3.1 Corrosion Rates (Short-Term, Long-Term, and Initial Estimates)
Key Takeaways
- Long-Term (LT) corrosion rate averages wall thinning over the entire operating history of the pipe: $(t_{initial} - t_{actual}) / Time_{total}$.
- Short-Term (ST) corrosion rate isolates wall thinning during the most recent inspection interval: $(t_{previous} - t_{actual}) / Time_{interval}$.
- The controlling rate is typically the larger (more conservative) of the LT and ST rates, unless process or operational changes dictate otherwise.
- All calculations must use active operating years (time in service) rather than calendar years to prevent underestimating the corrosion rate.
- When establishing initial corrosion rates for new services, inspectors must take thickness measurements within 3 to 6 months of start-up.
3.1 Corrosion Rates (Short-Term, Long-Term, and Initial Estimates)
In-service piping inspection under the API 570 standard is fundamentally driven by the need to understand how fast a piping system's metallic pressure boundary is thinning. The rate at which corrosion occurs directly determines when the piping system must be inspected next, whether it needs to be repaired or replaced, and how long it can safely remain in service. Consequently, calculating and selecting the correct corrosion rates are amongst the most critical responsibilities of the API 570 authorized piping inspector.
Long-Term and Short-Term Corrosion Rates
The API 570 code defines two primary corrosion rate calculations: the Long-Term (LT) corrosion rate and the Short-Term (ST) corrosion rate. Both are calculated as linear rates expressed in inches per year (in./yr) or millimeters per year (mm/yr).
Long-Term Corrosion Rate (LT)
The Long-Term corrosion rate averages the loss of wall thickness over the entire documented operating history of the piping system. It represents the overall steady-state thinning rate and is less sensitive to brief operational upsets or temporary seasonal changes. The formula for the Long-Term corrosion rate is:
Where:
- $t_{initial}$ is the thickness (in inches or millimeters) at the initial baseline inspection (typically when the pipe was first placed in service or first measured).
- $t_{actual}$ is the actual thickness measured at the most recent inspection at the same Condition Monitoring Location (CML).
- $t_{time}$ is the time period in operating years between the initial and actual inspections.
Short-Term Corrosion Rate (ST)
The Short-Term corrosion rate calculates the wall thickness loss over the most recent inspection interval. This rate is highly sensitive to recent changes in process conditions, fluid chemistry, catalyst degradation, or chemical injection rates. The formula for the Short-Term corrosion rate is:
Where:
- $t_{previous}$ is the thickness measured at the inspection immediately preceding the current inspection at the same CML.
- $t_{actual}$ is the actual thickness measured at the most recent inspection.
- $t_{time}$ is the time period in operating years between the previous and actual inspections.
Operating Years vs. Calendar Years
A critical parameter in both formulas is the time ($t_{time}$). The inspector must use operating years (time in service) rather than calendar years. If a piping system has been idle, blinded, or decommissioned for several years, using calendar years would artificially depress the calculated corrosion rate, creating a dangerous underestimation of the thinning rate. For example, if a pipe has been in place for 10 calendar years but was shut down and nitrogen-purged for 4 of those years, the time variable in the denominator must be 6 operating years, assuming no corrosion occurred during standby.
| Aspect | Long-Term Corrosion Rate (LT) | Short-Term Corrosion Rate (ST) |
|---|---|---|
| Focus | Historical average over pipe life | Recent behavior between last two checks |
| Formula | $(t_{initial} - t_{actual}) / Time_{total}$ | $(t_{previous} - t_{actual}) / Time_{interval}$ |
| Sensitivity | Low (smooths out process variations) | High (captures recent process upsets) |
| Primary Use | Assessing long-term system stability | Identifying accelerated degradation |
Selecting the Controlling Corrosion Rate
API 570 Section 7.1.1 states that the authorized inspector, in consultation with a piping engineer, must select the corrosion rate that best reflects the current behavior of the system.
- Standard Default: In most steady-state applications, the inspector will compare the calculated LT and ST rates and select the larger (more conservative) value as the controlling rate for remaining life and inspection interval calculations.
- Accelerated Corrosion: If a process change, fluid velocity increase, or temperature elevation has occurred, the ST rate will typically be much higher than the LT rate. In this scenario, the ST rate must be selected as the controlling rate because the historical LT rate no longer represents the current process aggressiveness.
