The Acid Plants Are Not Broken. They Were Switched Off.
Table of Contents
The way this news usually arrives is not a press release. It is somebody putting their head round the door to say they have heard that two plants are down and there is a sulfuric acid shortage. That is roughly what happened to us this week, and it is worth saying up front that the person was right about the direction and wrong about the scale. The number is not two. As of the first week of August it was four facilities, the reason has almost nothing to do with anything breaking, and the most interesting part of the story is a detail about catalyst chemistry that explains why the recovery will not be as quick as the shutdown was.
We sell sulfuric acid in packaged quantities — quarts through drums and totes — in seven strengths, so we spend a lot of time explaining which market a given drum actually comes from. That turns out to be the whole point of this story. There is a real contraction going on in American acid capacity right now, and there is a great deal of loose talk about a “sulfuric acid shortage” that rolls every concentration and every grade into a single commodity moving through a single pipe. It is not one. What follows is what is genuinely down, why a fertilizer company’s margin decision removes acid capacity from the Gulf Coast, the reason an idled acid plant is a harder thing to restart than an idled boiler, and what a buyer of packaged acid should and should not conclude from any of it.
What is actually down
On 11 May 2026 Mosaic said it would cut phosphate fertilizer production by half at Faustina, Louisiana and Bartow, Florida. Bruce Bodine, the company’s president and chief executive, gave the reason plainly: “Raw material prices and availability, especially for sulfur, are forcing us to revisit our production plan.” He framed it as a waiting game rather than a retreat — “a temporary move that allows us to limit the need for incremental sulfur at today’s prices and wait until the market normalizes.”
By the second-quarter earnings call on 5 August the cuts had gone deeper than half. Louisiana was described as completely offline. Bartow was running at about 40% of capacity. New Wales and Riverview, the two large Florida plants, were in the low-to-mid 70s. Two days later, on 7 August, the company said it would curtail further, and the list grew to four sites: Bartow and Faustina, already reduced, plus Riverview and Uncle Sam. In Brazil, additional temporary curtailments and idling were under way, following an April idling of single-superphosphate production and a May halt to phosphate rock output.
| Site | State | Reported status | On-site sulphur-burning acid plants |
|---|---|---|---|
| Faustina | Louisiana | Louisiana described as “completely offline” (Q2 call) | 2 plants, 1,800 MTPD each — 3,600 MTPD |
| Uncle Sam | Louisiana | Added to the curtailment list 7 August | 3 plants, 1,500 + 1,500 + 2,900 MTPD — 5,900 MTPD |
| Bartow | Florida | About 40% of capacity | — |
| Riverview | Florida | Low-to-mid 70s; added to the list 7 August | — |
| New Wales | Florida | Low-to-mid 70s; not named in the 7 August addition | 5 plants (largest rated 3,400 STPD) |
Why the acid-plant column is the important one. It is easy to read a phosphate curtailment as a fertilizer story with no bearing on the acid market. The plant registry says otherwise. Faustina and Uncle Sam are not phosphate plants that happen to buy acid; they are sites with their own sulphur-burning sulfuric acid trains, five between them, rated at roughly 9,500 tonnes a day. Annualised, that is in the region of three million tonnes of sulfuric acid capacity whose run rate is now set by a margin calculation rather than by demand for acid.
It is worth being precise about what “down” means here, because it is not the usual industrial sense of the word. Nothing exploded. There was no fire, no force majeure event at the gate, no mechanical failure of a converter or an absorption tower. These are deliberate, reversible, economically motivated reductions in run rate, and the company has been consistent in describing them as temporary. That is genuinely better news than an accident would be. It is also, for reasons that come down to the physical chemistry of the catalyst bed, not quite as reversible as the word “temporary” makes it sound.
