AMPP Corrosion Technician flashcards
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32 cards. Read the term and the definition here. The deck at the top of this page is optional.
- CSE reference electrode
- Copper/copper-sulfate half-cell used as the reference for structure-to-soil potential measurements; the -850 mV criterion for steel is stated versus this electrode.
- Instant-off potential
- Structure-to-soil potential measured immediately after interrupting CP current, removing IR drop so the true polarized potential is read against the -850 mV criterion.
- 100 mV polarization criterion
- Alternative CP acceptance criterion in which at least 100 mV of potential shift from native to polarized state demonstrates adequate protection of the structure.
- Sacrificial anode
- Galvanic anode (magnesium, zinc, or aluminum alloy) that corrodes preferentially to protect the structure, chosen when resistivity is low and current demand is modest.
- Impressed current system
- CP system using an external DC power source and inert anodes (MMO, high-silicon cast iron) to deliver high current in high-resistivity or high-demand environments.
- Stray current corrosion
- Corrosion caused by current from an external source discharging from the structure into the electrolyte; identified by potential shifts and mitigated by bonds or drainage.
- Anode resistance formula
- Dwight equation R = (rho/(2*pi*L))*(ln(4L/d)-1) gives the resistance to earth of a single vertical anode from soil resistivity and anode dimensions.
- Surface preparation standard
- SSPC-SP 5/NACE 1 (white metal) and SP 10/NACE 2 (near-white) define blast cleanliness levels; preparation is the largest factor in coating life.
- Anchor profile
- Surface roughness created by abrasive blasting, typically 1.5 to 4 mils for epoxy systems, measured by replica tape or profilometer.
- Holiday detection
- Testing for pinholes and thin spots using a low-voltage wet sponge on thin films or a high-voltage spark tester on thicker coatings.
- Cathodic disbondment
- Loss of coating adhesion around a defect caused by alkalinity and hydrogen generated by CP current; tested per ASTM G8 or G95.
- Soluble salt contamination
- Chlorides and sulfates left on the substrate that cause osmotic blistering and premature failure; removed and verified by conductivity testing before coating.
- Coating conductance
- Inverse of coating resistance; a well-coated structure shows low conductance and low CP current demand, while a failed coating shows high conductance.
- Galvanic series
- Ranking of metals by corrosion potential in seawater; coupling metals far apart on the series increases galvanic corrosion risk.
- Area ratio effect
- Galvanic corrosion of the anode accelerates when the cathode area is large relative to the anode area; design should avoid small-anode-to-large-cathode couples.
- PREN formula
- Pitting resistance equivalent number = %Cr + 3.3*%Mo + 16*%N; higher values indicate better resistance to chloride pitting in stainless steels.
- Sensitization
- Chromium carbide precipitation at grain boundaries in austenitic stainless steel during heating (425-815 C), depleting chromium and causing intergranular corrosion.
- Hydrogen embrittlement
- Loss of ductility in high-strength steels caused by absorbed hydrogen, aggravated by overprotection that produces hydrogen at the cathode.
- Oxygen depolarization
- Cathodic reaction O2 + 2H2O + 4e- -> 4OH- that dominates carbon steel corrosion in neutral aerated water and is limited by oxygen diffusion.
- Anodic inhibitor
- Inhibitor that promotes passive film formation (chromate, nitrite, molybdate); underdosing can convert general attack into severe localized pitting.
- Cathodic inhibitor
- Inhibitor that slows the cathodic reaction, often by precipitating a barrier film (zinc salts, polyphosphates), reducing overall corrosion rate.
- Filming amine inhibitor
- Adsorption-type inhibitor forming a hydrophobic film on metal, widely used to protect condensate return lines and oil and gas pipelines.
- Langelier Saturation Index
- Index comparing actual water pH to saturation pH; positive indicates scaling tendency, negative indicates corrosive tendency in cooling water systems.
- Oxygen scavenger
- Chemical such as sulfite or hydrazine that removes dissolved oxygen in boiler feedwater; sulfite is avoided above about 200 C.
- Biocide treatment
- Oxidizing (chlorine) or non-oxidizing (glutaraldehyde) chemicals used to control microbiologically influenced corrosion in cooling and process water.
- Corrosion cell elements
- Anode, cathode, electrolyte, and electrical path; removing any one element stops the corrosion reaction, which is the basis for most mitigation methods.
- Faraday's law
- Mass loss = (I*t*M)/(n*F), relating corrosion current and time to metal loss using atomic mass, electrons transferred, and Faraday's constant 96,485 C/mol.
- Corrosion rate conversion
- 1 microamp per square centimeter corresponds to about 0.0116 mm/year for iron; mpy = 0.128 * current density * (equivalent weight/density).
- Crevice corrosion mechanism
- Oxygen depletion and chloride buildup inside a tight gap create an active anode; mitigated by design that avoids tight crevices and by alloy selection.
- Erosion-corrosion
- Accelerated metal loss from combined flow and corrosion, localized at elbows, tees, and downstream of orifices; mitigated by velocity limits and material selection.
- NACE MR0175 / ISO 15156
- Standard for materials resistant to sulfide stress cracking in oil and gas; selection depends on H2S partial pressure, pH, and chloride content.
- Uniform corrosion
- Even metal loss across the surface, measured by weight loss or linear polarization; the least dangerous form because life can be predicted.