Sulfuric Acid Corrosion
General Information
Sulfuric acid has been well-known for centuries, with the earliest documented information dating back to the Sumerian period (2000-3000 years BC). Its significance in modern times, particularly during the 19th and 20th centuries, led to numerous extensive studies on its chemical properties, such as reactivity in processes like electrophilic aromatic substitution, as well as its corrosion reactions with common construction materials such as carbon steel, stainless steels, and high chromium and molybdenum alloys.
Corrosion of carbon steel and major austenitic stainless steels like 304L and 316L has been extensively studied over the last 60-70 years. These studies have provided a relatively good understanding of the correlation between temperature, velocity, acid concentration, and corrosion rate for the respective alloys.1 ,2 ,3 ,4 The development of new Corrosion Resistant Alloys (CRAs) such as Alloy B-2, B-3, Alloy-20, and Alloy 31 has virtually eliminated or at least minimized problems associated with sulfuric acid corrosion in refining and other industries.
The main challenge in operating with sulfuric acid in many applications arises during dilution, injection, or mixing, where the concentration of the acid may fluctuate from nearly 98% to nil. Only a few expensive alloys can handle situations where sulfuric acid changes its properties from a reducing to an oxidizing system and vice versa. The presence of contaminants like ferrous ions and halides may exacerbate this effect and accelerate the degradation of steels and alloys that are virtually immune to corrosion.
In the last decade, attention has been focused on the use of polymeric materials such as cross-linked low-density polyethylene (X-LDPE) and high-density polyethylene (HDPE) for sulfuric acid storage tanks. However, at high concentrations of sulfuric acid and exposure to sunlight, the resistance of plastic materials may change, leading to unpredictable degradation of pipes or vessels.
Given the wide range of applications for sulfuric acid, it is challenging to compile an exhaustive list of problematic areas. Typical locations for H2SO4 corrosion are listed in Table 1.
Table 1 Examples of typical locations of H2SO4 corrosion.
| Process Unit | H2SO4 corrosion impacted areas |
|---|---|
| Condensate Polishing Unit (CPU) Wastewater Treatment Plant (WTP) | Concentrated acid injection skid, as a whole system with particular focus on: • Acid injection quill • Pipe segment from injection quill to first check valve • Small bore piping in injection skid (high velocities) |
| Utility & Storage | • Concentrated acid storage tank • Intermediate storage tanks • Outlet from acid pumps • Elbows and tees in concentrated acid transportation pipelines |
| H2SO4 Alkylation Unit | • Contactor (mixing section) • Spent acid lines from acid settlers and spent acid tank |
Sulfuric Acid Corrosion is governed by a combination of several factors like chemical species and concentration, temperature, materials and/or flow regimes.
To find out more information about Sulfuric Acid Corrosion and impact of various parameters register for free or buy a subscription.
Tools
Below are our user-friendly calculators and integrity tools to estimate the H2SO4 corrosion of carbon steel and selected CRAs.
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H2SO4-Corrology®
H2SO4-Corrology® is designed to provide rapid corrosion rate estimates for steels and Corrosion Resistant Alloys (CRAs) in sulfuric acid service. It allows you to evaluate the impact of key process parameters like acid concentration, temperature, and velocity on corrosion rates.
NOTICE: The provided tool is for advisory purposes only. Corrology Innovations Limited and its employees shall not be held liable for any damages, resulting from the use or inability to use the information provided.
Note: Calculation results are currently hidden. Register for Free Trial to unlock Corrosion Rate and Service Life Results.
Integrity Risk Indicator (Corrology®-IRI: H2SO4)
The Challenge: Moving Beyond Linear Estimates
In sulfuric acid service, traditional linear corrosion tracking often fails to capture the rapid transition to accelerated damage. As wall thickness decreases, risk does not grow steadily - it accelerates exponentially. Small changes in acid concentration, temperature, or velocity can also shift an alloy from a stable operating window into a severe-corrosion regime.
The Solution: The H2SO4 Integrity Risk Indicator (IRI-H2SO4)
The IRI-H2SO4 quantifies asset risk by calculating corrosion rates, service-life context, and empirical remaining-life indicators through a margin-aware, API 581-inspired engine. This tool functions as a sensitivity analysis engine, allowing you to evaluate how shifting sulfuric acid concentration, temperature, and velocity impact carbon steel and Corrosion Resistant Alloys (CRAs) in Predictive Mode to determine the most robust material for your specific operating window.
The Advantage
Access a high-speed, agile modeling engine designed for rapid, defensible engineering decisions:
Non-Linear Risk Scaling: Utilize a logarithmic-exponential transformation that reflects the true physical reality of risk escalation in late-life degradation states.
Dynamic Inspection Credit: Input your Inspection Effectiveness (Class A-E) to see how high-quality data reduces uncertainty and optimizes maintenance intervals.
Auto-Derived Prior Confidence: Prior confidence is automatically computed from the uninspected time interval (tuncertainty): <3 years = High, 3-5 years = Medium, >=5 years = Low. This applies in both Predictive and Inspection modes and remains read-only in the standard UI workflow; API and integration callers may pass priorConfidenceOverride or priorConfidence when an explicit override is required.
Precision Structural Floors: Take control of your model by setting Manual T-Min structural floors to match your equipment’s unique geometry.
Expert Calibration: Gain confidence with a model structured against a 6-point lifecycle truth set, ensuring accuracy from low-risk early life to critical thin-wall scenarios.
API 581-Aligned Risk Bands: Status and score-pill color are determined by the log probability of failure (log Pf) rather than the 0-100 score scale alone. Thresholds follow API 581 PoF magnitude ranges: log Pf <= -5 = Very Low; -5 < log Pf <= -4 = Low Risk; -4 < log Pf <= -3 = Moderate; log Pf > -3 = Critical. This ensures that improvements in inspection effectiveness are always reflected in the displayed risk band, even in high-age or thin-wall scenarios where the numerical score is saturated.
Note: The Integrity Risk Indicator (IRI-H2SO4) shown below remains a static preview. To access the live risk engine, including Manual t_min and Inspection Effectiveness credits, please upgrade to Professional+.
References
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