Why a fertilizer decision is an acid decision
Sulfuric acid and phosphate fertilizer are joined at the hip, and the joint is the wet process. Phosphate rock is mostly fluorapatite, and to get the phosphorus out of it in a usable form you attack the rock with sulfuric acid. The reaction produces phosphoric acid and a very large quantity of calcium sulfate, which is gypsum, along with hydrogen fluoride that has to be scrubbed:
Ca₅(PO₄)₃F + 5 H₂SO₄ + 10 H₂O → 3 H₃PO₄ + 5 CaSO₄·2H₂O + HF
The stoichiometry alone says five moles of sulfuric acid for every three of phosphoric, but the stoichiometry is the optimistic case. Real phosphate rock carries carbonate and other impurities that consume acid without producing anything useful, so the practical figure is higher. Published process data puts it at roughly 1,360 kg of sulfuric acid per tonne of phosphoric acid, and the working range for acid consumption is around two to three tonnes of sulfuric acid per tonne of P₂O₅ depending on the rock. Whichever number you use, the conclusion is the same: phosphate is not a side consumer of sulfuric acid. It is the main one. Roughly 56% of the world’s sulfuric acid goes into fertilizer.
That is why the demand and supply sides of this market are so awkwardly coupled. A phosphate producer that cuts output does two things at once. It stops consuming acid, which loosens the market. And, if it makes its own acid on site — which the Louisiana sites do, on a large scale — it stops producing acid, which tightens it. Which effect dominates depends on the region, the freight economics and whether those trains were selling any merchant tonnes in the first place. Anyone who tells you confidently that a phosphate curtailment is straightforwardly bullish or bearish for the acid you buy in drums is guessing.
The upstream cause of all of it is sulfur, and sulfur has been the story of 2026 since the Strait of Hormuz disruption took a large share of seaborne supply out of easy reach and export restrictions removed most of the flexible valves from the market. We wrote that up at length when it broke; if you want the feedstock side of the picture, our 2026 sulfuric acid supply crisis explainer covers where the world’s sulfur comes from and why so little of it is a free agent. The short version is that sulfur is the dominant cash cost in burning acid — estimates run from about 70% up to 80% of production cost — so an acid plant’s margin tracks the sulfur price almost one for one.
The numbers on the board explain the decision without much need for interpretation. Qatar’s sulfur contract has been settling around $805 a tonne FOB. Mosaic told investors it had locked in a significant portion of its third-quarter molten sulfur supply at $705 a tonne, which it described as considerably below spot — a useful reminder that the company is not a distressed buyer, it is a disciplined one. Against that, diammonium phosphate was assessed at about $919 a tonne and monoammonium phosphate at about $959 in early September, with DAP up around 7% year on year. Fertilizer prices are high. They are not high enough, fast enough, to make incremental tonnes of sulfur at spot worth converting, and Bodine’s summary of the global consequence was blunt: “We believe global phosphate production will fall well short of last year by up to 30 million tons.”
The counterintuitive bit. This is not a shortage in the sense of everybody wanting acid and nobody having it. It is the opposite failure mode: the feedstock is expensive enough that turning it into acid, and the acid into fertilizer, destroys value. Plants are idle because running them loses money. That is a far more stubborn problem than a broken converter, because a repair has an end date and a margin does not.
An idled acid plant is not a paused acid plant
Here is the part that almost never makes the market commentary, and it is the reason we would not assume a fast snap-back even if sulfur eased tomorrow.
Sulfuric acid is not extracted. It is burned into existence, in three steps. Molten sulfur is sprayed into a furnace and burns to sulfur dioxide. The dioxide is then oxidised to sulfur trioxide over a catalyst, which is the hard step and the one the whole plant is built around. The trioxide is then absorbed into strong acid:
S + O₂ → SO₂ · 2 SO₂ + O₂ ⇆ 2 SO₃ · SO₃ + H₂O → H₂SO₄
Most people picture that catalyst as a solid: a hard ceramic pellet with vanadium in it, sitting in a bed, doing its work. That is only half right, and the other half is what makes shutdowns expensive. Under operating conditions the active vanadium phase is not solid at all. It is a molten salt — alkali pyrosulfates that dissolve the vanadium species — spread as a very thin liquid film across the surface of a porous diatomaceous-earth or silica support. The pellet is the sponge. The catalyst is the liquid in it.
