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Raja Ratnam
20th Sept 2004
Optimising Capacity andOptimising Capacity and
Efficiency of Coal-Fired Power PlantsEfficiency of Coal-Fired Power Plants
BackgroundBackground
 Wholly owned subsidiary of ALSTOM Power
 Operates Independently
 Former Engineering Support Group for the QLD Utilities
 Over 48 Engineers & Scientists - Brisbane
 Covers 4 Sectors - Power, Mining, Petro-Chem & Processes
 Recent Major Projects -
 Owner’s Engineer in conjunction with PB Power for CS
Energy’s Kogan Creek 750MW supercritical coal-fired plant
 Shortlisted for the Collie 330MW O&M contract in WA
Presentation Objectives:
 Overview Business Environment
 Why Upgrades no longer an option ?
 Overview of some current Upgrade applications
 Why a Wholistic Approach ?
 Business Mentality - Optimise because you want BOTH at the
Same Time - Capacity & Efficiency
 IR impacting on business decisions
 New Environmental Regulations delayed
 Local Economy concerns only
 Liability - ring fenced to within operational boundary
 Government Owned Utilities - not profit driven
 Oversupplied market
 Plant generally within design life
Past Business Environment
 Meet Shareholder’s Demands - Maximise Profitability
Want Highest Capacity when Price is HIGH
Want Maximum Thermal Efficiency when Price is LOW
 Must have Reliability - minimise expensive hedging
 Positive Cash Flow
 No Risks
New Business Drivers
 Probability of Failures Increasing
Plant Ageing - more than 30 years old
Experienced Personnel numbers down - Attrition Rate
increasing Exponentially with Batch retirement
 Peak Demands critical - summer & winter
 Rapid growth in Technology and Options - too many choices ?
 Rising Class Action initiatives - 3rd party claims
 Foreign IPP’s exiting because of overseas issues
 Threat of Terrorism - unknown & unpredictable
 Community Environmental Attitude is Aggressive
 Capital is scarce - short payback
Current Business Environment
Why Upgrade?
Ageing Plant - Refurbish not enough !
 Impending Environmental Laws
 Greater Operating Flexibility - Maximise Profits
 Less People Dependent
 Minimise Business Risks
Capital is scarce
 Need higher ROI , shorter payback
 New technology for better returns
Regain Design Performance
Review Risk Management Strategies - eg redundant plant
Understand Plant Limits - use technology to improve
measurements and monitor degradation
Operate closer to limits - use technology
Real-time production strategy - capacity or efficiency ?
Include all costs for specific strategy - eg increase
maintenance
Before Upgrade - Back to Basics
How well is this Controller doing ?How well is this Controller doing ?
What is ProcessDoctor ?What is ProcessDoctor ?
ProcessDoctor is a software solution for automatic,
control loop performance assessment and
monitoring
BenefitsBenefits
Identify
Variability
Diagnose, Maintain to
Reduce
Variability
Move
Target
Benchmark, Monitor
& Sustain
Excessive process variability prevents operators from running the plant at or near its operating limits
or constraints.
time
throughput
Current Performance
Process Constraint
Optimal Performance
$
Other
900
35
180
25/40/35
5
Power
2000
65
350
25/40/35
8
PetroChem
1500
100
180
25/40/35
9
Oil & Gas
1200
50
220
25/40/35
6
EEMUA
144
9
10
80/15/5
1
Industry Findings - AlarmsIndustry Findings - Alarms
How many alarms do you get every day?
Average Alarms
per Day
Average Standing
Alarms
Peak Alarms
per 10 Minutes
Average Alarms/
10 Minute Interval
Distribution %
(Low/Med/High)
How many alarms do you get every day?
