Watts Bar Unit 1 A2 Feedwater Heater Partition Plate Weld Failure

Similar documents
2017 FSRUG Thermal Performance Feedwater Heater Troubleshooting FSRUG FWH Troubleshooting 1

What to Expect from Your EtaPRO Investment

ICONE DRAFT Proceedings of the 16th International Conference on Nuclear Engineering ICONE16 May 11-15, 2008, Orlando, Florida, USA

Seabrook Station Condenser Tube Leaks. Jim Johnson Seabrook Station FSRUG 2017

Chapter 11. Design of Other BOP

POWERENERGY

LIFE MANAGEMENT OF FEEDWATER HEATERS AT KCPL

Steam Power Cycles Part II

HEAT EXCHANGE INSTITUTE, INC.

PALO VERDE NUCLEAR GENERATING STATION

Boiler Basics. Design and operation

Kube Engineering. Industry Guide. Power Industry

PV Newsletter Monthly Publication from CoDesign Engineering Skills Academy

LONGEVITY SOLUTIONS FEEDWATER HEATERS CONDENSERS HEAT EXCHANGERS PRESSURE VESSELS AIR PREHEATERS ISOLATION DAMPERS AFTERMARKET SERVICES AND PARTS

ANNEX V. AP600 & AP1000 Westinghouse Electric, USA

9707 Key West Avenue, Suite 100 Rockville, MD Phone: Fax:

Foster Wheeler Condensers and Feedwater Heaters. High Quality Steam Components

CHAPTER 5 CONDENSER AND EVAPORATIVE COOLING TOWER

Optimizing Strategy for Boiler Drum Level Control

CONSIDERATIONS IN CONVERTING A DUAL SHELL OR A DUAL PRESSURE COAL FIRED PLANT CONDENSER INTO A COMBINED CYCLE PLANT CONDENSER

Understanding Site Hazards

POWER Selecting Shell Side Design Temperature for Feedwater Heaters

MECHANICAL SCIENCE Module 2 Heat Exchangers

Feed Water Heaters Performance Indicators and Characteristics on the 405MW Coal-Thermal Power Plant

HumidiPack,HumidiPackPlus and HumidiPackPlus CF Steam Humidifier Systems

POWERENERGY

Secondary Systems: Condensate/Feedwater Cycle

Reactor-Boiler and Auxiliaries - Course 433 BOILER STEAM AND WATER SYSTEMS

Convection is the heat transfer by the macroscopic movement of a fluid, such as a car's engine kept cool by the water in the cooling system.

Appendix B3 System/Component Cause Codes

Information on selection of an economizer, and resulting payback due to changes in inlet water temperature.

"ESDDR" Series Electric Humidifier

Cold Weather Preparedness Plant Winterization Lessons Learned & Best Practices

Math & Physics. Complete combustion requires an Air-FuelRatio of 14.7 to 1 for combustion.

Product portfolio A one-stop-shop for industrial cooling products and developments

MODULATING CONTROL OF LOW NO X BURNERS

MECHANICAL SCIENCE Module 2 Heat Exchangers

Heat Exchanger Excellence DESIGN BUILD SUPPLY INSTALL MAINTAIN.

WELCOME TO THE AWT REGIONAL TRAINING PROGRAM

CONDENSER TUBE COMPARISON WINYAH 2. Leif Svensen P.E. Santee Cooper One Riverwood Drive Moncks Corner, SC 29461

OPERATION & MAINTENANACE MANUAL

BORSIG WASTE HEAT BOILERS FOR NITRIC ACID, CAPROLACTAM AND FORMALDEHYDE PLANTS PROCESS HEAT EXCHANGER. A Member of KNM Group Berhad

CHAPTER 3 BASIC STEAM CYCLE

Circulation Heaters. To order, call or shop online at omega.com SM. CHF Series

Condenser Vacuum Improvement and Related Parametric Analysis: A Case Study on A 120MW Thermal Power Plant

Steam and Power Conversion System

MULTI-CHANNEL R134A TWO-PHASE FLOW MEASUREMENT TECHNIQUE FOR AUTOMOBILE AIR-CONDITIONING SYSTEM

Enhancing Black liquor Evaporation capacity through Process Reengineering

Solution of I Mid Term Steam Engineering 6ME5A

Catawba Nuclear Station Delay Coil Chemical Decon Projects

Influence of Feed Water Heaters on the Performance of Coal Fired Power Plants

A Newsletter published by ESI. The Steam and Power SPECIAL FORCES

the NC gases and the partial pressure Pv of the water vapor. Then, (1) Pt = Pnc + Pv Also, M v M nc