A liquid catalyst has a freezing point, and this one is inconveniently high. Below roughly 400 °C the melt is no longer molten and activity collapses; reported rates fall away sharply somewhere in the 370–400 °C region depending on the formulation and the gas. In the converter itself the active phase sits as a melt across a band of about 450–610 °C, and operators generally run around 430–450 °C as the compromise between kinetics and equilibrium, which still returns 96–98% conversion per pass. An acid plant, in other words, is a machine whose working fluid must be kept above its freezing point at all times. Cold is not a neutral state for it. Cold is a phase change.
What repeated phase changes do to the bed was set out earlier this year in Sulfuric Acid Today by Aida Barberena and Jeremy Schneider of Elessent Clean Technologies, whose MECS catalysts are among the most widely used in the industry. Their argument is that the industry persistently underestimates thermal cycling, and they identify three mechanisms that compound one another.
| Mechanism | What happens in the bed | Consequence |
|---|---|---|
| Support breaks down under thermal shock | The diatomaceous-earth support expands and contracts on every heating and cooling cycle | Microcracking and structural fatigue; loss of porosity; at higher temperatures the porous structure can collapse into a dense, amorphous mass |
| Vanadium changes oxidation state | Temperature swings shift the distribution toward less reactive vanadium species | Activity falls before any physical damage is visible; on cooling the melt can redistribute unevenly, leaving local dead zones |
| Contamination amplifies both | Ash from sulfur, dust and iron oxide lodge in the pore structure; if the gas crosses the acid dew point, condensate forms | Rising pressure drop, and active salts can be leached straight off the pellet surface |
Two details in that article deserve to be quoted rather than paraphrased. The first is a field case. A plant that went through nearly ten shutdowns in a single year — not because of anything wrong inside the acid plant, but because upstream upsets kept interrupting the hot process gas — saw the cumulative effect degrade the bed into what the authors describe as “essentially solidified dust,” forcing a premature replacement of the entire catalyst charge. The second is the sentence that ought to be pinned above every operator’s desk this year, about the temptation to rush a heat-up or admit wet gas below the acid dew point to save time: those choices “might save hours but could cost months in catalyst life.”
Where the money is. Catalyst is one of the largest consumables in an acid plant, and the premium formulations are not cheap to touch. With cesium raw-material prices climbing, the authors note that maintenance on even a small portion of a cesium bed can run to several hundred thousand dollars — and that for larger units, or multiple beds, the costs multiply quickly. The indirect bill is the one that constrains supply: lost activity means reduced capacity to hold emissions inside permit limits, and rising pressure drop means less throughput and more blower power.
None of this contradicts Mosaic’s position. The company has said it is prepared to ramp back to full rates in weeks rather than months once conditions allow, and for the fertilizer trains that is entirely plausible. But it is worth holding the two clocks separately. The commercial clock is set by the sulfur price and can turn in a week. The metallurgical clock is set by how many times a bed has been taken through a cooling cycle, and it only runs one way. A plant that cycles repeatedly through a long, uncertain curtailment is accumulating a maintenance liability that does not show up in a quarterly operating rate, and the industry’s own catalyst suppliers have been unusually direct about saying so.
What this does and does not mean for your drum
Now the part that matters if you are not a phosphate producer. The honest answer is that a fertilizer-chain contraction does not price every sulfuric acid the same way, and the single most common mistake we see during a supply scare is a buyer reacting to a headline about a market they are not actually in.
Sulfuric acid is sold by concentration, and concentration is not a cosmetic difference. It changes the freezing point, the density, the corrosion behaviour toward specific metals and plastics, and what the acid is physically able to do. It also, critically, changes which production route the material came from. Bulk 93% acid off a sulphur-burning train is the grade that shares a supply chain with fertilizer production. High-purity reagent material and purified electrolyte acid are produced and finished to different specifications for different customers, and their availability and pricing do not move in lockstep with a DAP margin in Florida.
