Corrosion Monitoring
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Transcript of Corrosion Monitoring
EDS 2004/Metallurgy 9-1
Corrosion Monitoring
EDS 2004/Metallurgy 9-2
Outcomes
Recall classes of corrosion monitorsIdentify operating principlesIdentify significant limitations
EDS 2004/Metallurgy 9-3
Types of Corrosion Monitors
NDTCorrosion couponsElectrical resistance probesLinear polarization resistance probesHydrogen probes
EDS 2004/Metallurgy 9-4
Non Destructive Testing
EDS 2004/Metallurgy 9-5
Nondestructive Testing
Advantages and disadvantages vary somewhat with methodAdvantages– Direct measurement of metal loss– Equipment is portable so measurements can be
made at any desired location– May be usable on stream– Portable – move until corrosion is found
EDS 2004/Metallurgy 9-6
Nondestructive Testing
Disadvantages– May or may not show pitting or cracking– May or may not show corrosion around
complex geometries– Gives only an average corrosion rate
EDS 2004/Metallurgy 9-7
Corrosion Coupons
EDS 2004/Metallurgy 9-8
Corrosion Coupons
Advantages– Direct evidence of corrosion– Shows pitting– Can show cracking, crevice corrosion, and
galvanic corrosion– Can be conducted on line or in lab– Can be used in any corrosive environment– Available in essentially all commercial alloys
EDS 2004/Metallurgy 9-9
Corrosion Coupons
Disadvantages– Gives only an average corrosion rate– Must select proper location in process– Intrudes into process– Improper cleaning/handling will give
erroneous results– SLOW
EDS 2004/Metallurgy 9-10
Corrosion Coupons
EDS 2004/Metallurgy 9-11
Corrosion Coupons
EDS 2004/Metallurgy 9-12
Corrosion Coupons
Greatest benefit of using corrosion coupons is for the selection of a new alloy in a process known to be corroding.
EDS 2004/Metallurgy 9-13
Electrical Resistance Probe
EDS 2004/Metallurgy 9-14
Electrical Resistance Probe
Advantages– Fast enough to detect the effects of process
changes on corrosion rate (sensitivity on the order of 1 - 2 days)
– High sensitivity probes reported to respond more rapidly
– Work in most corrosive environments— some limits on corrodants and temperature
EDS 2004/Metallurgy 9-15
Electrical Resistance Probe
Advantages– Available in most commercial alloys– May detect pitting
EDS 2004/Metallurgy 9-16
Electrical Resistance Probe
Disadvantages– Must select proper location in process– Time sensitivity insufficient to measure the
effect of upsets on corrosion– May protrude into process– Must be changed periodically
EDS 2004/Metallurgy 9-17
Electrical Resistance Probes
EDS 2004/Metallurgy 9-18
Electrical Resistance Probe
New
Not so New
Electrical resistance of probe varies with cross section of wire
EDS 2004/Metallurgy 9-19
Electrical Resistance Probe
EDS 2004/Metallurgy 9-20
Electrical Resistance Probe
Typical electrical resistance probe sensitivity
EDS 2004/Metallurgy 9-21
Linear Polarization Probe
EDS 2004/Metallurgy 9-22
Linear Polarization Probe
Probe is electrochemical in nature– Applies a small 10 - 20 mV sinusoidal potential– Measures current response– Calculates resistance of system– Calculates corrosion rate based on resistance
EDS 2004/Metallurgy 9-23
Linear Polarization Probe
Current i(measured)
Potential εε = Eapp - Ecorr
Slope = = Rp∆ε∆i
∆ε∆iRp = = B
icorr
B is a constant for a given system and relativelyconstant between systems
EDS 2004/Metallurgy 9-24
Linear Polarization Probe
Advantages– Speed
— Test are short— Responds quickly enough to detect corrosion
caused by upsets– Electrodes available for most commercial alloys– Will normally detect pitting
EDS 2004/Metallurgy 9-25
Linear Polarization Probe
Disadvantages– Requires at least some electrolyte– Beneficial to determine B independently or to
calibrate with coupon tests– Must select proper location in process
EDS 2004/Metallurgy 9-26
Linear Polarization Probe
Probes can be 2 or 3 electrode
EDS 2004/Metallurgy 9-27
Linear Polarization Probe
EDS 2004/Metallurgy 9-28
Hydrogen Permeation Sensor
EDS 2004/Metallurgy 9-29
Hydrogen Permeation
Indicator for– Aqueous corrosion when certain species are
present e.g. HF, H2S, CN-, As– Hydrogen embrittlement– Hydrogen blistering– SOHIC– Sulfide stress cracking
EDS 2004/Metallurgy 9-30
Pressure Gauge
Installed at a fixed locationHydrogen penetrates the tip of the gauge and is trapped. Pressure increases within the system and is recorded on the gaugeThe gauge is periodically reset
EDS 2004/Metallurgy 9-31
Pressure Gauge
EDS 2004/Metallurgy 9-32
Hydrogen Sensor
“Patch” attaches to pipe or vessel– Magnetic or Strap– Low or high temperature
Air pulled through channels in patch– Sweeps hydrogen to remote sensor
Sensor measures hydrogen concentration– Hydrogen flux calculated
Portable – can move to find corrosion
EDS 2004/Metallurgy 9-33
Hydrogen Sensor
Useful for– High temp corrosion e.g. naphthenic acid– Predicting/measuring hydrogen
blistering/sulfide stress cracking– May or may not predict general corrosion rates
— Effect of recombination poisons on hydrogen penetration must be calibrated
EDS 2004/Metallurgy 9-34
Hydrogen Sensor