ProcessGuard is out-of-the-box Alarm Management
software that lets you:
•Seamlessly reduce nuisance alarms in
your control system
•Automatically:
•Collect & store alarm data
•Analyze and identify bad actors
• Remove bad actors
• Monitor to sustain results
•Increase uptime, increase equipment
reliability, and improve plant safety
Example
Condenser Performance ImprovementsCondenser Performance Improvements
 Maintain Tubes
 Early replacement - ECT surveys
 Maintain cleanliness - on line and off line, filtration
 Eliminate Shell Air Leakage
 Improve CW Flow stratification - tubes fully primed
 Improve Internal Steam Paths
 Maintain Air Extraction system
 On line Performance Monitoring - reduce variance - use
remote experts
TECHNOS
TCW is a Remote Monitoring & Control SystemTECHNOS
MONITOR & ANALYSE CONDENSER PERFORMANCE
TECHNOS
1
L o w p e rfo rm a n c e th re sh o ld
C o n d e n se rP e rfo rm a n c e fa c to r
O p tim u mp e rfo rm a n c e
80
85
90
95
100
Condenser
Performance Factor
(% of optimum)
Time
Typical usage of your Technos Condenser Watch
Low performance threshold
Condenser Performance factor
Optimum performance
Corrective action with TCW=
Inject new balls ?
Modify cycle times?
Adjust alarm thresholds?
Add CTCS ?…
Loss of Condenser performance
Remote alarm notification
TECHNOS CTCS- Condenser Tube Cleaning System
0 12 24 36
P re d ic te d (fro m d e sig n c o n d itio n s)
A c h ie v e d (fro m fie ld d a ta )
-500
0
500
1000
1500
2000
2500
3000
3500
4000
Cumulative
increase in
revenue (k$)
Time (months)
CTCS Payback analysis
Predicted (from design
conditions)
Achieved (from field data)
TCW Calculations are made with actual data
Condenser tube condition assessmentCondenser tube condition assessment
EXTERNAL
DEFECT
INTERNAL
DEFECT
THROUGH
DEFECT
SUPPORT
PLATE
EDDY CURRENT SIGNAL
1999
1994
% THROUGH WALL% NUMBER OF TUBES AFFECTED
1997
Eddy Current Testing
Boiler Plant Upgrades Applied in Australia
Playford South Australia
Existing 1400mg/N cu m
burner
RoBTAS burner to give 60%
reduction, OFA not shown
Low NOx
Conversion of ESP Casings to Baghouses (Fabric Filters)
Burner Tip UpgradesBurner Tip Upgrades
 Improvement of Plant Competitive
position by re-establishing the tip
design to suit the fuel now fired.
 Unburned Carbon reduction was the
achieved aimof the project.
 <12 month paybackforcustomer.
 Higherturndown achieved formills
Turbine Plant Upgrades Applied in Australia
Co-ordinate measuring machineCo-ordinate measuring machine
 Simple 3D “wireframe” CAD
model generated
 Complex surface
representation
 High degree of accuracy
 Full model assembly is the
basis of the retrofit design
without further work
Retrofit Design from Site SurveyRetrofit Design from Site Survey
 “Virtual assembly”
guarantees fit
 Flexible design
accommodates
features
inaccessible during
survey
Before Retrofit
p=
T=
m=
104bar
538°C
200kg/s
200MW 8929kJ/kWh
After Retrofit
p=
T=
m=
104bar
538°C
200kg/s
205MW 8885kJ/kWh
S:SDPrespgi-psu6.12.00Hazelwood Info.ppt
Parsons HP-IP
StageStage
LossesLosses
Efficiency improvementsEfficiency improvements
High power density bladingHigh power density blading
 Reduced profile losses
 Reduced secondary (end-wall losses)
 Reduced leakage losses
 Further aerodynamic refinements
Total improvement in stage efficiency:
5-6 percentage points relative to late 1980s
 Bigger improvements on older units
