AMPP Senior Corrosion Technologist flashcards
AMPP Senior Corrosion Technologist · Build recall with a focused review session.
32 cards. Read the term and the definition here. The deck at the top of this page is optional.
- Carbon equivalent threshold
- A calculated value combining carbon and alloying elements; values above about 0.40 in carbon steels indicate elevated weld cracking risk and require preheat or controlled procedures.
- PREN formula
- Pitting resistance equivalent number equals Cr plus 3.3 times Mo plus 16 times N; higher values indicate greater resistance to chloride pitting in stainless steels.
- Sensitization of stainless steel
- Chromium carbide precipitation at grain boundaries in the 425-815 C range depletes adjacent chromium below about 12 percent, leaving the steel susceptible to intergranular corrosion.
- Galvanic corrosion principle
- When two dissimilar metals are coupled in an electrolyte, the more active metal becomes anodic and corrodes faster; the potential difference and area ratio drive the rate.
- Hydrogen embrittlement susceptibility
- High-strength steels (hardness above about 22 HRC) are prone to hydrogen embrittlement and sulfide stress cracking; austenitic stainlesses are generally more resistant.
- Inhibitor efficiency formula
- Percent efficiency equals the blank corrosion rate minus the inhibited rate, divided by the blank rate, times 100; measured by weight loss, LPR, or resistance methods.
- Oxygen scavenger limits
- Sulfite removes dissolved oxygen but breaks down to sulfide above about 150 C; hydrazine and DEHA are used at higher boiler temperatures.
- Boiler pH control
- Coordinated phosphate programs maintain boiler water pH around 9.5 to 10.5 to prevent caustic attack and acidic corrosion of the steel.
- Biocide alternation
- Alternating oxidizing agents such as hypochlorite with non-oxidizing agents such as glutaraldehyde limits microbial resistance and biofilm regrowth in cooling systems.
- Scale inhibitor mechanism
- Phosphonates and polyacrylates inhibit scale by threshold effects and crystal distortion; over-dosing can precipitate the inhibitor itself and foul the system.
- Coating resistance formula
- Resistance equals resistivity times dry film thickness divided by area; thicker, more resistive films provide better barrier protection against electrolyte contact.
- Surface preparation standard
- SSPC-SP 10 (Near-White) or SP 5 (White Metal) is required for immersion service; residual chloride is commonly limited to about 3-5 micrograms per square centimeter.
- Anchor profile range
- A typical anchor profile of 1.5 to 3.5 mils (38-89 micrometers) improves adhesion; excessive profile can leave peaks uncoated and cause early failure.
- Holiday detection voltage
- High-voltage spark testers detect pinholes; voltage is set by dry film thickness, commonly about 100 volts per mil, per manufacturer guidance.
- FBE pipeline coating
- Fusion-bonded epoxy is a standard buried pipeline coating applied at about 350-500 micrometers thickness; it provides good adhesion and cathodic disbondment resistance.
- Coating adhesion testing
- Pull-off testing per ASTM D4541 measures adhesion strength; the failure mode (adhesive versus cohesive) indicates whether surface preparation or coating chemistry is at fault.
- CO2 corrosion drivers
- Sweet corrosion rate increases with CO2 partial pressure and temperature; models such as NORSOK M-506 or de Waard-Milliams estimate rates for carbon steel.
- H2S threshold
- An H2S partial pressure above 0.05 psi (0.0035 bar) triggers sulfide stress cracking evaluation for susceptible steels under NACE MR0175/ISO 15156.
- Water wetting requirement
- Internal corrosion requires water contact with the steel; oil-wet surfaces may remain protected even without chemical treatment in multiphase flow.
- Erosional velocity limit
- API RP 14E approximates erosional velocity as C divided by the square root of mixture density, with C of 100 for continuous and 125-200 for intermittent service.
- Pigging and ILI
- Pigging distributes inhibitors and removes solids; in-line inspection with magnetic flux leakage or ultrasonic tools detects and sizes metal loss.
- Internal monitoring methods
- Corrosion coupons give time-averaged rates, electrical resistance probes give real-time trends, and linear polarization resistance gives instantaneous rates for electrolyte systems.
- CP protection criterion
- A polarized potential of -850 mV versus copper-copper sulfate, or a 100 mV polarization shift, indicates adequate cathodic protection when IR drop is accounted for.
- CP current requirement
- Current equals coated area times bare current density times one minus coating efficiency; degraded coatings increase current demand and rectifier output.
- Anode resistance formula
- For a vertical rod, resistance equals soil resistivity divided by twice pi times length, times the natural log of four times length over diameter minus one.
- Sacrificial anode selection
- Magnesium suits high-resistivity soils, zinc suits low-resistivity soils and seawater, and aluminum alloys are used for offshore structures and pipelines.
- Close-interval survey
- A moving reference electrode measures potential along a pipeline at short intervals, locating coating defects and confirming protection level distribution.
- Stray current corrosion
- DC current leaving a structure to earth causes accelerated corrosion at the discharge point; mitigation uses drainage bonds or localized sacrificial anodes.
- Confined space atmosphere limits
- Entry requires oxygen between 19.5 and 23.5 percent, flammable gas below 10 percent LEL, and H2S below the site limit, typically 10 ppm.
- Hot work gas testing
- Combustible gas readings above 10 percent LEL prohibit hot work; continuous monitoring is required near coatings, tanks, and confined spaces.
- Job Safety Analysis
- A JSA documents hazards, controls, and responsibilities for a task; it is reviewed with the crew and updated whenever conditions or scope change.
- Chemical segregation rule
- Incompatible chemicals such as acids and hypochlorite must be stored separately; SDS review, PPE selection, and spill response planning precede handling.