Cryogenic Air Separation Plant
Estimated Cryogenic Air Separation Price
Product & Technical Features
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Smart Modular Air Separation
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Fully automatic PLC/DCS control, load regulation 30%~110%, adapting to downstream fluctuation
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Stable Multi-gas Production
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Simultaneous gaseous and liquid product output (LIN, LOX, LAR) with cryogenic liquid storage tanks
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Durable On-site Gas Supply
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Design life ≥20 years, continuous operation cycle ≥2 years, low maintenance cost
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Intelligent Cryogenic Separation
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Modular design, easy installation, small footprint, suitable for on-site centralized gas supply
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Core Advantages
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Low Energy Consumption
Employs an advanced heat exchange network; integrated energy consumption is ≤ 0.48 kWh/Nm³ (for nitrogen), representing an industry-leading standard.
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High Reliability
Features oil-free operation of turbomachinery and automatic regeneration of molecular sieves, enabling continuous operation for ≥ 2 years without shutdown.
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Flexible Load Adjustment
Supports a load regulation range of 30% to 110%, making it particularly well-suited for variable-load operating conditions found in industries such as coal chemicals and steel manufacturing.
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Safety & Environmental Protection
Operates at low temperatures and atmospheric pressure; involves no hazardous chemicals; waste gas can be recovered or discharged in full compliance with environmental standards.
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Intelligent Control
Features DCS-based remote diagnostics and fault pre-warning capabilities, requiring minimal operating personnel and facilitating convenient maintenance.
Product Specifications
| Model | KDON-50/50 | KDON-80/160 | KDON-180/300 | KDON-260/500 | KDON-350/700 | KDON-550/1000 |
|---|---|---|---|---|---|---|
| O₂ Output Nm³/h | 50 | 80 | 180 | 260 | 350 | 550 |
| O₂ Purity %O₂ | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 |
| N₂ Output Nm³/h | 50 | 160 | 300 | 500 | 700 | 1000 |
| N₂ Purity ppm O₂ | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 |
| Unit Energy KWh/Nm³O₂ | ≤1.3 | <0.85 | ≤0.68 | ≤0.65 | ≤0.65 | ≤0.65 |
| Footprint m² | 145 | 150 | 160 | 180 | 250 | 420 |
| Model | KDN-200 | KDN-300 | KDN-400 | KDN-700 | KDN-1000 | KDN-1600 |
|---|---|---|---|---|---|---|
| N₂ Output Nm³/h | 200 | 300 | 400 | 700 | 1000 | 1600 |
| N₂ Purity ppm O₂ | ≤3 | ≤3 | ≤3 | ≤3 | ≤3 | ≤3 |
| LN₂ Output L/h | / | 10 | 10 | 20 | 40 | 60 |
| N₂ Pressure MPa | 0.34~1 | 0.34~1 | 0.34~1 | 0.34~1 | 0.34~1 | 0.34~1 |
| Footprint m² | 95 | 150 | 220 | 260 | 300 | 320 |
| Model | KDO-180y | KDO-250y | KDO-400y | KDON-1200y/300y | KDONAr-1300y/200y/40y |
|---|---|---|---|---|---|
| LO₂ Output Nm³/h | 180 | 400 | 400 | 1200 | 1300 |
| LO₂ Purity % | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 |
| LO₂ Pressure MPa | 0.2 | 0.2 | 0.2 | 0.2 | 0.2 |
| LN₂ Output Nm³/h | — | — | — | 300 | 200 |
| LN₂ Purity PPm O₂ | — | — | — | ≤5 | ≤5 |
| LN₂ Pressure MPa | — | — | — | 0.5 | 0.5 |
| LAr Output Nm³/h | — | — | — | — | 40 |
| LAr Purity | — | — | — | — | ≤1.5ppm O₂+4ppm N₂ |
| LAr Pressure MPa | — | — | — | — | 0.2 |
| Footprint m² | 250 | 300 | 350 | 850 | 4000 |
| Component | Symbol | Volume Fraction % | Weight Fraction % |
|---|---|---|---|
| Nitrogen | N₂ | 78.084 | 75.5 |
| Oxygen | O₂ | 20.95 | 23.1 |
| Argon | Ar | 0.932 | 1.29 |
| Carbon Dioxide | CO₂ | 0.035 | 0.05 |
| Helium | He | 0.00046 | 0.00006 |
| Neon | Ne | 0.0016 | 0.0011 |
| Krypton | Kr | 0.00011 | 0.00032 |
| Xenon | Xe | 0.000008 | 0.00004 |
| Component | Symbol | Boiling Pt. ℃ | Melting Pt. ℃ | Gas Density Kg/m³ | Liquid Density Kg/L | Critical Temp. ℃ | Critical Pressure MPa(G) |
|---|---|---|---|---|---|---|---|
| Nitrogen | N₂ | -195.8 | -209.86 | 1.2506 | 0.81 | -147 | 3.45 |
| Oxygen | O₂ | -183 | -218.4 | 1.4289 | 1.14 | -119 | 5.13 |
| Argon | Ar | -185.7 | -189.2 | 1.784 | 1.4 | -122 | 4.959 |
| Helium | He | -268.9 | -272.55 | 0.18 | 0.125 | -267.7 | 0.2335 |
| Neon | Ne | -246.1 | -248.6 | 0.748 | 1.204 | -228.7 | 2.813 |
| Krypton | Kr | -153.2 | -157.2 | 1.735 | 2.155 | -63.7 | 5.6 |
| Xenon | Xe | -108 | -111.8 | 1.664 | 3.52 | 16.6 | 6.01 |
Working Principle
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① Pre-cooling and Compression: Feed air compressed to 0.5~0.8MPa, pre-cooled to ~5℃ for dewatering.
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② Molecular Sieve Purification: Enters molecular sieve adsorber; 13X sieve adsorbs residual H₂O, CO₂, hydrocarbons.
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③ Main Heat Exchange + Expansion Refrigeration: Purified air cooled to ~-170℃ in main heat exchanger; turbo expander provides refrigeration.
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④ Distillation Separation: Enters distillation column; preliminary separation in lower column, rectification in upper column yields high-purity N₂ and O₂.
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⑤ Product Export: Gaseous products reheated and delivered; part liquefied and stored in cryogenic tanks (LIN -196℃, LOX -183℃).
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Coal Chemical
Large-scale N₂ for coal gasification, ammonia synthesis, methanol production -
Electronics & Semiconductor
Ultra-high purity N₂ (≥99.9999%) for chip manufacturing -
Medical
Medical LOX for hospital O₂ supply; LIN for cryopreservation -
Food & Beverage
LIN freezing, N₂ flushing for freshness -
Metal Heat Treatment
High-purity N₂ for annealing & quenching to prevent oxidation -
Aerospace
LOX as rocket oxidizer







