure: | - Post test fiber recovery for transport calibration 24 | ||
-Establish fluid condition | |||
-Incremental debris addition | FTA-100 (Clean Strainer) | ||
-Flow sweep | * Objectives: | ||
-Incremental chemical product addition 28}} | - VISTA correlation for clean strainer using different fluids | ||
* Sequential phases of one test: | |||
- DI water | |||
- DI water + baseline | |||
- DI water + baseline + chem surrogate | |||
* Procedure: | |||
- Establish fluid condition | |||
- Vary temperature and velocity | |||
* Benefit: | |||
- Reliable interpretation of composite head loss | |||
- Possible direct measurement of fluid viscosity and density 25 | |||
FTA-200 (1/4th in. thin bed) | |||
* Objectives: | |||
- Strainer performance near lower limit of contiguous bed (most likely condition) | |||
- Assess filtration transition during loading (use in FTA-300) | |||
- Establish L* for alternate bed configuration | |||
* Sequential phases of one test: | |||
- Batch addition of premixed fiber + particulate | |||
- Batch addition of prepared chemical surrogate | |||
* General Procedure: | |||
- Establish fluid condition | |||
- Incremental debris addition | |||
- Flow sweep | |||
- Incremental chemical product addition 26 | |||
FTA-300 (1/16th in. thin bed) | |||
* Objectives: | |||
- Dominant risk condition if adverse response | |||
- Establish L* for alternate bed configuration | |||
* Sequential phases of one test: | |||
- Batch addition of premixed fiber + particulate | |||
- Batch addition of prepared chemical surrogate | |||
* General Procedure: | |||
- Establish fluid condition | |||
- Incremental debris addition | |||
- Flow sweep | |||
- Incremental chemical product addition 27 | |||
FTA-400 (DBA Load) | |||
* Objectives: | |||
- Compare results to previous ARL test under similar conditions | |||
- Assess degree of uncertainty in L* for extreme debris conditions | |||
* Sequential phases of one test: | |||
- Batch addition of premixed fiber + particulate | |||
- Batch addition of prepared chemical surrogate | |||
* General Procedure: | |||
- Establish fluid condition | |||
- Incremental debris addition | |||
- Flow sweep | |||
- Incremental chemical product addition 28}} | |||
Latest revision as of 16:02, 10 January 2025
| ML14315A087 | |
| Person / Time | |
|---|---|
| Site: | South Texas |
| Issue date: | 11/04/2014 |
| From: | Harrison A South Texas |
| To: | Balwant Singal Division of Operating Reactor Licensing |
| References | |
| Download: ML14315A087 (30) | |
Text
1 NRR-PMDAPEm Resource From:
Harrison Albon [awharrison@STPEGS.COM]
Sent:
Tuesday, November 04, 2014 4:45 PM To:
Singal, Balwant; Stang, John
Subject:
STP Slides for 11/6/14 Public Phone Call Attachments:
STP Head-Loss Testing for Addressing GSI-191 - 110614 - Final.pdf
Hearing Identifier:
NRR_PMDA Email Number:
1681 Mail Envelope Properties (8C918BCF8596FB49BD20A610FA5920CF02182452)
Subject:
STP Slides for 11/6/14 Public Phone Call Sent Date:
11/4/2014 4:44:54 PM Received Date:
11/4/2014 4:46:33 PM From:
Harrison Albon Created By:
awharrison@STPEGS.COM Recipients:
"Singal, Balwant" <Balwant.Singal@nrc.gov>
Tracking Status: None "Stang, John" <John.Stang@nrc.gov>
Tracking Status: None Post Office:
CEXMBX04.CORP.STPEGS.NET Files Size Date & Time MESSAGE 3
11/4/2014 4:46:33 PM STP Head-Loss Testing for Addressing GSI-191 - 110614 - Final.pdf 668820 Options Priority:
Standard Return Notification:
No Reply Requested:
No Sensitivity:
Normal Expiration Date:
Recipients Received:
STP Strainer Testing to Address GSI-191 South Texas Project Nuclear Operating Company Alion Science and Technology University of New Mexico Thursday, November 6, 2014 1
Desired Outcome
- Establish common understanding of STP strainer tests
- Purpose and scope
- Procedures
- Facility and diagnostics
- Identify and understand NRC staff issues with test plan
- Focus continued discussion for resolution of issues in follow-on public meeting 2
Review of STP RIR Head Loss Approach Current Licensing Amendment Request
- Modified NUREG/CR-6224 correlation for conventional P
- Challenged on bases for: inconsistent derivation, inconsistent prediction, uncertainty assessment (x5)
- Exponential factors for chemical P
- Challenged on multiplicative effect and bases for S,M,L magnitude Requests for Additional Information
- HTVL data used for initial calibration of VISTA correlation
- Reynolds scaling illustrates wider relevance of available data
- Alternate quantification of realistic response for model uncertainty
- Strainer performance data used for initial L* (L-star)
- Additive description of chemical head loss
- New interpretation of limited data Audit
- STP committed to develop and apply L* additive chemical approach
- NRC emphasized need for head-loss data under representative performance conditions 3
=
Background===
- LAR calculates Total Head Loss (THL) head loss as follows:
THL = 5 X H X M; where:
- H is from NUREG/CR-6224 using theoretical compression
- M is a chemical effects multiplier conditioned on break size, bed thickness, and sump temperature
- Revised approach THL = NCHL + CHL; where:
- NCHL is calculated using VISTA head loss
- CHL is chemical head loss based on L* head loss 4
High-Level Plan for Test and Analysis