- Operational Upsets: If a temporary process upset (e.g., a desalter bypass or acid carryover) occurred during the last interval, the ST rate might show a massive, non-representative spike. If the upset has been resolved and the system has returned to normal baseline conditions, the inspector, with proper engineering justification, may choose not to use the spiked ST rate, or may use a rate determined by a corrosion specialist.
Initial Rates for New or Changed Services
When a new piping system is placed in service, or when an existing piping system's service conditions are modified, there is no historical thickness data to calculate a rate. API 570 establishes a strict protocol for establishing the initial corrosion rate:
- Step 1: Similar Service Data: The inspector should obtain corrosion rate data from existing piping systems in similar service at the same facility or in similar industry operations.
- Step 2: Published Data & Software: If local data is unavailable, the inspector can consult published corrosion databases, corrosion curves (such as McConomy curves for sulfidation or Couper-Gorman curves), or proprietary modeling software.
- Step 3: Specialist Consultation: A corrosion specialist or piping engineer should review the process conditions (temperature, pressure, velocity, chemical concentrations) to estimate the rate.
- Step 4: Initial Verification (The 3-to-6-Month Rule): If an estimated corrosion rate is used, the inspector must verify the actual rate by taking thickness measurements (typically using non-destructive on-stream ultrasonic testing) after a short period of operation, generally 3 to 6 months (or up to 1000 hours of operating service). This physical reading is used to validate or adjust the initial estimate.
Localized and Pitting Corrosion Considerations
While the standard formulas assume uniform thinning across the pipe wall, many damage mechanisms, such as acid attack, microbiologically influenced corrosion (MIC), or erosion-corrosion at elbows, result in localized thinning. For localized corrosion, the inspector must use the minimum localized thickness reading at a given CML to calculate the rates. If pitting is present, standard ultrasonic grid measurements or profile radiography are employed, and the deepest pit within a designated area is tracked. Under API 570, localized corrosion rates must be treated with extreme caution, and the highest local rate must be selected as the controlling rate for that specific circuit. The inspector cannot average high and low thickness readings across different CMLs to artificially lower the corrosion rate; each CML stands alone in its corrosion rate determination.
Worked Calculation Example
Consider a piping circuit fabricated from carbon steel (NPS 8, Schedule 40) in a refinery hydroprocessing unit. An inspector reviews the following CML historical thickness measurements:
- Baseline (Initial - Year 2016): $0.322\ \text{in.}$
- Previous Inspection (Year 2021): $0.297\ \text{in.}$
- Actual Inspection (Year 2026): $0.262\ \text{in.}$
The piping system operates continuously (100% duty cycle, so calendar years equal operating years).
1. Calculate Long-Term Corrosion Rate ($CR_{LT}$):
2. Calculate Short-Term Corrosion Rate ($CR_{ST}$):
3. Selecting the Controlling Rate: Since the short-term rate ($0.007\ \text{in./yr}$) is higher than the long-term rate ($0.006\ \text{in./yr}$), the controlling rate for this CML must be set to $0.007\ \text{in./yr}$ to maintain conservative safety margins.
Common Exam Traps
- Calendar vs. Operating Years: The exam may state that a pipe was installed 12 years ago but was out of service for 2 years. Ensure you divide the thickness loss by 10 operating years, not 12.
- Units Confusion: Be prepared to convert between inches and mils (where $1\ \text{mil} = 0.001\ \text{in.}$). A rate of $0.005\ \text{in./yr}$ is $5\ \text{mils/yr}$. The exam may mix these units in the question and options.
- Initial Rate Timing: Remember the 3-to-6-month verification rule. Questions frequently ask when thickness measurements must be taken to verify an estimated rate.
A carbon steel piping system has a baseline thickness of 0.375 inches in 2016. In 2021, the thickness was measured at 0.345 inches. In 2026, the thickness was measured at 0.300 inches. What are the calculated long-term and short-term corrosion rates, respectively, assuming continuous operation?
An inspector is establishing an initial corrosion rate for a newly installed piping system in a process service where no historical data is available. According to API 570, after placing the piping system in service, within what timeframe must the inspector take thickness measurements to verify the estimated rate?
A piping system was installed in a refinery 10 calendar years ago. However, the unit was shut down and nitrogen-purged for a total of 3 years during this period. When calculating the long-term corrosion rate, what time duration should the inspector use in the denominator of the corrosion rate formula?