| Grade we stock | Typically bought for | Relationship to the fertilizer-acid story |
|---|---|---|
| 93% Technical | General industrial acidification, pH control, drain and process work, pickling | Closest cousin. This is the workhorse concentration off sulphur-burning capacity, so it is the one most exposed to sulfur economics |
| 96% ACS Grade | Analytical and laboratory work where the specification is the product | Different chain. Bought against a published specification, not a commodity index |
| 50% Electrolyte Grade | Battery electrolyte and flow-battery work | Different chain, and a different purity conversation entirely |
| 37% Battery Acid | Lead-acid battery filling and topping | Dilute, pre-mixed, bought by application rather than by index |
| 70% | Process work wanting strength without full concentration | Intermediate; dilution of stronger material |
| 30% | Lighter acidification and treatment duties | Dilute; furthest from the commodity conversation |
Your grade is not their grade. If you buy packaged acid against a specification — an ACS lot, an electrolyte lot, a fixed concentration your process is validated on — the right response to a fertilizer-chain headline is to confirm your specification and your lead time, not to switch concentration. A drum of 93% is not a substitute for a drum of 96% ACS material, and it is not an upgrade either. They are different products bought for different reasons.
There is a related trap in the arithmetic. Substituting a different concentration to chase availability is not a like-for-like swap, because you are buying water as well as acid. A drum of 93% and a drum of 70% do not contain the same quantity of H₂SO₄, and re-basing a process on the wrong assumption is a more expensive error than a few weeks of lead time. If you are ever unsure what the equivalent volume is, our complete sulfuric acid concentration guide has the comparison laid out, and anyone diluting should remember the direction of the operation: acid into water, never the reverse, because the heat of dilution is substantial.
The practical advice we would give a packaged-acid buyer in September 2026 is unglamorous. Know the concentration and grade your process is actually specified on, and put it on the purchase order rather than relying on a generic description. Ask for the lot-specific Certificate of Analysis if your quality system needs the documented numbers rather than a nominal value. Talk to us about lead times before you are down to your last drum, because visibility is cheap and expediting is not. And treat a headline about acid plants in Louisiana as information about the commodity end of the market, which it is, rather than as a reason to panic about a laboratory reagent, which it is not.
What we are watching next
If you want to follow this without a subscription to a price service, there are a handful of indicators that will move before any announcement does.
- The sulfur contract settlement. Qatar’s quarterly number around $805 a tonne FOB is the reference everyone else argues with. It is the input that has to fall before curtailed capacity has a reason to come back.
- The DAP and MAP spread against it. Roughly $919 and $959 a tonne in early September. Curtailment is a margin decision, so watch the gap between fertilizer prices and sulfur cost rather than either number alone.
- Gulf terminal acid inventories. Price reporters have been describing tightening inventories at Gulf terminals. That is the closest public proxy for merchant availability in the region that matters most to North American buyers.
- Mosaic’s next quarterly call. The company has been explicit and specific about operating rates by site, which makes its calls the single most useful public document on American phosphate acid capacity.
- Restart language, not restart dates. When capacity does come back, watch whether the announcements mention catalyst screening or replacement. That is the tell for whether the cycling bill has come due.
Common questions
Is there actually a sulfuric acid shortage right now?
There is a genuine contraction in American phosphate-linked acid capacity, with four Mosaic facilities curtailed or idled as of 7 August 2026, and price reporters describe tightening inventories at Gulf terminals. But “shortage” is too blunt a word for what is happening. The constraint is the cost of sulfur rather than an absence of capacity, and it affects commodity bulk acid far more directly than it affects packaged acid bought against a specification.
Which Mosaic plants are down, and by how much?
As of the second-quarter call on 5 August 2026, Louisiana was described as completely offline and Bartow, Florida as running at about 40% of capacity, with New Wales and Riverview in the low-to-mid 70s. On 7 August the company said it would curtail further, naming four sites: Bartow, Faustina, Riverview and Uncle Sam. Additional curtailments and idling were also under way in Brazil.
Why would a company switch off a plant instead of selling the acid?
Because sulfur is the dominant cash cost in making sulfuric acid — commonly estimated at 70–80% of production cost — so when sulfur is expensive enough, converting it destroys value rather than creating it. Mosaic’s chief executive described the cuts as a temporary step to limit the need for incremental sulfur at current prices while waiting for the market to normalise.