- New horizontal flume at UNM to test full-scale strainer module (January shakedown)
- Four, multi-day tests (finished end of March)
- Data refine and validate L* additive chemical P
- Data calibrate VISTA correlation of strainer response
- Schedule supports current resolution plan 5
Application of Test Results
- STP closure path is based on analytic evaluation of full accident spectrum with quantitative understanding of uncertainty
- VISTA correlation of HTVL data will be compared to nonchemical strainer response
- Porosity controlled by compaction is the only factor lacking direct measurement (dominant uncertainty)
- Refined L* for chemical head-loss increment will be added to VISTA predictions to obtain total head loss
- Tests provide calibration of L* and validation of VISTA to STP strainer response
- Tests provide validation of composite analytic evaluation to actual STP strainer response 6
Available Test Data
- Existing STP HTVL tests (Alion)
- fiber and particulates only
- Existing STP flume tests (ARL)
- fiber, particulates and WCAP surrogate
- Existing and planned Vogtle HTVL tests (UNM)
- fiber, coatings and WCAP surrogate
- Existing Sv characterization (UNM)
- Planned STP strainer tests (UNM) 7
Available Data Assessment
- Previous strainer qualification testing
- Some tests meet debris transport goals
- No tests with revised mass ratios
- All tests with 120F tap water
- All tests with WCAP-16530 surrogate chemical
- Alion HTVL tests with diverse loading
- Used for initial calibration of VISTA correlation
- Concerns about nonprototypic bed formation
- No chemical products of concern were identified during prototypical testing 8
Motivation for Testing
- Additional data needed to support L*, additive chemical head loss method
- Most likely, low chemical loads not well characterized
- Additional debris + chemical combinations needed
- Demonstrate physical connection between Reynolds scaling of VISTA and plant flow conditions
- Measure Re of debris-loaded strainer (with uncertainty)
- Identify any gaps in HTVL database
- Quantify magnitude and causes of uncertainty between analytic head-loss evaluation and strainer module performance
- Obtain performance data at the transition to potential strainer failure (most effect on risk) 9
Current L* Additive Chem Head Loss 10 0
1 2
3 4
5 6
7 8
9 10 0
500 1000 1500 2000 2500 3000 CHL (ft)
L* (g/m2)
STP strainer test data Correlation Illustrates analytic methodology for data interpretation Prior tests useful for uncertainty quantification Not based on current debris loads Not designed to support L* quantification
Generate Additional L* Data
- Focus batch resolution on low concentrations
- Check L* envelope with alternate conventional beds 11 0
1 2
3 4
5 6
7 8
9 10 0
500 1000 1500 2000 2500 3000 CHL (ft)
L* (g/m2)
STP strainer test data Correlation Hypothetical Trends
Purpose of VISTA Reynolds scaling provides common basis for comparing all available data Common basis essential to select, define, defend desired tests Common basis essential to demonstrate testing sufficiency Rigorous treatment of residual uncertainty (compression)
- Calibrate factor of 5 to actual percentiles of variation Provides correlation to strainer data under representative performance conditions Addresses recognized analytic deficiencies of NUREG/CR-6224 Provides alternate view of real behavior to judge model uncertainty Correlation is essential to diagnose and evaluate subtle interactions in accident space Correlation is essential to accurately associate infinite debris combinations Final application to risk quantification will fully acknowledge uncertainties 12
VISTA Uncertainty Quantification
- Model for conventional debris head loss
- Familiar scaling for a range of flow conditions
- In a flume test:
- Constant particle-to-fiber mass ratio
- Water properties known from in-situ characterization
- Velocity known by pump flow measurement
- ONLY average bed porosity and bed thickness across strainer are UNKNOWN
- Formal uncertainty propagation can be used to calibrate the uncertainty factor applied to all predictions (like defining the 95th percentile) 13
Planned FIESTA Tests
- FTA-000 (Shakedown)
- FTA-100 (Clean Strainer)
- FTA-200 (1/4th inch contiguous bed)
- FTA-300 (1/16th inch thin bed)
- FTA-400 (DBA load)
- Exact loads to be determined by CASA Grande spectrum analysis
- Intermediate batches in FTA-200 will help define threshold for FTA-300 14
High-Level Test Description
- Strainer module testing using protocols similar to those used in the STP 2008 flume tests
- 4 tests with an STP module in a flume facility
- 1 clean strainer + 3 debris/chem series
- Target steady state test conditions emphasize maximum plant vulnerability (minimum NPSHmargin)
- Maximum flow rate and temperature similar to time of recirculation
- Two Steps: (1) conventional debris + (2) chemical product
- Temperature and velocity sweep before chemical addition
- Debris tests incorporate prototypical amounts of particulate (e.g. paint from STP reduced inventory)
- Debris tests use incremental additions of WCAP chemicals based on 30 days of precipitate formation
- L* head loss per area per chemical added across full conc. range 15
Typical Flow Sweep 16 Rates based on flume heat exchange Min/max P variation limited to 25% of steady Add more debris if bed does not return to prior P
