How Is Argon Made From Air? The Process Explained

Argon is extracted from ordinary atmospheric air through a process called cryogenic distillation, which chills air to extremely low temperatures until its component gases liquefy and can be separated based on their different boiling points. The atmosphere is about 0.93 percent argon by volume, making it the third most abundant atmospheric gas after nitrogen and oxygen, and air remains the only commercially meaningful source. The industrial infrastructure behind this seemingly simple idea is enormous, energy-intensive, and surprisingly elegant in its engineering.

Why Air Is the Only Practical Source

Argon does not form chemical compounds under normal conditions. It is a noble gas, meaning it almost never reacts with anything, so you cannot mine an argon ore or synthesize it through a chemical reaction the way you might produce, say, ammonia. The atmosphere is essentially a massive, constantly replenished reservoir of the gas. Earth’s argon is overwhelmingly the isotope argon-40, produced over billions of years by the radioactive decay of potassium-40 in the planet’s crust and mantle. That argon slowly escaped into the atmosphere and accumulated there.

At roughly 0.93 percent of the atmosphere, argon is far more abundant than most people assume. There is more argon in the air than water vapor in many climates, and about 23 times more argon than carbon dioxide. This abundance is what makes air separation economically viable: every 100 cubic meters of air you process contains almost a full cubic meter of argon, along with roughly 78 cubic meters of nitrogen and 21 of oxygen. All three are valuable industrial products, and modern air separation units are designed to recover all of them simultaneously.

Cleaning the Air Before It Enters the Plant

Before air can be cooled to cryogenic temperatures, it has to be scrubbed of impurities that would freeze solid and clog the equipment. Moisture is the most obvious problem: water ice would block the narrow passages of heat exchangers within minutes. Carbon dioxide poses the same risk, since it freezes at a higher temperature than the operating conditions of the cold box. Trace hydrocarbons are a safety concern because some can concentrate and become flammable in oxygen-rich streams.

The cleanup step typically uses adsorption beds filled with materials like alumina and zeolites. Compressed feed air passes through these beds, which trap water vapor, CO₂, and hydrocarbons on their surfaces. The beds are regenerated cyclically, either by swinging the pressure down or by heating them, so the plant runs continuously with one bed actively cleaning air while the other regenerates. Industry specifications call for extremely low impurity levels after this step, with water vapor reduced to around 0.1 parts per million and carbon dioxide to about 1 part per million.

1ScienceDirect. Sorbents for air prepurification in air separation

Cooling Air Until It Liquefies

Once the air is clean, the real work begins: bringing it down to cryogenic temperatures, roughly minus 190 degrees Celsius, where nitrogen and oxygen become liquids. This cooling is accomplished through a combination of compression, heat exchange, and expansion.

The basic concept dates back to the late 1800s. You compress air, remove the heat of compression, and then let the high-pressure air expand rapidly. That expansion cools the gas dramatically. The cold gas is routed back through a heat exchanger to pre-cool the incoming compressed air, and the cycle repeats, each pass getting colder than the last, until the air begins to liquefy. The earliest version of this idea, the Linde-Hampson cycle, used only a throttle valve for expansion. Modern plants improve on it substantially by diverting part of the compressed air through a turbine expander, which extracts useful work and achieves deeper cooling more efficiently. This approach, known as the Claude or Claude-Heylandt cycle, reduces the amount of mechanical energy the compressors need to supply by carefully managing the temperature difference between the warm incoming stream and the cold returning stream inside the heat exchanger.

2PubMed Central. Optimization of Cryogenic Gas Separation Systems Based on Exergetic Analysis-The Claude-Heylandt Cycle for Oxygen Separation

The result is a stream of liquefied air entering the distillation section of the plant. At this point, you have a cold liquid mixture of nitrogen, oxygen, and argon, along with trace amounts of other noble gases like neon, krypton, and xenon.

Separating Argon by Distillation

Cryogenic distillation works on the same principle as distilling alcohol from a fermented liquid, just at much lower temperatures. Different gases have different boiling points: nitrogen boils at about minus 196°C, argon at minus 186°C, and oxygen at minus 183°C. When you partially boil a liquid air mixture, nitrogen (the most volatile) preferentially enters the vapor phase and rises, while oxygen (the least volatile) tends to stay liquid and sinks. Argon sits between them, which makes it both recoverable and tricky to isolate in high purity.

A standard large-scale air separation unit uses two linked distillation columns, commonly called the high-pressure and low-pressure columns. These are tall, packed or trayed vessels where rising vapor and falling liquid continuously exchange heat and mass. Nitrogen concentrates at the top of the columns, oxygen at the bottom, and argon accumulates in a zone partway up the low-pressure column where the oxygen-to-argon ratio is most favorable. A side draw from this zone pulls off a crude argon stream, typically containing around 2 to 5 percent oxygen along with argon, and routes it to a dedicated argon column for further purification. The interconnection between these columns is complex: they share heat through a condenser-reboiler at their junction, and the operating conditions in one column directly affect what happens in the other.

