Module 2.6 — Hydrazine vs. carbohydrazide vs. sulfite: how they work, how they're selected, and the health and handling considerations that drive real-world choices.
| Agent | Reaction Byproducts | Toxicity Profile | Pressure Suitability |
|---|---|---|---|
| Hydrazine (N₂H₄) | Nitrogen, water — no TDS added | Suspected carcinogen; strict handling required | Historically all pressures; now largely legacy |
| Carbohydrazide | Decomposes to hydrazine-like intermediates then N₂/H₂O — no TDS added | Significantly lower toxicity than hydrazine | All pressures, including high-pressure/supercritical |
| Sodium Sulfite | Sodium sulfate — adds dissolved solids | Low toxicity, easy handling | Low-to-moderate pressure only — TDS addition limits high-pressure use |
Click any agent to see its tradeoffs. The choice isn't just "which removes oxygen best" — it's a three-way tradeoff between byproduct chemistry, toxicity, and pressure-class suitability.
Module 1.1 introduced the deaerator's job: mechanically stripping the bulk of dissolved oxygen from feedwater by heating it near saturation temperature. Mechanical deaeration typically gets dissolved oxygen down to a few hundred ppb but rarely to zero, and even a few ppb of residual oxygen is enough to drive meaningful corrosion over time in a system that operates continuously for years. Oxygen scavengers are the chemical cleanup step that finishes the job mechanical deaeration starts, reacting directly with residual dissolved oxygen to remove it from solution.
Hydrazine (N₂H₄) reacts with dissolved oxygen to form nitrogen gas and water — genuinely clean byproducts that add no dissolved solids to the system, which made it attractive for decades across all pressure classes including high-pressure and supercritical units. The complication is toxicity: hydrazine is classified as a suspected human carcinogen, requiring strict handling, storage, and exposure control procedures. This health profile is the single biggest reason the industry has broadly moved toward alternatives over recent decades, even though hydrazine's chemistry performance was never really the problem.
Carbohydrazide decomposes in feedwater conditions through intermediate compounds before ultimately reacting to remove oxygen, producing nitrogen and water as final byproducts — the same clean, TDS-free outcome as hydrazine, without hydrazine's toxicity profile. This combination (hydrazine-equivalent performance and byproduct cleanliness, without hydrazine's health hazard) is why carbohydrazide has become the common default choice for units needing an oxygen scavenger across pressure classes, including high-pressure and supercritical service where TDS-free byproducts matter most.
Sodium sulfite reacts with dissolved oxygen to form sodium sulfate, a straightforward, low-toxicity, easy-to-handle reaction. Its limitation is exactly what carbohydrazide and hydrazine avoid: sodium sulfate is a dissolved solid that adds directly to boiler water TDS. On a lower-pressure drum boiler already running phosphate treatment with blowdown handling TDS control, that addition is manageable and sulfite's low handling burden makes it an attractive, simple choice. On a high-pressure or once-through unit, that same TDS addition is disqualifying.
| Factor | Hydrazine | Carbohydrazide | Sulfite |
|---|---|---|---|
| TDS added | None | None | Yes (sodium sulfate) |
| Toxicity | High — suspected carcinogen | Low | Low |
| High-pressure/AVT suitable | Yes (legacy) | Yes | No |
| Current industry status | Declining, being phased out | Common modern default | Still common on lower-pressure units |