Installation of Hartlepool HP Turbine Retrofit
Hartlepool HP Turbine Retrofit (UK)
High Efficiency Blading in Operation
Generator Upgrades Applied in Australia
Advances in TechnologyAdvances in Technology
 Stainless steel hollow
conductors
– No copper in water system
 Welded water box design
– No braze joints in water
system
4
5
6
7
8
1
2 3
1 brazed electrical copper connection
2 welded special alloy block
3 stainless steel water chamber
4 teflon hoses
5 stainless steel hollow conductor
6 electrical connection brazed during
assembly (joined with high frequency
brazing within 1,5 minutes)
7 stainless steel fittings
8 Micadur bar insulation
Main Advantages: bars prefabricated
(including water chambers and electrical
connection)
Water Cooled Stator Bar EndsWater Cooled Stator Bar Ends
original water chambers
new water chambers
out of stainless steel
HAZELWOODHAZELWOOD
New parts in colour :
• End winding support
• Water manifold
• Teflon hoses
• Stator bars
• Circular winding
Stator rewinds with this technology can provide a
10 - 15 %increase in capability
Insulation SystemInsulation System
– MICADUR® insulation
system
• Outstanding 40 year operational
record
∀ ≈ 4500 V per mm thickness
(≈ 114 V/mil)
• Tested at 4 times operating
voltage
• Non-hygroscopic
Stator Cross Double Roebel barsStator Cross Double Roebel bars
Benefit from Additional Power Output -> 2-pole
Stator bar design with a
double Roebel bar
of a 2-pole generator
Apparent Power 686 MVA
All copper hollow Mixed stainless hollow
& copper solid
Loss reduction / kW ------ ≈ 634
Benefit / 7000 h full load a year,
@ 0.03 $/kWh
------
≈ 135 000 $/year
Typical Efficiency Increase with SS Hollow Conductors
Technical features derived from typical pre-engineering studies
Typical GE generator
Before rewind After rewind Comment
MVA 590 590
MW 560 560
p.f. 0,95 0,95
KV 22 22
Winding inlet temperature (°C) 45 45
Winding outlet temperature (°C) @ Un 78,4 74,2
Winding outlet temperature (°C) @ Umin= Un-5% 81,7 77,1
Water velocity in hollow conductors (m/s) 1,25 1,8
Pressure drop through the winding (bar) 1,7 2,5
Stator winding losses (kW) 3488 2820 - 668 kW
Winding DC resistance (ohms) 0,00307 0,00274
Reserve of output (%) 4% 12%
Double Roebel bars
& Stainless Steel Hollow conductors
ACTUAL LOSS REDUCTIONS DEPENDANT ON
MACHINE TYPE
 After cleaning
Chemical Cleaning: CuproplexChemical Cleaning: Cuproplex
 Oxide deposits
Typical Arrangement for CuproplexTypical Arrangement for Cuproplex
Air – Water Reverse Flushing of Winding Cooling SystemAir – Water Reverse Flushing of Winding Cooling System
Normal cooling water flow
Pressurised air-water
flow
Scales of copper oxyde
Mechanical flushing of stator bars
Result Without MonitoringResult Without Monitoring
New stator core & winding with conversion to water cooling
 OEM : WESTINGHOUSE
 Generator : 495 MVA
Direct hydrogen cooled
 Problem : Stator core
– Hot spots in stator core. Damage caused during stator slot
rewedging
 Solution :
– New stator core and stator winding
– Conversion to water cooled stator winding
– 45 MVA power increase, 300 kW losses reduction
Why a Wholistic Approach ?Why a Wholistic Approach ?
 Capital is scarce - must maximise investment
 Power Plant systems are inter-related
 Desk-top Study - Total Plant
 Restore than Upgrade
 Follow Business Drivers - capacity or efficiency ?