3ScienceDirect. Dynamic Modelling and Control of Cryogenic AIR Separation Plants

The crude argon column, sometimes called the side-arm column, strips most of the remaining oxygen out of the argon stream through additional distillation stages. Older plants used a catalytic reactor to remove the last traces of oxygen by reacting it with added hydrogen to form water, which was then dried out. Many newer plants skip the hydrogen entirely and use additional distillation stages instead, achieving oxygen removal to below a few parts per million purely through physical separation. This “no-hydrogen” approach is safer and simpler, though it requires more distillation trays and tighter process control.

Getting to High Purity

The argon that comes off the crude argon column is typically in the range of 95 to 98 percent pure. For many industrial uses, including welding shielding gas and certain metallurgical processes, purity requirements start at 99.99 percent and go up from there. Semiconductor manufacturing demands even higher purity, sometimes 99.9999 percent (often written as “6N” purity, for six nines).

Reaching those levels requires a final purification step. In plants that still use the catalytic deoxidation approach, the crude argon is warmed, mixed with a slight excess of hydrogen, and passed over a palladium or nickel catalyst where the oxygen reacts with hydrogen to form water. The water is then removed by adsorption drying, and the remaining gas is essentially pure argon with trace hydrogen, which can be removed by a further adsorption or gettering step. In all-distillation plants, the final purity is achieved purely by adding more theoretical separation stages, which avoids introducing any new chemicals into the product stream.

The finished product is stored either as a high-pressure gas in cylinders and tube trailers, or as a cryogenic liquid in insulated tanks. Liquid argon is the preferred form for bulk transport because it is far denser than the gas, so a single tanker truck can deliver the equivalent of thousands of gas cylinders.

The Energy Cost of Making Argon

Cryogenic air separation is energy-hungry. The main electricity consumer is the air compressor at the front end of the plant, which typically accounts for the large majority of total power consumption. Argon is the most energy-intensive product to recover on a per-kilogram basis because it is the least abundant of the three main products and requires the most separation work. One detailed simulation of a plant processing 100 kilograms of air per second found that the specific power consumption for argon was about 17.35 kilowatt-hours per kilogram, compared with roughly 0.32 kWh/kg for oxygen and 0.37 kWh/kg for nitrogen.

4Applied Thermal Engineering. Potential for improving the energy efficiency of cryogenic air separation unit (ASU) using binary heat recovery cycles

That gap makes sense when you consider the concentrations involved. The plant is designed primarily to produce oxygen and nitrogen, which together make up 99 percent of the feed. Argon at under 1 percent is almost a byproduct, and teasing it out to high purity from gases with very similar boiling points demands many additional distillation stages and careful heat management. The argon column is, in a sense, a precision instrument bolted onto the side of what is already a large industrial process.

There is active research into reducing these energy costs. An optimization study of a thermally integrated air separation plant in Colombia showed that under improved operating conditions, the plant could achieve around a 58 percent average reduction in specific energy consumption while also recovering more argon.

5Chemical Engineering Research and Design. Modeling, validation and exergy evaluation of a thermally-integrated industrial cryogenic air separation plant in Colombia. Part II. Optimization under variable products demand

Waste heat recovery systems offer another avenue. By attaching an organic Rankine cycle to capture low-grade heat that the plant would otherwise reject, engineers have shown power consumption reductions of up to 11 percent across all three product streams.

4Applied Thermal Engineering. Potential for improving the energy efficiency of cryogenic air separation unit (ASU) using binary heat recovery cycles

Why Cryogenic Distillation Still Dominates

Given the energy costs, you might wonder why the industry has not moved on to something cheaper. The answer is that cryogenic distillation scales extremely well, produces multiple high-purity products from a single feed stream, and can deliver enormous volumes. A single large air separation unit can produce thousands of tonnes of oxygen, nitrogen, and argon per day. No competing technology comes close to matching that throughput at comparable purity.

Non-cryogenic methods do exist for oxygen and nitrogen production. Pressure swing adsorption and membrane separation can produce moderately pure oxygen or nitrogen for applications that do not need extreme purity or enormous quantities. But argon is a much harder target for these methods. Argon and oxygen have almost identical molecular sizes (argon’s kinetic diameter is about 3.4 angstroms versus oxygen’s 3.46), and argon is chemically inert, so you cannot exploit a chemical affinity the way you can with oxygen on certain adsorbents. Separating argon from oxygen by adsorption at ambient temperature has historically required expensive silver-exchanged zeolites, which preferentially adsorb oxygen over argon but add significant cost and complexity.

For smaller-scale argon needs, some plants recover argon from industrial off-gases, but these sources are niche. The vast majority of the world’s argon supply comes from cryogenic air separation units co-producing oxygen and nitrogen.

New Materials That Could Change the Game

The difficulty of separating argon from oxygen without cryogenics has attracted researchers working on advanced porous materials. The most promising recent developments involve metal-organic frameworks, or MOFs, which are crystalline materials with precisely tunable pore sizes and surface chemistries. The idea is to design a material whose pores are shaped to preferentially grab argon atoms while letting oxygen molecules pass through.