Steam System Best Practices Document No. 11

MU053: CHILLERS: Operation & Maintenance of Chilled Water Systems

Chapter 10 VAPOR AND COMBINED POWER CYCLES

Speransa 2008: Round table: Nuclear and sustainable development Universitad Politecnica de Valencia \UPV - Passive safety systems -

H O B O K E N R E S I D E N T I A L

A Long Experience in Energy Equipment and one Goal: The Customer s satisfaction. Heating Equipment and System

AUTOMATION OF BOILERS USING LABVIEW

I&C Upgradation and Modernization at CHASNUPP 1 & 2. Presented By: Waseem Uddin Farooqi PAEC, Pakistan

Heat traced pipe-in-pipe for S or J-lay proof of concept test results

Heater Inspection Guidelines

3.1 Deaerator Systems

Week 13 Chapter 10 Vapor & Combined Power Cycles

SHELL AND TUBE HEAT EXCHANGER (STHE) - part b

Homework #4 (group) Tuesday, 27 by 4:00 pm 5290 exercises (individual) Tuesday, 27 by 4:00 pm extra credit (individual) Tuesday, 27 by 4:00 pm

Enhancing Current Maintenance Practices 04. Managing the Risk 06. Constant Monitoring of Electrical Enclosures 08

FIFTH CLASS POWER ENGINEER S

The Condensate Water Systems

Marine Heat Exchangers SALES SERVICE REPAIR

Heat Transfer Equipment

9/18/2017. Nicholas Thornton, CEM. Systems: HVAC, Electrical, and Technology. Overview. Today s Goals Introductions HVAC Electrical Technology Q&A

UNFIRED STEAM GENERATORS STANDARD EQUIPMENT

Annex A-8 CONCENTRATED SOLAR POWER UNITS INDEX TO SYSTEM/COMPONENT CAUSE CODES

Innovate & Implement

CLASS POWER ENGINEER S CERTIFICATE

Efficient Steam System Design

Efficiency of Application the Condensing Heat Utilizers in the Existing Boiler's Unit in Heat Power Station

AC SYSTEM CONFIGURATION- CENTRAL CHILLER PLANT

Foreign Object Experience Update

SHELL AND TUBE HEAT EXCHANGERS FOR INDUSTRIAL ONCE-THROUGH COOLING SYSTEMS AND THE OCCURRENCE OF LEAKAGE

INSTRUCTION MANUAL CLEAN BELLOWS TYPE INDUSTRIAL ROBOT SPECIFICATIONS. Notice

BASCO U-TUBE & TANK IMMERSION HEAT EXCHANGERS. ...world leaders in heat transfer technology

ASH MEASUREMENT AT NRG HUNTLEY USING HIGH TEMPERATURE STRAIN GAUGES

PRESSURE-ENTHALPY CHARTS AND THEIR USE By: Dr. Ralph C. Downing E.I. du Pont de Nemours & Co., Inc. Freon Products Division

Falling Film Heat Exchangers for Solar Water Heaters

Presenter: Malcolm McLaughlin Date: 04/04/2019. A Review of Medical Device and Optical Critical Cleaning

Importance of Auditing/Reviewing Your Company s GADS Events

Boiler Basics: Design & Application Differences. Presented by Steve Connor July 30, 2014

BP Alaska GC-1. Design Review Project. January 2003

Steam The Primary Force

Circulation Heaters. To order, call or shop online at omega.com SM. CHF Series

A. ASHRAE Handbook HVAC Applications, Snow Melting and Freeze Protection

COMMERCIAL SOLAR SOLUTIONS

Thermodynamics II Chapter 5 Refrigeration

WHY THE REMOVAL OF NONCONDENSABLE GASES AND AIR IS CRITICAL IN A STEAM SYSTEM

Using HD-FOS for Characterizing Heat Exchangers. Case Study. Using HD-FOS for Characterizing Heat Exchangers

Brazil. Current status in NPP I&C and Discussion Topics. 24th Meeting of the IAEA TWG-NPPIC

On-line Side Stream Oil in Water Analyser - Model OIW-EX 100 or OIW-EX 1000

Transcription:

Watts Bar Unit 1 A2 Feedwater Heater Partition Plate Weld Failure

Watts Bar Unit 1 Feedwater Heating Overview Watts Bar Unit 1 is a PWR 4 Loop Westinghouse Design with a Siemens/Westinghouse Turbine/Generator Watts Bar Unit 1 began Commercial Operation in May 1996 The Watts Bar Unit 1 Condensate System consists of the following in terms of Feedwater Heating: 3 Feedwater Heater Strings/Trains (A, B, & C) comprised of 21 total Feedwater Heaters Each String consists of 3 Low Pressure Condensate Heaters (#5, #6, and #7) Each String consists of 3 Intermediate Condensate Heaters (#2, #3, and #4) Each String consists of 1 High Pressure Feedwater Heater (#1) 3 Condensate Booster Pumps 3 Hotwell Pumps 2 Turbine Driven and 1 Motor Drive Main Feedwater Pumps 3 Condensate Demineralized Pumps

