H2S Corrosion in Manholes: Why It Happens and How to Stop It
Of all the forces working to destroy concrete manholes, hydrogen sulfide (H2S) gas is among the most destructive and least understood by the public works professionals tasked with managing it. H2S-driven concrete corrosion is responsible for billions of dollars in annual infrastructure losses across North American wastewater systems — yet many municipalities still don’t have a systematic plan to address it.
This guide explains the science behind H2S corrosion, how to recognize it in the field, and which rehabilitation strategies deliver the best long-term protection.
The Chemistry of H2S Corrosion
The process that destroys concrete manholes begins not with H2S itself, but with what happens to it. Here’s the sequence:
- Organic material in sewage decomposes anaerobically, producing hydrogen sulfide gas dissolved in the wastewater
- As turbulence releases H2S from solution (especially at drop connections and changes in grade), it concentrates in the manhole’s headspace
- Naturally occurring bacteria — primarily Acidithiobacillus thiooxidans — colonize the moist concrete surface above the waterline
- These bacteria oxidize H2S to sulfuric acid (H2SO4) as a metabolic byproduct
- Sulfuric acid reacts with calcium hydroxide in the concrete, forming calcium sulfate (gypsum) — a compound that has no structural strength
- The gypsum layer swells, cracks, and spalls, exposing fresh concrete to the cycle
Under severe conditions, this process can destroy concrete at rates of 3/8 inch per year or more. A 6-inch-thick manhole wall can be compromised to the point of structural failure within 15–20 years in high-H2S environments.
Risk Factors: Which Manholes Are Most Vulnerable
Not all manholes face equal H2S exposure. The highest-risk conditions include:
- Low-flow sewer segments — slower flow means more time for sulfide generation in the biofilm
- Long transmission lines — sulfide accumulates with retention time
- Warm temperatures — H2S generation rates roughly double for every 10°C increase in wastewater temperature
- High organic load — more substrate for sulfate-reducing bacteria
- Flat-grade mains — less turbulent flow, less oxygen, more anaerobic conditions
- Drop manholes — the turbulence of the drop supercharges H2S release to the headspace
Field Identification of H2S Corrosion
Before specifying a rehabilitation approach, inspectors need to accurately characterize the type and extent of corrosion. Key indicators include:
- Soft, mushy concrete — the gypsum conversion layer feels soft when probed with a screwdriver or pick
- White crystalline deposits — gypsum precipitate on the concrete surface
- Aggregate exposure — the cement paste has been consumed, leaving coarse aggregate “floating” in a weak matrix
- Loss of section — measurable reduction in wall thickness from original design
- Sulfurous odor — strong H2S smell (though at dangerous concentrations, H2S deadens the sense of smell — always use gas monitoring equipment)
Using NASSCO’s MACP protocol, H2S corrosion is classified on a five-grade scale from Grade 1 (surface deposit/light deterioration) to Grade 5 (loss of section, imminent structural failure). Proper MACP scoring drives your rehabilitation prioritization — learn more in our Technical Resources section.
Rehabilitation Options: Matching the Method to the Damage
Polyurea Spray-Applied Linings (Grade 1–3)
For manholes with mild to moderate H2S corrosion, spray-applied polyurea systems provide excellent protection. A properly prepared and applied polyurea liner creates a seamless, impermeable barrier that blocks H2S contact with the concrete substrate and resists acid attack at pH levels down to 1.
Key advantages: fast cure times (minutes, not hours), exceptional adhesion to properly prepared concrete, flexibility to bridge minor cracks, and proven 20+ year service records in the field. See our detailed guide on polyurea application best practices.
Cementitious Coatings (Grade 1–2)
Calcium aluminate cement (CAC) or modified Portland cement coatings can provide cost-effective protection in lower-risk environments. These systems rely on a different chemistry than OPC concrete — CAC converts to hydrates that are more resistant to sulfuric acid attack. However, they are not impermeable and perform best as a preventive measure rather than a corrective one.
Structural Relining (Grade 3–5)
When H2S corrosion has advanced to loss of section or structural compromise, a protective coating alone is insufficient. Structural relining systems — including fiberglass reinforced polymer (FRP) inserts, structural spray liners, or full reconstruction — are required to restore structural integrity before applying a protective barrier.
For extreme cases (Grade 4–5), replacement may be more cost-effective than rehabilitation. Our cost comparison tool can help you run the numbers for your specific situation — visit our Resources page.
The Cost of Doing Nothing
The temptation to defer H2S corrosion rehabilitation is understandable — competing budget priorities, the “invisible” nature of underground damage, and the perceived complexity of specification and procurement all contribute to delay. But the math is unambiguous: every year of deferred rehabilitation on a high-H2S manhole adds disproportionately to the eventual repair cost.
A manhole that can be rehabilitated with spray-applied polyurea for $3,000–$5,000 today may require full structural relining ($8,000–$15,000) within five years, and complete replacement ($25,000–$80,000 depending on depth and location) within ten. The $100,000 Manhole article on this site illustrates this cost escalation with a real municipal case study.
Getting Started with an H2S Assessment Program
The first step toward managing H2S corrosion systematically is understanding your system’s risk profile. This means:
- Mapping your collection system to identify long, flat, warm-weather segments with high organic load
- Deploying H2S monitoring equipment at high-risk manholes to establish baseline gas levels
- Conducting MACP inspections on high-risk manholes to establish current condition grades
- Building a rehabilitation priority queue based on condition grade, risk factors, and consequence of failure
- Developing a capital plan that addresses the highest-priority manholes first while implementing a preventive lining program for assets still in good condition
Our upcoming webinars include sessions on MACP scoring, H2S monitoring, and rehabilitation planning. Join the community to register.

Dave Kowalski
3 months agoExcellent breakdown of the chemistry involved. We’ve been dealing with H2S corrosion in our system for years and this matches exactly what we’re seeing in the field. The note about H2S deadening your sense of smell is something we drill into every crew during safety training — can’t say it enough.
Lisa Marchetti
3 months agoGreat resource. I’d add that the bacterially-mediated corrosion process can be slowed by pH elevation — some utilities have had success with calcium hydroxide slurry treatments to raise the biofilm pH. Not a substitute for proper rehabilitation, but worth knowing as a supplemental strategy.
Randy Owens PE
3 months agoThe Grade 3 decision point for protective coating vs. structural relining is exactly right. We’ve seen too many projects that specified polyurea on manholes that needed structural work first — you’re just papering over a structural problem.