Two recent studies illustrate where this research stands. One group engineered a MOF called TYUT-20 with pores shaped to match the spherical profile of argon atoms while repelling the elongated shape of oxygen molecules. The material achieved an argon adsorption capacity of 14.5 cubic centimeters per gram and an argon-over-oxygen selectivity of 1.54 at room temperature and atmospheric pressure.

6Angewandte Chemie. A Metal‐Organic Framework with Tailored Shape‐Matched Interactions Towards Ambient‐Temperature Argon Removal for Oxygen Purification

A separate team optimized an aluminum-based MOF called Al-FUM by tuning its pore size and internal polarity to favor argon adsorption through stronger molecular interactions. Al-FUM reached an argon uptake of 7.2 cubic centimeters per gram and achieved argon/oxygen selectivity of 1.28, outperforming all previously reported non-silver-based adsorbents. In dynamic experiments, it produced oxygen at over 99.99 percent purity from an argon-oxygen mixture in a single pass under ambient conditions.

7Chemical Engineering Science. Selective recognition of argon by an aluminum-based MOF for oxygen recovery from Ar/O2 mixture under ambient conditions

These selectivities are modest compared to what cryogenic distillation achieves, and the adsorption capacities are still low for industrial-scale production. But the fact that any material can preferentially adsorb argon over oxygen at room temperature is itself a noteworthy achievement, given how chemically similar the two gases are. If these materials can be scaled up and their capacities improved, they could eventually allow argon recovery without the enormous energy penalty of cooling air to cryogenic temperatures. For now, they are most relevant as a potential way to polish the crude argon-oxygen mixture that comes off the main distillation columns, potentially replacing or supplementing the dedicated argon column.

What Argon Is Actually Used For

Understanding the scale of the production process helps when you realize how much argon modern industry consumes. The largest single use is as a shielding gas in welding. When you weld metals like steel, aluminum, or titanium, the molten metal reacts readily with oxygen and nitrogen in the air, creating weak, porous, or brittle joints. Flooding the weld zone with argon displaces the reactive gases and protects the molten pool. Argon is preferred over other noble gases for this job because it is dense enough to form a stable blanket over the weld, cheap enough to use in large volumes, and completely inert.

Steelmaking is another major consumer. In the argon-oxygen decarburization process, argon is blown through molten steel alongside oxygen to reduce the carbon content without excessive oxidation of valuable alloying elements like chromium. The semiconductor industry uses ultra-high-purity argon as a sputtering gas to deposit thin films onto silicon wafers and as a carrier gas in crystal growth processes. Lighting is a smaller but familiar use: incandescent bulbs and many fluorescent and discharge lamps contain argon because it conducts heat poorly, which helps keep the filament hot, and it does not react with the filament material.

Double-pane windows filled with argon instead of air provide better thermal insulation because argon’s thermal conductivity is lower than that of nitrogen or oxygen. This is a growing market as building energy codes tighten around the world. Scientific research uses argon in particle detectors, in laboratory glove boxes for handling air-sensitive chemicals, and as a carrier gas in analytical instruments like mass spectrometers.

How Plant Operations Adapt to Demand

One underappreciated aspect of argon production is that it is not independent of oxygen and nitrogen demand. Because all three gases come from the same feed stream and the same distillation system, the plant’s operating conditions are a constant balancing act. When a customer needs more oxygen, the plant adjusts its distillation columns accordingly, and this can affect how much argon is available for recovery. If nitrogen demand spikes, the operator shifts the column profiles to favor nitrogen purity at the top, which again changes the argon concentration at the side draw.

Weather affects things too. Hot, humid air contains more water vapor, which means the pre-purification beds work harder and may need more frequent regeneration. Atmospheric pressure and temperature changes alter the density of the incoming air and the performance of the compressors. Plants in tropical climates face different optimization challenges than those in arid or cold regions. The operators and control systems running these plants are constantly tuning dozens of variables to maximize recovery of all three products while staying within energy and equipment constraints.

3ScienceDirect. Dynamic Modelling and Control of Cryogenic AIR Separation Plants

This interconnectedness occasionally causes real-world supply disruptions. When a major air separation unit goes down for maintenance or an unexpected shutdown, the argon market can tighten quickly because the lost argon production cannot be easily made up by other plants already running at capacity. The steel and electronics industries have both experienced argon shortages in recent years when clusters of air separation units went offline simultaneously. Unlike oxygen and nitrogen, which have some alternative production routes, argon supply is almost entirely tied to these cryogenic plants, making it more vulnerable to disruptions.

Shauna Matsumoto

Shauna Matsumoto teaches chemistry and physical science at a public high school. With 13 years in the sciences, she worked in industrial chemical production and refinery laboratories before entering the classroom. Matsumoto also contributes pieces on industrial chemistry to Biology Insights.