Why can’t an idled acid plant just be switched back on?
It can, but not for free. The active phase of the catalyst is a molten alkali-pyrosulfate salt holding vanadium, spread as a thin film on a porous support, and below roughly 400 °C that melt solidifies and conversion collapses. Every shutdown and restart is a thermal cycle that microcracks the support, shifts vanadium toward less reactive species, and risks leaching active salts off the pellet if the gas crosses the acid dew point. In one documented case, nearly ten shutdowns in a year degraded a bed into what the catalyst supplier called essentially solidified dust.
Does this affect the concentration I buy?
Not uniformly. Bulk 93% acid off sulphur-burning capacity is the grade most exposed to sulfur economics. Analytical ACS material, purified electrolyte acid and pre-mixed dilute battery acid are produced and sold against specifications, and their availability does not track a fertilizer margin. The correct response is to confirm your specification and lead time rather than to substitute a different concentration.
Should I switch to a different strength if my usual grade is tight?
Only with the arithmetic done first. Different concentrations contain different quantities of H₂SO₄ per unit volume, so a substitution changes your process chemistry and your dosing, and a stronger acid is not a drop-in replacement for a weaker one. Where a specification is involved, a nominally similar concentration from a different production route may not meet it at all. Talk it through before you re-base anything.
References & Authoritative Sources
Curtailment facts and operating rates are from the company’s own announcements and earnings call plus the trade press that covered them; plant capacities are from the industry acid-plant registry; the catalyst chemistry is from the catalyst supplier’s technical article and the peer-reviewed literature below.
- Mosaic to further curtail US, Brazil phosphate output — Argus Media, 7 August 2026. The four named facilities (Bartow, Faustina, Riverview, Uncle Sam), the Brazil idling, and the curtailed raw-material availability language.
- Mosaic to scale back US phosphate production over high input costs — Agri-Pulse. The 11 May 2026 announcement of 50% cuts at Faustina and Bartow, and Bruce Bodine’s “forcing us to revisit our production plan” and “temporary move” statements.
- Mosaic Q2 2026 earnings call: locks in $705 sulfur as curbs slash global phosphate output — 5 August 2026. Operating rates by site (Louisiana offline, Bartow about 40%, New Wales and Riverview low-to-mid 70s), the $705/tonne third-quarter molten sulfur position, and the “up to 30 million tons” global phosphate statement.
- Mosaic reveals plans to reduce Brazil and US output — World Fertilizer. Independent coverage of the same curtailment programme.
- How shutdown-startup cycles quietly destroy catalyst lifetimes (PDF) — Aida Barberena and Jeremy Schneider, Elessent Clean Technologies, reprinted from Sulfuric Acid Today, Spring/Summer 2026. Thermal-cycling mechanisms, the diatomaceous-earth support, the vanadium oxidation-state shift, the acid dew-point leaching, the ten-shutdowns field case and “essentially solidified dust,” the cesium-bed cost, and “might save hours but could cost months in catalyst life.”
- Oxidation of sulfur dioxide over supported vanadia catalysts (PDF) — Lehigh University Operando Molecular Spectroscopy & Catalysis Laboratory. The molten-salt nature of the active vanadium phase under reaction conditions and the thin liquid film on the silica support.
- Progress on the mechanistic understanding of SO₂ oxidation catalysts — Catalysis Today. Molten alkali pyrosulfates dissolving the vanadium species, and the collapse of activity below the melt temperature.
- 40 CFR 60.203 — Standards of performance for wet-process phosphoric acid plants (PDF) — US Government Publishing Office. The regulatory definition of the wet-process plant this article describes.
- Sulphur prices, trend and forecast — ChemAnalyst. The Qatar contract settlement around $805/tonne FOB and the wider sulfur price context.
- 6 of 8 Fertilizer Prices Lower, Led by UAN28 — DTN/Progressive Farmer, 9 September 2026. Early-September DAP and MAP average prices and the year-on-year comparison.
