
In brief: Salt plants lose stainless steel to chlorides, and the two factors that decide how fast are the grade specified and the free iron left on it during fabrication. Grade 316 is 304 with about 2% molybdenum added, which is what buys chloride resistance; passivation removes the free iron and rebuilds the passive film, but it cannot replace metal already lost to a pit.
Most plants treat salt industry corrosion as a cleaning problem. It is usually a materials problem and a contamination problem, decided long before anyone picks up a hose.
Two things set the ceiling on how long your stainless lasts in chloride service. The grade you bought, and how much loose iron was left on it during fabrication. Get those wrong and no cleaning schedule rescues the equipment. Get them right and maintenance becomes routine.
For most salt equipment, yes, and the reason is one alloying element. Euro Inox describes grade 1.4401, which is AISI 316, as AISI 304 “with about 2% molybdenum added”, and says it is “particularly resistant to high levels of chloride”, which is why it suits salty foods (Stainless Steel in the Food and Beverage Industry).
That single addition separates steel that survives brine from steel that pits in it. Plants that specified 304 to save money on a brine tank learn this quickly.
Molybdenum is not a magic number. It raises the chloride level the passive film tolerates, and salt plants can still exceed it. The question is never whether 316 is good, but whether it is good for this duty at this concentration and temperature.
Evaporation is what catches people out. Feed brine may sit at a concentration the grade handles comfortably, then the same liquor concentrates through the train until the last effect runs conditions the first never sees. One grade across a whole plant is usually wasteful at the front or inadequate at the back.
The most concentrated liquor in the plant is therefore the hardest duty on the steel, and that is where evaporator bodies and heat transfer surfaces sit.
When the duty is aggressive enough that austenitic grades keep failing. Euro Inox is direct: in very corrosive environments “it may be necessary to use one of the second group of iron-carbon-chromium-nickel stainless steels”, the duplex grades.
The compositions below come from Euro Inox. The duty column is our own view of where each grade earns its place in a salt plant.
| Grade | What it carries | Where it fits in a salt plant |
|---|---|---|
| 304 (1.4301) | Chromium and nickel, no molybdenum | Dry handling, structures, non-contact frames |
| 316 (1.4401) | 304 plus about 2% molybdenum | Most brine and wet salt contact duty |
| 2304 (1.4362) | 23% chromium, duplex structure | Higher strength where chlorides are moderate |
| 2205 (1.4462) | 22% chromium, about 3% molybdenum | Concentrated brine, evaporators, hard service |
Duplex costs more, and Euro Inox notes it has general corrosion resistance similar to the austenitics but much higher mechanical strength, helped by an addition of about 0.15% nitrogen. It also resists stress corrosion cracking better.
Free iron gives chlorides a place to start. This is the part most plants underestimate, because the damage does not begin in the stainless at all.
Euro Inox puts the mechanism plainly. Particles of carbon steel embedded in a stainless surface “will not only corrode in a damp atmosphere, creating unsightly streaks of rust, but can also lead to pitting or crevice corrosion of the stainless steel in the indentation which is entrapping the carbon steel particle”.
That is contamination rather than a defect in your steel. It arrives from grinding wheels used on mild steel, from tools, and from carbon dust in a shared fabrication bay. Euro Inox recommends that stainless fabrication be carried out in an area separate from carbon steel work, and that grease, oil and crayon marks be removed with a non-chlorinated solvent.
In a salt plant that contamination sits under wet salt for months. Removing it is exactly what passivation does, and it is why new equipment should be treated before it goes into service.
Food grade changes the consequence while the chemistry stays the same. Salt is two markets with two different risk profiles, and the same pit means different things in each.
On the food grade side, the salt is specified against BIS standards for sale in India, and against ASTM D632, the Standard Specification for Sodium Chloride. A corroding surface in product contact is a contamination question and an audit question at the same time.
On the industrial and chemical grade side, the pressure is availability. A pitted evaporator means a shutdown, and in a continuous plant that is expensive in its own way. Our salt industry page sets out how we serve both sides.
The maintenance work is the same. What differs is how you justify it internally, and which auditor asks about it.
The split matters for scheduling. A food grade line has a natural window when packing stops, while a continuous plant may run for months before you can open anything. That decides whether you maintain on inspection or react to failures.