 Staged Risk Managed Process
 In-house plus External Expertise

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Optimising Efficiency & Capacity Sep 04 Rev 0

  • 1. Raja Ratnam 20th Sept 2004 Optimising Capacity andOptimising Capacity and Efficiency of Coal-Fired Power PlantsEfficiency of Coal-Fired Power Plants
  • 2. BackgroundBackground  Wholly owned subsidiary of ALSTOM Power  Operates Independently  Former Engineering Support Group for the QLD Utilities  Over 48 Engineers & Scientists - Brisbane  Covers 4 Sectors - Power, Mining, Petro-Chem & Processes  Recent Major Projects -  Owner’s Engineer in conjunction with PB Power for CS Energy’s Kogan Creek 750MW supercritical coal-fired plant  Shortlisted for the Collie 330MW O&M contract in WA
  • 3. Presentation Objectives:  Overview Business Environment  Why Upgrades no longer an option ?  Overview of some current Upgrade applications  Why a Wholistic Approach ?
  • 4.  Business Mentality - Optimise because you want BOTH at the Same Time - Capacity & Efficiency  IR impacting on business decisions  New Environmental Regulations delayed  Local Economy concerns only  Liability - ring fenced to within operational boundary  Government Owned Utilities - not profit driven  Oversupplied market  Plant generally within design life Past Business Environment
  • 5.  Meet Shareholder’s Demands - Maximise Profitability Want Highest Capacity when Price is HIGH Want Maximum Thermal Efficiency when Price is LOW  Must have Reliability - minimise expensive hedging  Positive Cash Flow  No Risks New Business Drivers
  • 6.  Probability of Failures Increasing Plant Ageing - more than 30 years old Experienced Personnel numbers down - Attrition Rate increasing Exponentially with Batch retirement  Peak Demands critical - summer & winter  Rapid growth in Technology and Options - too many choices ?  Rising Class Action initiatives - 3rd party claims  Foreign IPP’s exiting because of overseas issues  Threat of Terrorism - unknown & unpredictable  Community Environmental Attitude is Aggressive  Capital is scarce - short payback Current Business Environment
  • 7. Why Upgrade? Ageing Plant - Refurbish not enough !  Impending Environmental Laws  Greater Operating Flexibility - Maximise Profits  Less People Dependent  Minimise Business Risks Capital is scarce  Need higher ROI , shorter payback  New technology for better returns
  • 8. Regain Design Performance Review Risk Management Strategies - eg redundant plant Understand Plant Limits - use technology to improve measurements and monitor degradation Operate closer to limits - use technology Real-time production strategy - capacity or efficiency ? Include all costs for specific strategy - eg increase maintenance Before Upgrade - Back to Basics
  • 9. How well is this Controller doing ?How well is this Controller doing ?
  • 10. What is ProcessDoctor ?What is ProcessDoctor ? ProcessDoctor is a software solution for automatic, control loop performance assessment and monitoring
  • 11. BenefitsBenefits Identify Variability Diagnose, Maintain to Reduce Variability Move Target Benchmark, Monitor & Sustain Excessive process variability prevents operators from running the plant at or near its operating limits or constraints. time throughput Current Performance Process Constraint Optimal Performance $
  • 12. Other 900 35 180 25/40/35 5 Power 2000 65 350 25/40/35 8 PetroChem 1500 100 180 25/40/35 9 Oil & Gas 1200 50 220 25/40/35 6 EEMUA 144 9 10 80/15/5 1 Industry Findings - AlarmsIndustry Findings - Alarms How many alarms do you get every day? Average Alarms per Day Average Standing Alarms Peak Alarms per 10 Minutes Average Alarms/ 10 Minute Interval Distribution % (Low/Med/High)
