2025 Guide: Cryogenic ASU for Container-Glass Production

cryogenic ASU

A cryogenic ASU is a large-scale industrial gas system designed to separate air into its primary components: oxygen, nitrogen, and occasionally argon. It operates on the principle of cryogenic distillation, taking advantage of different boiling points of gases at extremely low temperatures. Here’s how it works: First, ambient air is drawn into the ASU and compressed to a high pressure by an air compressor. The compressed air is then cooled and passed through purification units to remove moisture, carbon dioxide, and hydrocarbons – impurities that would freeze solid in the cold temperatures ahead. Next, the clean, dry air is directed into a heat exchanger and cooled to sub-zero cryogenic temperatures (around -300°F / -185°C) until it liquefies. The liquefied air enters a distillation column system inside a tall insulated cold box. In this double-column (low-pressure and high-pressure) distillation setup, oxygen and nitrogen separate based on their boiling points: oxygen (boiling ~ -183°C) liquefies at a higher temperature than nitrogen (boiling ~ -196°C). As the mixture boils and re-condenses on trays inside the column, oxygen concentrates in the lower part as a liquid, while nitrogen rises as a vapor. The result is two primary product streams – one of high-purity oxygen and one of high-purity nitrogen. The oxygen stream can be drawn off as a gas or liquid. In a typical on-site configuration for a glass plant, gaseous oxygen (often 95–99.5% oxygen purity) is delivered from the ASU cold box to the furnace through pipelines at the desired pressure. The ASU keeps producing oxygen continuously to meet the furnace demand. The other stream is nitrogen, which is produced in excess (since air contains four times more nitrogen than oxygen by volume). Nitrogen recovery from a cryogenic ASU provides nitrogen gas that can be used elsewhere in the plant or stored as liquid. Some ASU designs also have an additional column to extract argon (present ~1% in air), but argon is usually not required for glass production and may be vented or captured only in larger plants. The entire ASU is highly automated, with control systems maintaining the proper temperatures, pressures, and flows to ensure consistent purity and output. Cryogenic ASUs are known for their reliability; once started, they run continuously for months or years with minimal downtime. This reliability is vital for container-glass plants, as the glass furnace operates 24/7 and depends on a steady oxygen feed. In terms of integration, the ASU becomes the on-site source of oxygen supply, often complemented by a backup system (such as a reserve liquid oxygen tank) to keep the furnace running if the ASU needs maintenance. Overall, the cryogenic ASU is the workhorse that enables large-scale oxygen-on-demand, making it a cornerstone of modern container-glass production facilities aiming for higher efficiency and lower emissions.

cryogenic ASU
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To put the cryogenic ASU in context, it helps to compare it with an alternative oxygen generation method commonly used for smaller-scale needs: Pressure Swing Adsorption (PSA). PSA plants (including vacuum swing adsorption, VPSA) produce oxygen by passing air over special adsorbent materials that capture nitrogen, concentrating oxygen up to about 90–95% purity. They operate at ambient temperature (non-cryogenic) and are more compact but have capacity and purity limitations. The table below provides a technical comparison of a cryogenic ASU versus a PSA oxygen generator, highlighting key parameters relevant to container-glass production:

ParameterCryogenic ASU (On-site Oxygen Plant)PSA Oxygen Generator
Oxygen Purity95–99.5% (high purity, selectable)~90–95% (lower purity)
Typical O₂ Capacity RangeLarge – from ~1,000 up to 20,000+ Nm³/hModerate – tens to a few hundred Nm³/h per unit
Oxygen Delivery ModeContinuous gas output; can also produce liquid backupContinuous but in cycles; gas only (needs buffer tank)
Specific Energy Consumption~0.4–0.6 kWh per Nm³ O₂ (at high purity)~0.2–0.4 kWh per Nm³ O₂ (more energy efficient at lower purity)
Nitrogen ByproductYes – high-purity N₂ available (use or sale)No usable byproduct (waste N₂ vented)
Footprint & EquipmentLarger installation (tall distillation columns, compressors, cooling systems)Compact, skid-mounted modules (compressor and adsorption vessels)
Optimal Use CaseHigh-volume oxygen needs (large furnaces, full oxy-fuel combustion)Low-to-medium demand (small furnaces or oxygen enrichment)

Table 1: Comparison of cryogenic ASU and PSA oxygen generation for container-glass plants.

cryogenic ASU

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