Problem (P.) and Root Cause (R.C.)
(% of units experiencing the problem - estimated)
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Solutions
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MANAGEMENT
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P. Monitoring does not prevent major water chemistry upsets
R.C. Monitoring is not round-the-clock, there are no approved actions, training, etc. (80%)
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Guidelines, training of operators and chemists, on-line instruments with alarms
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P. Repeat failures
R.C. No root cause analysis - complacency (70%)
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Multi-disciplinary root cause analysis, derived and verified solutions.
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P. Startup delays
R.C. Water chemistry upsets, and layup corrosion during testing and commissioning of new units (90%)
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Commissioning guidelines, training, corrosion protection during storage and erection.
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CYCLE DESIGN
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P. Difficulty in controlling corrosion and water and steam chemistry
R.C. Mixed metallurgy in feedwater system (40%)
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All-ferrous systems (including auxiliary heat exchangers).
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P. Difficulty in controlling corrosion and water and steam chemistry
R.C. No means to effectively remove impurities from the cycle (70%)
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Boiler blowdown design, blowdown of mud drums, filtration of return condensate and feedwater, condensate polishing, frequent chemical cleaning
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P. Erosion-corrosion and cavitation
R.C. High flow velocities in carbon steel piping (50%)
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Proper design velocities, use of alloy steels, reduce oxygen scavenger, increase O2.
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OPERATION
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P. Poor control of water chemistry
R.C. Operators underestimate the effects of upsets (60%)
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Training, guidelines, management support.
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P. Wrong or delayed corrective actions
R.C. Insufficient training of operators, lack of written guidelines (60%)
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Training, guidelines, management support.
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P. Long startups due to high concentration of oxides
R.C. Poor startup chemistry, high oxygen concentrations (30%)
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Proper layup, filling with deaerated water.
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BOILER, SUPERHEATER, AND REHEATER
|
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P. High carry-over
R.C. Damaged internals, drum level control, foaming, high solids (25%)
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Inspect and fix, improve chemistry, monitor Na and cation conductivity in steam, train operators.
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P. Boiler tube failures
R.C. High local heat flux and poor circulation (20%)
|
Adjust combustion, reduce maximum load, clean boiler, do not patch weld.
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P. High water quality
R.C. High approach temperature leading to erosion-corrosion (15%)
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Balance the heat input in the economizer.
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P. Solid particle erosion of turbine blades and >Fe throughout the cycle, long startups
R.C. Exfoliation of magnetite (80% of other utility units)
|
Chemical cleaning of superheater and reheater, balancing the fireside temperatures
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TURBINE
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P. Blade and disk corrosion (pitting, corrosion fatigue, and stress corrosion) in the LP section
R.C. Marginal steam chemistry, no layup, high stresses and vibration (40%)
|
Control steam chemistry and layup, tune blade vibration, redesign blade attachment.
|
P. HP turbine deposits leading to loss of performance in high pressure drum boiler units
R.C. Carry-over of copper and phosphate (80%)
|
Optimize cycle chemistry, replace copper alloy tubing in HP heaters.
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P. Sticking turbine valves
R.C. Impurities in steam (several cases of destructive overspeed) (20%)
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Exercise valves weekly, improve steam purity.
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CONDENSER
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P. Condenser tube leaks
R.C. Many possible causes including pitting, erosion, etc. (60%)
|
Preventive tube plugging, replace with better material.
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DEAERATOR
|
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P. Corrosion cracking of welds
R.C. Root cause not known, possibly water piston and high residual stresses (40%)
|
Calculate and change the conditions for water piston, inspect periodically and perform fracture mechanics evaluation.
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P. High oxygen in effluent
R.C. Distress of the internals (20%)
|
Fix internals, better control of pressure, temperature, and load changes.
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FEEDWATER HEATERS AND HEAT EXCHANGERS
|
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P. Erosion-corrosion of tube inlets
R.C. High local flow velocities and turbulence (50%)
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Tube inlet inserts, replace tubes with more resistant material.
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P. Pitting and leaks in austenitic stainless steel tubing
R.C. Presence of chloride in feedwater (30%)
|
Improve feedwater chemistry. When replacing tubes, use better material, test for large inclusions.
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PIPING
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P. Erosion-corrosion of feedwater piping
R.C. High flow velocity, turbulence, low pH, and excessive concentration of oxygen scavenger (70%)
|
Inspect critical components ASAP, evaluate feedwater and wet steam piping, improve water chemistry.
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WATER CHEMISTRY
|
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P. Difficulty in controlling water chemistry and detecting problems
R.C. Inadequate sampling points (i.e. steam, return condensate) (40%)
|
Improve sampling
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P. Sampling errors
R.C. Low sample flow, high sample temperature, long sample lines, surface taps, deposits in tubing (70%)
|
Increase sample flow (4 to 6 ft/sec), clean coolers, satellite sampling with shorter lines, isokinetic sampling nozzles
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P. High concentration of organic acids, corrosion, and scale and deposits
R.C. Inappropriate water treatment chemicals or their overfeeding (60% of industrial)
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Evaluate the use of chemicals, minimize concentration, neutralize acidic conditions.
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P. High concentrations of oxygen and CO2
R.C. Air inleakage (80%)
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Identify locations using helium or SF6, fix leaks.
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P. Incorrect analytical results from analysis of O2, SiO2, etc.
R.C. Analytical interferences due to organic chemicals (30% of industrial)
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Determine interferences, change analytical method
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P. Boiler tube failures: caustic gouging, hydrogen damage, pitting, and overheat
R.C. High levels of impurities in boiler water
|
Control condenser leaks, improve corrective actions, reduce feedwater Fe, chemically clean boiler, change water treatment
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P. Contaminated return condensate
R.C. Fe, Cu, organics, process chemicals leaking into the system (40%)
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Monitor, polish, automatic dump
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P. Release of makeup or condensate polisher regenerants
R.C. Unreliable or poorly designed valving and inadequate monitoring (5%)
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Reliable design, maintenance, monitoring, proper operator actions
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