Free iron and a damaged passive film, and nothing beyond that. Being clear about the limit is more useful than overselling it.
Passivation dissolves the loose iron sitting on the surface and lets the chromium-rich film reform. ASTM A380, the Standard Practice for Cleaning, Descaling, and Passivation of Stainless Steel Parts, Equipment, and Systems, is the reference for how that work is specified.
What it cannot do is put back metal that has already gone. A pit is missing material. Passivation will clean it and slow what happens next, and the pit is still there. It also cannot correct a grade that was wrong for the duty, which is why the first two sections of this post matter more than this one.
Our passivation service runs in citric chemistry, on site or at our own premises, which matters when the equipment is too large to move.
Then the sequence changes, and cleaning is the wrong first move. Scale and corrosion product need removing before you can assess anything.
Skipping step 1 is the common error. A plant that goes straight to chemical treatment often spends the money and still cannot say whether the equipment is fit to run. Our note on common passivation failures covers the ways this goes wrong.
The record from step 5 is worth as much as the treatment. Pitting is slow, and memory is not a measurement. A dated note of where the pits were turns the next inspection into a comparison, and it answers what an auditor really asks.
Tie it to the shutdown you already have. Salt duty varies too much for a universal interval, and a plant handling saturated brine at temperature is nothing like one packing dry product.
A workable pattern is an inspection at every planned shutdown, passivation on a cycle set by what those inspections show, and unscheduled treatment after anything that damages the film: weld repairs, a brine spill onto a dry line, or a wash with the wrong chemistry.
Here is a fictional illustration, not a specific project. A plant near Dahej inspects at its April shutdown, finds the evaporator sound but the brine transfer line pitting at the weld seams, and treats only that line. The scenario is fictional. Inspection is what makes targeted work possible, and targeted work keeps the budget sensible.
Our inspection and monitoring uses imported, fully calibrated instruments, and the output is a remedy now plus a frequency for the next check.
That frequency is worth arguing about internally. Too long and you are repairing. Too short and you are spending on equipment that was fine. A record of what the same surfaces looked like last time is what settles it.
With the drawings and the surface, in that order. Find out what grade each item actually is, because purchase records and site reality often differ, then look at the welds on the wettest line you have. Weld seams carry heat tint and trapped contamination, which is why they fail first, and our note on pickling versus passivation explains which treatment that calls for.
Rouging Solutions has been treating stainless steel since 2015, with 60+ combined years across pharma, semiconductor and food processing, and 26+ clients served in 8 industries including salt. We work on site or at our own premises, and our team responds within 24 hours.
If the grade is wrong for the duty, we will say so plainly. Talk to us before your next shutdown, while the equipment is open and the decision is still cheap.
No. Passivation removes free iron and lets the passive film reform, which slows further attack, but the metal already lost to a pit does not come back. Where pitting has roughened the surface, mechanical or electropolishing is usually needed before passivation is worth doing.
For dry handling, structures and non-contact frames, often yes. For brine, wet salt and anything that stays damp, molybdenum-bearing grades are the sensible choice, because that element is what raises the chloride level the surface tolerates.
Salt sold in India is specified against BIS standards, and ASTM D632 is the ASTM specification for sodium chloride. Those govern your product. The surface treatment on the equipment that makes it is a separate matter, referenced against practices such as ASTM A380.
Welding leaves heat tint and can leave contamination, both of which weaken the passive film exactly where brine tends to sit. A weld seam also traps fabrication contamination, which is why it is the first place worth looking on any wet line.
Some of it. Inspection usually can, and so can work on isolated sections. Full-system treatment needs the line down, which is why tying it to a planned shutdown is far cheaper than reacting to a failure mid-season.
Sources. Euro Inox, Stainless Steel in the Food and Beverage Industry, Materials and Applications Series Volume 7, published by worldstainless (grade composition, chloride resistance, duplex grades and carbon steel contamination) · ASTM D632, Standard Specification for Sodium Chloride · ASTM A380/A380M, Standard Practice for Cleaning, Descaling, and Passivation of Stainless Steel Parts, Equipment, and Systems. Standards are revised periodically, so check the current edition before specifying against one. This is technical guidance for engineers, not regulatory advice.