- Sulfuric acid production cost model — IMARC Group. Elemental sulfur as the dominant share of production cost, and the sensitivity of acid economics to feedstock price.
The three we would put on the bench
Sulfuric Acid 93% Technical Grade
The industrial workhorse concentration, and the one closest to the commodity story above.
Sulfuric Acid 50% Electrolyte Grade
For battery and flow-battery work, where purity is the specification that matters.
Not sure which strength your process is actually specified on?
Tell us the application, the concentration you are running today and the container size you receive it in, and we will confirm the grade and work out the equivalent volume if you are considering a different strength. If a substitution would change your process chemistry, we will say so rather than ship you the nearest thing in stock.
Browse sulfuric acid by strength and sizeKey numbers and sources
| Number | What it is | Source |
|---|---|---|
| 4 facilities | Mosaic sites curtailed or idled: Bartow, Faustina, Riverview, Uncle Sam | Argus Media, 7 Aug 2026 |
| Offline / ~40% | Louisiana operating status and Bartow rate | Mosaic Q2 2026 call |
| 3,600 + 5,900 MTPD | Sulphur-burning acid capacity at Faustina and Uncle Sam | Acid-plant registry |
| $805 / $705 | Qatar sulfur contract FOB, and Mosaic’s locked Q3 molten sulfur price | ChemAnalyst; Mosaic Q2 call |
| ~400 °C | Below this the vanadium pyrosulfate melt solidifies and activity collapses | Catalysis literature |
| 70–80% | Sulfur as a share of sulfuric acid production cost | IMARC production cost model |
Frequently Asked Questions
Is there actually a sulfuric acid shortage right now?
There is a genuine contraction in American phosphate-linked acid capacity, with four Mosaic facilities curtailed or idled as of 7 August 2026, and price reporters describe tightening inventories at Gulf terminals. But "shortage" is too blunt a word for what is happening. The constraint is the cost of sulfur rather than an absence of capacity, and it affects commodity bulk acid far more directly than it affects packaged acid bought against a specification.
Which Mosaic plants are down, and by how much?
As of the second-quarter call on 5 August 2026, Louisiana was described as completely offline and Bartow, Florida as running at about 40% of capacity, with New Wales and Riverview in the low-to-mid 70s. On 7 August the company said it would curtail further, naming four sites: Bartow, Faustina, Riverview and Uncle Sam. Additional curtailments and idling were also under way in Brazil.
Why would a company switch off a plant instead of selling the acid?
Because sulfur is the dominant cash cost in making sulfuric acid — commonly estimated at 70–80% of production cost — so when sulfur is expensive enough, converting it destroys value rather than creating it. Mosaic's chief executive described the cuts as a temporary step to limit the need for incremental sulfur at current prices while waiting for the market to normalise.
Why can't an idled acid plant just be switched back on?
It can, but not for free. The active phase of the catalyst is a molten alkali-pyrosulfate salt holding vanadium, spread as a thin film on a porous support, and below roughly 400 °C that melt solidifies and conversion collapses. Every shutdown and restart is a thermal cycle that microcracks the support, shifts vanadium toward less reactive species, and risks leaching active salts off the pellet if the gas crosses the acid dew point. In one documented case, nearly ten shutdowns in a year degraded a bed into what the catalyst supplier called essentially solidified dust.
Does this affect the concentration I buy?
Not uniformly. Bulk 93% acid off sulphur-burning capacity is the grade most exposed to sulfur economics. Analytical ACS material, purified electrolyte acid and pre-mixed dilute battery acid are produced and sold against specifications, and their availability does not track a fertilizer margin. The correct response is to confirm your specification and lead time rather than to substitute a different concentration.
Should I switch to a different strength if my usual grade is tight?
Only with the arithmetic done first. Different concentrations contain different quantities of H2SO4 per unit volume, so a substitution changes your process chemistry and your dosing, and a stronger acid is not a drop-in replacement for a weaker one. Where a specification is involved, a nominally similar concentration from a different production route may not meet it at all. Talk it through before you re-base anything.