WCAP-16530 Surrogate
- Standard external preparation will be adopted for consistency with industry practice
- Standard external preparation is not likely to produce realistic chemical products or quantities - difficult to judge uncertainty
- Standard room temperature settling/
storage/mixing procedures
- Introduction to higher temperature flume
- Bench tests will quantify possible redissolution
- Compensate mass inventory to preserve total solid 17
Chemical Corrosion Inventory
- Chemical batches added to pre-established fiber and particulate bed
- Batches provide incremental response independent of total inventory added
- Finer batch resolution will capture:
- First 2-3 days of potential passivation (UNM) day inventory (UNM corrosion)
- Coarse batch resolution will capture: day inventory (x5 UNM corrosion) day inventory (WCAP corrosion) 18
External Chemical Preparation 19
FIESTA Facility Description
- Use of STP strainer module
- Polycarbonate channel custom-built to achieve representative approach velocity
- Procedures to encourage near 100% transport STP Strainer Module from Alden Test (2008) 20
FIESTA Facility Description
- Dimensions: 32 (L) x 6 (H) x 4 (W)
- Polycarbonate walls with steel structure and support system
- Inline heating
- Multiple drains on flume floor to track debris transport UNM FIESTA Facility STRAINER POLYCARBONATE CHANNEL WALLS DRAINS 21
FIESTA Facility Description
- Temperature Range: 25 C to 85 C (nominal test operation at 55 C)
- Temperature cycling possible
- Prepared chemical precipitates added via inline system from auxiliary tank
- Debris added using industry standard methods
- Intent to achieve near 100% debris transport 22
FIESTA Primary Instrumentation Diagnostic Purpose Flume Sampling Frequency Mode Volumetric flow rate Face velocity on the test module 0.1 to 0.02 Hz (every 10 to 50s)
Online Differential Pressure Array Hydraulic loss through the debris bed. Clean strainer response along the module.
matched with flow samples Online Static pool pressure Fluid density in combination with level matched with flow samples Online Liquid Temperature Fluid properties, pH correction matched with flow samples Online Room Temperature Differential pressure correction matched with flow samples Online Atmospheric Pressure Pump NPSH Once per 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> or as specified in test plan Spot Read Liquid Level Fluid density, chemical conc, water make up.
4 times per hour or as specified in test plan Online or Spot Read Total pipe volume Chemical conc.
NA once pH Chemical debris preparation and flume test conditions Once per 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> after first chemical add or as specified in test plan Bench Reading ICP Flume concentration for mass balance Once per 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> after first chemical add, or as specified in test plan Grab Sample Mass balance Milligram to kg accuracy for surrogate chemical preparation NA As needed Particle sizing Characterize surrogate chemical product NA As needed Light table Verify debris preparation NA Each debris batch 23
FTA-000 (Shakedown)
- Instrument operation/calibration
- Perfect and train debris preparation/storage
- Perfect and train chem preparation/storage
- Perfect and train cleaning procedures
- Demonstrate near 100% debris transport
- Narrow flume
- Mild agitation
- No bed disturbance
- Post test fiber recovery for transport calibration 24
FTA-100 (Clean Strainer)
- Objectives:
- VISTA correlation for clean strainer using different fluids
- Sequential phases of one test:
- DI water
- DI water + baseline
- DI water + baseline + chem surrogate
- Procedure:
- Establish fluid condition
- Vary temperature and velocity
- Benefit:
- Reliable interpretation of composite head loss
- Possible direct measurement of fluid viscosity and density 25
FTA-200 (1/4th in. thin bed)
- Objectives:
- Strainer performance near lower limit of contiguous bed (most likely condition)
- Assess filtration transition during loading (use in FTA-300)
- Establish L* for alternate bed configuration
- Sequential phases of one test:
- Batch addition of premixed fiber + particulate
- Batch addition of prepared chemical surrogate
- General Procedure:
- Establish fluid condition
- Incremental debris addition
- Flow sweep
- Incremental chemical product addition 26
FTA-300 (1/16th in. thin bed)
- Objectives:
- Dominant risk condition if adverse response
- Establish L* for alternate bed configuration
- Sequential phases of one test:
- Batch addition of premixed fiber + particulate
- Batch addition of prepared chemical surrogate
- General Procedure:
- Establish fluid condition
- Incremental debris addition
- Flow sweep
- Incremental chemical product addition 27
FTA-400 (DBA Load)
- Objectives:
- Compare results to previous ARL test under similar conditions
- Assess degree of uncertainty in L* for extreme debris conditions
- Sequential phases of one test:
- Batch addition of premixed fiber + particulate
- Batch addition of prepared chemical surrogate
- General Procedure:
- Establish fluid condition
- Incremental debris addition
- Flow sweep
- Incremental chemical product addition 28