Bang Intelligent
Cryogenic Air Separation Unit
CRYOGENIC AIR SEPARATION SERIES
Process Principle
The basic principle of air separation is use cryogenic rectification to condense air into liquid and separate the air according to the evaporation temperature of each component.The twostage rectification tower simultaneously obtains pure nitrogen and pure oxygen at the top and bottom of the upper tower. It is also possible to take out liquid oxygen and liquid nitrogen from the evaporation side and the condensation side of the main cooling respectively. The air separation in the rect ification toweris divided into two stages, airis separated forthefirsttime in the lowertower to obtain liquid nitrogen and at the same time obtain oxygen-enriched liquid air. The oxygenenriched liquid air is sent to the upper tower for rectification to obtain pure oxygen and pure nitrogen. The upper tower is divided into two sections: with the liquidair inlet as the boundary,the upper part is the rectification section, which rectifies the rising gas, recovers the oxygen component, and purifies the nitrogen purity, and the lower section is the stripping section to remove the nitrogen components in the iquid, separated to improve the oxygen purity of the iquid.
Process Flow
1. Air compressor (screw type): Uses air as raw material, collects and compresses air to 8 bar
2. Refrigerated dryer: Standard configuration removes moisture and impurities from the air, bringing the air dew point to -20℃ (intermediate configuration uses an adsorption dryer, bringing the dew point to -40℃); Advanced configuration uses a combined dryer (dew point reaches -60℃)
3. Precision filter: A/T/C three-stage filter removes oil, dust, and impurities.
4. Air buffer tank: Stores pure, dry air as raw material for subsequent adsorption and oxygen separation.
5. Adsorption tower: A & B adsorption towers can work alternately, regenerating adsorption and filling with sodium molecular sieves to filter out oxygen molecules.
6. Oxygen analyzer: Monitors and analyzes oxygen purity in real time, indicating normal equipment operation and triggering alarms.
7. Valves & pipelines: Intelligent control valves enable fully automatic equipment operation, PLC control, SUS304 pipelines.
8. Oxygen buffer tank: Stores qualified oxygen, which can be directly piped or bottled for use.
9. Pressure regulator: Adjusts and regulates the oxygen outlet pressure (3-6 Bar).
10. Dust filter: Removes dust from the molecular sieves in the oxygen.
11. Check valve: Preventing Oxygen Backflow
12. Booster: Oxygen booster, pressurizes oxygen to the filling pressure, typically 150 bar or 200 bar
13. Pressure Regulating Valve: Regulates the pressure of the oxygen compressor
14. Filling Drain: Distributes high-pressure oxygen to individual oxygen cylinders
Equipment + Process
1.Air Compressor Suction air
2.Precision Filter Removal dust and oil
3.Air Pre-cooler Reduce the air temperature to 5-8℃
4.Water Separator
5.Air Tank
6.Molecular Sieve Purifier
12.Gas Analyzer
11.Filling Device
10.Liquid Oxygen Pump
9.Turbo-expander
7.Precision Filter
8.Rectification Column(Cold Box)
13.Electrical & instrument control system
14.Oxygen cylinder
BWDN High Purity Nitrogen Air Separation Unit
Technical indicators
| Nitrogen Purity | ≥99.9997% | Raw Material Medium | Air |
|---|---|---|---|
| Phase State | Gas Phase | Temperature State | Normal Temperature |
| Operation Cycle | ≥24 Months | Start Time | ~12 Hours |
Specifications Classification
| Model | \ \ Unit | BWDN -200 | BWDN -300 | BWDN -400 | BWDN -700 | BWDN -1000 | BWDN -1600 | BWDN -3000 |
|---|---|---|---|---|---|---|---|---|
| Nitrogen Production | Nm³/h | 200 | 300 | 400 | 700 | 1000 | 1600 | 3000 |
| Liquid Nitrogen Production | \ \ L/H | / | 10 | 10 | 20 | 40 | 60 | 150 |
| Nitrogen Purity | PPmO₂ | ≤3 | ≤3 | ≤3 | ≤3 | ≤3 | ≤3 | ≤3 |
| Nitrogen Pressure | MPa.A | 0.34~1 | 0.34~1 | 0.34~1 | 0.34~1 | 0.34~1 | 0.34~1 | 0.34~1 |
| Device Occupied Area | m² | 95 | 150 | 220 | 260 | 300 | 320 | 410 |
BWDO Cryogenic Oxygen Air Separation Unit
The cryogenic oxygen production & oxygen&nitrogen production process introduces a low-pressure process into the air separation equipment, which reduces the energy consumption of theair separation and improves the safety of operation, correspondina chemical software is used inprocess calculation and unit equipment design for process distillation calculation and structurecalculation to ensure advanced and reliable equipment.