Condensate Flow Drawing

Feedwater Flow Drawing

Thermal Performance Review Terminal Temperature Difference (TTD) Parameter used to evaluate a Feedwater Heater s performance related to Heat Transfer; TTD is the Saturation Temperature of the Extraction Steam minus the feedwater outlet temperature; Normal Operating TTD is 5 Deg F Tsat - TFW Out = TTD Drain Cooler Approach Temperature (DCA) Method used to validate Feedwater Heater levels; DCA is the difference between the drain cooler outlet and the feedwater inlet; Normal Operating DCA is 10 Deg F TDrains Out TFW In = DCA Feedwater Temperature Rise (FW ΔT) - FW ΔT is the difference between the feedwater outlet temperature and the feedwater inlet temperature; Normal FW ΔT is 40 Deg F TFW Out - TFW In = FW ΔT

Initial Event Discovery Information for 1A2 Feedwater Heater System Monitoring/Trending identified an adverse trend in the TTD associated with the 1A2 Feedwater Heater (Began in May 2012 when values increased to approximately 6 Deg F) Initial thoughts were the Thermocouple measuring Feedwater Outlet Temperature was failing

Troubleshooting and Additional Findings Adverse Trend in TTD continued to worsen to approximately 8.5 Deg F (January 2014) Feedwater Outlet Thermocouple was replaced and the condition did not change (March 2014) Eddy Current Testing scheduled for WBN U1C12 Refueling Outage (Spring 2014)

WBN U1C12 Refueling Outage During WBN U1C12 Refueling Outage (Spring 2014), Eddy Current Testing was performed on the 1A2 Feedwater Heater and as a result, 4 tubes were plugged During the Eddy Current Testing, a black, slippery substance was found on the inside of the tubes which was a result of solidifying of the following substances: Ethanolamine (ETA) Condensate Corrosion Inhibitor Iron No abnormalities were noted other than the ETA/Iron mixture that had plated out inside the tubes

WBN U1C13 Outage Preparations After WBN U1C12 Refueling Outage, the TTD worsened to approximately 10 Deg F Plans were made to re-open the 1A2 Feedwater Heater during WBN U1C13 Refueling Outage once extensive research was performed and the issue was better understood The troubleshooting plan consisted of the following: Engineering to Inspect the inlet tubesheet, inlet piping, and hemi-head (shell) before removing the Pass Partition Plate Cover Engineering to Inspect the outlet tubesheet, outlet piping, and hemi-head (shell) after removing the Pass Partition Plate Cover Vendor to clean the tubes using high pressure demineralized water (This was to clean the tubes prior to Eddy Current Testing) Obtain sample of black sludge to have tested by Chemistry Fill shell side of Feedwater Heater to ensure no tubes are leaking (Water would visually flow from the tubes depending on the location of leak) TVA Inspection Services to perform Ultrasonic Thickness Measurement TVA Inspection Services to perform Eddy Current Testing

WBN U1C13 Refueling Outage During Engineering Inspection with the Partition Plate Cover removed, a degraded weld was identified on the partition plate expansion joint (Found during Tube Cleaning for Eddy Current) 75% of the hemispherical weld on the expansion joint was eroded away which created a ¼ to ½ inch wide gap The degraded weld allowed a portion of the flow entering the 1A2 Feedwater Heater to pass through without gaining any heat load As a result, the performance/heat transfer associated with the 1A2 Feedwater Heater was accurately displayed in the TTD trends. The decision was made to grind out the degraded weld and re-weld back like the original design

Videos/Pictures of Weld Failure Video:

Pictures of the Weld Repair

Conclusion/Future Actions It is believed that the weld failed in the 1A2 Feedwater Heater due to an ineffective weld from the factory The 1B2 Feedwater Heater is scheduled for Eddy Current Testing during WBN U1C14 (Spring 2017) and a contingency work order will be planned to execute the same repairs if the same condition exists If the same condition exists in the 1B2 Feedwater Heater, a contingency will exist to also open the 1C2 Feedwater Heater instead of waiting until WBN U1C16 when it is scheduled for Eddy Current Testing The same condition is not believed to exist in the 1B2 or 1C2 Feedwater Heater because an adverse trend in TTD does not exist The current plan is to monitor the performance of the 1A2 Feedwater Heater until U1C20 (Spring 2026) when the next scheduled Eddy Current Testing will occur Corrective actions will be executed if the adverse TTD trend returns.

Questions?