  • 13. How many alarms do you get every day? ProcessGuard is out-of-the-box Alarm Management software that lets you: •Seamlessly reduce nuisance alarms in your control system •Automatically: •Collect & store alarm data •Analyze and identify bad actors • Remove bad actors • Monitor to sustain results •Increase uptime, increase equipment reliability, and improve plant safety
  • 15. Condenser Performance ImprovementsCondenser Performance Improvements  Maintain Tubes  Early replacement - ECT surveys  Maintain cleanliness - on line and off line, filtration  Eliminate Shell Air Leakage  Improve CW Flow stratification - tubes fully primed  Improve Internal Steam Paths  Maintain Air Extraction system  On line Performance Monitoring - reduce variance - use remote experts
  • 16. TECHNOS TCW is a Remote Monitoring & Control SystemTECHNOS
  • 17. MONITOR & ANALYSE CONDENSER PERFORMANCE TECHNOS 1 L o w p e rfo rm a n c e th re sh o ld C o n d e n se rP e rfo rm a n c e fa c to r O p tim u mp e rfo rm a n c e 80 85 90 95 100 Condenser Performance Factor (% of optimum) Time Typical usage of your Technos Condenser Watch Low performance threshold Condenser Performance factor Optimum performance Corrective action with TCW= Inject new balls ? Modify cycle times? Adjust alarm thresholds? Add CTCS ?… Loss of Condenser performance Remote alarm notification
  • 18. TECHNOS CTCS- Condenser Tube Cleaning System 0 12 24 36 P re d ic te d (fro m d e sig n c o n d itio n s) A c h ie v e d (fro m fie ld d a ta ) -500 0 500 1000 1500 2000 2500 3000 3500 4000 Cumulative increase in revenue (k$) Time (months) CTCS Payback analysis Predicted (from design conditions) Achieved (from field data) TCW Calculations are made with actual data
  • 19. Condenser tube condition assessmentCondenser tube condition assessment EXTERNAL DEFECT INTERNAL DEFECT THROUGH DEFECT SUPPORT PLATE EDDY CURRENT SIGNAL 1999 1994 % THROUGH WALL% NUMBER OF TUBES AFFECTED 1997 Eddy Current Testing
  • 20. Boiler Plant Upgrades Applied in Australia Playford South Australia
  • 21. Existing 1400mg/N cu m burner RoBTAS burner to give 60% reduction, OFA not shown Low NOx
  • 22. Conversion of ESP Casings to Baghouses (Fabric Filters)
  • 23. Burner Tip UpgradesBurner Tip Upgrades  Improvement of Plant Competitive position by re-establishing the tip design to suit the fuel now fired.  Unburned Carbon reduction was the achieved aimof the project.  <12 month paybackforcustomer.  Higherturndown achieved formills
  • 24. Turbine Plant Upgrades Applied in Australia
  • 25. Co-ordinate measuring machineCo-ordinate measuring machine  Simple 3D “wireframe” CAD model generated  Complex surface representation  High degree of accuracy  Full model assembly is the basis of the retrofit design without further work
  • 26. Retrofit Design from Site SurveyRetrofit Design from Site Survey  “Virtual assembly” guarantees fit  Flexible design accommodates features inaccessible during survey
  • 27. Before Retrofit p= T= m= 104bar 538°C 200kg/s 200MW 8929kJ/kWh After Retrofit p= T= m= 104bar 538°C 200kg/s 205MW 8885kJ/kWh S:SDPrespgi-psu6.12.00Hazelwood Info.ppt Parsons HP-IP
  • 29. Efficiency improvementsEfficiency improvements High power density bladingHigh power density blading  Reduced profile losses  Reduced secondary (end-wall losses)  Reduced leakage losses  Further aerodynamic refinements Total improvement in stage efficiency: 5-6 percentage points relative to late 1980s  Bigger improvements on older units
  • 30. Installation of Hartlepool HP Turbine Retrofit
  • 31. Hartlepool HP Turbine Retrofit (UK) High Efficiency Blading in Operation
  • 33. Advances in TechnologyAdvances in Technology  Stainless steel hollow conductors – No copper in water system  Welded water box design – No braze joints in water system
