Separating gases at scale is, at its core, an exercise in exploiting small physical differences under precisely controlled conditions. Cryogenic distillation does this by cooling gas mixtures to temperatures where components condense and vaporize at different rates – a process that sounds straightforward until you're managing a column operating at –170°C with product purity requirements measured in parts per million.
The technology has been industrially mature for over a century, but "mature" doesn't mean static. Equipment design, process integration, and the range of recoverable products have all evolved substantially, particularly as demand for trace atmospheric gases has grown in semiconductor manufacturing, space propulsion, and medical applications.
The Physical Basis: Why Cryogenic Distillation Works
All distillation separations rely on differences in volatility between components. In gas separation, the relevant property is the boiling point at a given pressure. Nitrogen boils at –196°C at atmospheric pressure; oxygen at –183°C; argon at –186°C. These differences – some of them quite small – are what the distillation column is engineered to exploit.
The process begins with compression and pre-cooling of the feed air stream, followed by the removal of water vapor and carbon dioxide, which would freeze and block equipment at cryogenic temperatures. The cleaned, compressed air is then cooled in a heat exchanger against returning product and waste streams before entering the cold box – the insulated assembly where separation actually occurs.
Inside the cold box, distillation columns operating at different pressures achieve the primary separations. The double-column arrangement common in air separation plants uses a higher-pressure column to produce a crude separation, feeding into a lower-pressure column for final product purification. Liquid and vapor streams interact across structured packing or distillation trays, with heavier components (higher boiling point) concentrating toward the bottom and lighter components toward the top.
Argon Recovery: Where the Engineering Gets Interesting

Oxygen and nitrogen separation is thermodynamically favorable. The boiling point difference is sufficient that high-purity products are achievable in a standard double-column configuration. Argon is more demanding.
Argon's boiling point (–186°C) sits between oxygen (–183°C) and nitrogen (–196°C), which means it tends to concentrate in intermediate regions of the distillation column rather than reporting cleanly to either product stream. Recovering argon at high purity requires a dedicated side column – the crude argon column – fed from a specific draw point in the low-pressure column where argon concentration is highest.
Crude argon from this column still contains percent-level oxygen contamination. Final purification to the grades required for welding, electronics manufacturing, or analytical applications requires either catalytic oxygen removal followed by drying, or a further distillation stage. The choice between these routes depends on target purity, plant scale, and whether hydrogen is available for the catalytic route.
Cryoin Europe works with argon across this full production and purification range, which is relevant context for understanding the process depth behind high-purity argon supply.
Noble Gas Recovery: A Different Scale of Challenge
Krypton and xenon present a qualitatively different separation problem. Their atmospheric concentrations – roughly 1.1 ppm for krypton and 0.086 ppm for xenon – mean that recovering useful quantities requires processing enormous volumes of air through the primary separation plant before the concentration and purification stages for these components even begin.
In practice, noble gas recovery is integrated into large air separation units as an add-on process. A krypton/xenon-enriched liquid oxygen fraction is withdrawn from the main column and fed to a dedicated concentration unit – typically a smaller distillation column – where the noble gases accumulate in the bottom fraction while oxygen is stripped overhead and returned to the main process.
The resulting crude Kr/Xe fraction contains both gases alongside residual oxygen and trace contaminants including hydrocarbons, which concentrate from the feed air despite upstream removal steps. Subsequent purification requires catalytic combustion of hydrocarbons, drying, and then the separation of krypton and xenon from each other since they have different boiling points and are used in different applications.
This multi-stage process is what Cryoin Europe specializes in for its noble gas product range. The feedstock is the byproduct stream from air separation; the output is specification-grade krypton and xenon for industrial and high-technology end uses.
Heat Integration and Energy Consumption
Cryogenic processes are energy-intensive by nature. Compressing air to the pressures required for liquefaction, then removing that compression heat and cooling the stream to cryogenic temperatures, represents a substantial electricity demand. For large industrial ASUs, energy cost is typically the dominant operating expense.