The cryogenic oxygen production &oxygen&nitrogen production process introduces a low-pressure process into the air separation equipment, which reduces the energy consumption of theair separation and improves the safety of operation. Corresponding chemical software is used inprocess calculation and unit equipment design for process distillation calculation and structurecalculation to ensure advanced and reliable equipment.
The company designed and developed a skid-mounted purification system to minimize on-sitepiping installation time
Technical indicators
| Name | Oxygen Gas | Pressure | 20MpaG(Adjustable) |
|---|---|---|---|
| Purity | ≥99.6% | Operation Cycle | 12 Months |
| Start Time | ~24 Hours | Single Column,Internal compression Process | Single Column,Internal compression Process |
| Name | Oxygen&Nitrogen Gas | Pressure | 20MpaG(Adjustable) |
|---|---|---|---|
| Oxygen Purity | ≥99.6%O₂ | Nitrogen Purity | ≥99.99% |
| Start Pressure | 1.0MPaG | Double column,External compression Process | Double column,External compression Process |
Specifications Classification
| Model | Unit | BWDON -50-50 | BWDON -80/160 | BWDON -180-300 | BWDON -260-500 | BWDON -350-700 | BWDON -550-1000- | BWDON -750-1500 | BWDON 1200-3000-30Y |
|---|---|---|---|---|---|---|---|---|---|
| Oxygen Production | Nm³/h | 50 | 80 | 180 | 260 | 350 | 550 | 750 | 1200 |
| Oxygen purity | %O₂ | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 |
| Nitrogen Production | Nm³/h | 50 | 160 | 300 | 500 | 700 | 1000 | 1500 | 2000 |
| Nitrogen Purity | PPmO₂ | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 | ≤10 | ≤5 |
| Liquid Argon Production | Nm³/h | 一 | 一 | 一 | 一 | 一 | 一 | 一 | 30 |
| Liquid Argon Purity | PpmO₂+ PPmN₂ | 一 | 一 | 一 | 一 | 一 | 一 | 一 | ≤1.5PpmO₂ +4PPmN₂ |
| Liquid Argon Pressure | MPa.A | 一 | 一 | 一 | 一 | 一 | 一 | 一 | 0.2 |
| Unit Consumption | Kwh/ Nm³O₂ | ≤1.3 | ≤0.85 | ≤0.68 | ≤0.68 | ≤0.65 | ≤0.65 | ≤0.63 | ≤0.55 |
| Device Occupied Area | m² | 145 | 150 | 160 | 180 | 250 | 420 | 450 | 800 |
BWDON Ar-Y Cryogenic Liquid Air Separation Unit
Liquid air separation equipment requires more coolingcapacity than gas air separation equipment.
According to the different production of liquid air separationequipment, we adopt a variety of different refrigeration cycleprocesses,turbine expander refrigeration, low temperaturepre-cooling refrigeration, circulating compressor high andlow pressure expander refrigeration, etc.,through variousmethods to achieve reduction Energy consumption goals.The control system adopts DCS or PLC control system, andauxiliary field instruments, so that the whole set ofequipmentis simple to operate, stable and reliable.
Specifications Classification
| Model | \ Unit | BWDO -180y | BWDO -250y | BWDO -400y | BWDON- 1200y/300y | BWDONAR -1300y/200y/40y | BWDONAR -2700y/300y/90y |
|---|---|---|---|---|---|---|---|
| Liquid Oxygen Production | Nm³/h | 180 | 250 | 400 | 1200 | 1300 | 2700 |
| Liquid Oxygen Purity | %O₂ | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 | ≥99.6 |
| Liquid Oxygen Pressure | MPa.A | 0.2 | 0.2 | 0.2 | 0.2 | 0.2 | 0.2 |
| Liquid Nitrogen Production | Nm³/h | 一 | 一 | 一 | 300 | 200 | 300 |
| Liquid Nitrogen Purity | PPmO₂ | 一 | 一 | 一 | ≤5 | ≤5 | ≤5 |
| Liquid Nitrogen Pressure | MPa.A | 一 | 一 | 一 | 0.5 | 0.5 | 0.5 |
| Liquid Argon Production | Nm³/h | 一 | 一 | 一 | 一 | 40 | 90 |
| Liquid Argon Purity | PpmO₂ +PPmN₂ | 一 | 一 | 一 | 一 | ≤1.5PpmO₂ +4PPmN₂ | ≤1.5PpmO₂ +4PPmN₂ |
| Liquid Argon Pressure | MPa.A | 一 | 一 | 一 | 一 | 0.2 | 0.2 |
| Device Occupied Area | \ m² | 250 | 300 | 350 | 850 | -4000 | -4500 |
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