  • 34. 4 5 6 7 8 1 2 3 1 brazed electrical copper connection 2 welded special alloy block 3 stainless steel water chamber 4 teflon hoses 5 stainless steel hollow conductor 6 electrical connection brazed during assembly (joined with high frequency brazing within 1,5 minutes) 7 stainless steel fittings 8 Micadur bar insulation Main Advantages: bars prefabricated (including water chambers and electrical connection) Water Cooled Stator Bar EndsWater Cooled Stator Bar Ends
  • 35. original water chambers new water chambers out of stainless steel HAZELWOODHAZELWOOD
  • 36. New parts in colour : • End winding support • Water manifold • Teflon hoses • Stator bars • Circular winding
  • 37. Stator rewinds with this technology can provide a 10 - 15 %increase in capability Insulation SystemInsulation System – MICADUR® insulation system • Outstanding 40 year operational record ∀ ≈ 4500 V per mm thickness (≈ 114 V/mil) • Tested at 4 times operating voltage • Non-hygroscopic
  • 38. Stator Cross Double Roebel barsStator Cross Double Roebel bars
  • 39. Benefit from Additional Power Output -> 2-pole Stator bar design with a double Roebel bar of a 2-pole generator Apparent Power 686 MVA All copper hollow Mixed stainless hollow & copper solid Loss reduction / kW ------ ≈ 634 Benefit / 7000 h full load a year, @ 0.03 $/kWh ------ ≈ 135 000 $/year Typical Efficiency Increase with SS Hollow Conductors
  • 40. Technical features derived from typical pre-engineering studies Typical GE generator Before rewind After rewind Comment MVA 590 590 MW 560 560 p.f. 0,95 0,95 KV 22 22 Winding inlet temperature (°C) 45 45 Winding outlet temperature (°C) @ Un 78,4 74,2 Winding outlet temperature (°C) @ Umin= Un-5% 81,7 77,1 Water velocity in hollow conductors (m/s) 1,25 1,8 Pressure drop through the winding (bar) 1,7 2,5 Stator winding losses (kW) 3488 2820 - 668 kW Winding DC resistance (ohms) 0,00307 0,00274 Reserve of output (%) 4% 12% Double Roebel bars & Stainless Steel Hollow conductors ACTUAL LOSS REDUCTIONS DEPENDANT ON MACHINE TYPE
  • 41.  After cleaning Chemical Cleaning: CuproplexChemical Cleaning: Cuproplex  Oxide deposits
  • 42. Typical Arrangement for CuproplexTypical Arrangement for Cuproplex
  • 43. Air – Water Reverse Flushing of Winding Cooling SystemAir – Water Reverse Flushing of Winding Cooling System Normal cooling water flow Pressurised air-water flow Scales of copper oxyde Mechanical flushing of stator bars
  • 44.
  • 45. Result Without MonitoringResult Without Monitoring
  • 46. New stator core & winding with conversion to water cooling  OEM : WESTINGHOUSE  Generator : 495 MVA Direct hydrogen cooled  Problem : Stator core – Hot spots in stator core. Damage caused during stator slot rewedging  Solution : – New stator core and stator winding – Conversion to water cooled stator winding – 45 MVA power increase, 300 kW losses reduction
  • 47. Why a Wholistic Approach ?Why a Wholistic Approach ?  Capital is scarce - must maximise investment  Power Plant systems are inter-related  Desk-top Study - Total Plant  Restore than Upgrade  Follow Business Drivers - capacity or efficiency ?  Staged Risk Managed Process  In-house plus External Expertise

Hinweis der Redaktion

  1. To answer the question, what is control loop performance assessment, we ask the Questions…. Figure shows the time trend for 4STM-04500 (A SH Spray Valve station). As control engineers we ask “ How good is this control, Can we do better” The answer to the question is “You don’t know without more information” Next slide
  2. The ‘Doc’ in ProcessDoctor is for ‘DOCTOR’. We have called it this because like a medical doctor diagnoses the health of his or her patient, ProcessDoctor helps diagnose the health of control loops. ProcessDoctor gives you the additional information you require to determine, if and how the variability can be reduced in the control loop.