Explosion-proof Cryogenic Nitrogen Plant

Explosion-proof Cryogenic Nitrogen Plant

Explosion-proof cryogenic nitrogen plant is purpose-built for these conditions. It is not a standard unit with add-on Ex components, but rather a system designed from the ground up—covering compressors, cold box sealing, instrument loops, and electrical logic—in full compliance with ATEX or IECEx standards. The goal: to deliver stable high-purity nitrogen while containing ignition sources and preventing any external flammable atmosphere from being ignited.
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Product Introduction

In petrochemical processing, underground coal mining, tanker inerting, and fine chemical operations where flammable gases, vapors, or combustible dusts are present, nitrogen serves as both a protective gas and a process purge medium. When nitrogen generation equipment must be placed in Zone 1, Zone 2, or Class I Division 2 hazardous locations, the plant's explosion-proof design and operational integrity become direct factors in process safety.

An explosion-proof cryogenic nitrogen plant is engineered specifically for such service conditions. This equipment is not a standard cryogenic unit with explosion-proof components retrofitted afterward; rather, it follows a forward-design approach that complies with ATEX or IECEx certification frameworks across all subsystems-compressor selection, cold box sealing, instrument signal routing, and electrical control logic. The objective is to enable stable high-purity nitrogen output while containing any potential ignition sources, thereby preventing the equipment from triggering an incident in the presence of combustible atmospheres.

 

Process Principle

The plant uses standard cryogenic air separation, adapted for hazardous areas.Ambient air is filtered, compressed in a multistage centrifugal compressor, then cooled to 5–10°C in a precooler to knock out free water. A pair of switching molecular sieve beds removes residual CO₂, moisture, and hydrocarbons-critical in Ex applications since CO₂ would freeze in the main exchanger and hydrocarbons can accumulate in the column's oxygen-rich zone.The clean air enters the main heat exchanger, cools to near liquefaction (about -170°C) against returning waste and product nitrogen, then feeds into the rectifying column. Oxygen and nitrogen separate by boiling point (-183°C vs -196°C). Nitrogen is taken off the top; oxygen-enriched bottoms are throttled to the upper column for further separation.

Ex protection is built into key points: motors are Ex d flameproof or Ex e increased-safety; instruments are Ex ia intrinsically safe with isolators; the cold box runs under slight positive dry nitrogen with O₂ monitoring; and DCS includes emergency vent and fast-isolation trips. These measures keep an explosion-proof cryogenic nitrogen plant from acting as an ignition source under leak or upset conditions.

 

Performance Specifications (Typical Range)

The table below presents representative capacity intervals. For specific projects, flow rate, purity, and power consumption can be tailored to match the site's hazardous area classification and ambient conditions.

Nitrogen PurityCapacity Range (Nm³/h)Discharge Pressure (MPaG)Dew Point (°C)Specific Power (kWh/Nm³)
99.9%100 – 6,0000.05 – 0.8≤ -600.28 – 0.45
99.99%80 – 3,0000.05 – 0.6≤ -700.32 – 0.52
99.999%50 – 1,5000.05 – 0.4≤ -760.38 – 0.60

Specific power consumption generally decreases with increasing plant capacity. Units above 2,000 Nm³/h are typically equipped with expansion turbine boost braking, allowing optimization to below 0.30 kWh/Nm³. The operating temperature envelope covers ambient conditions from -15°C to 45°C; for extreme cold or hot climates, the heat exchanger cores and valve materials require additional design validation for low-temperature impact toughness and high-temperature creep resistance.

 

Technical Data

ParameterSpecification
Ex MarkingEx d e ib IIB T4 / Ex db eb ib IIC T4 (depending on option)
Hazardous Area SuitabilityZone 1, Zone 2, Class I Div 1 & 2
Start-up Time (cold to full capacity)≤ 8 hours
Turndown Range60% – 110% stepless adjustment
Nitrogen Pressure Stability±0.02 MPa
Cooling Water DemandPer process design, closed-loop circulation
Molecular Sieve RegenerationWarm waste nitrogen, with Ex d electric heater
Instrument Air SupplyDry oil-free compressed air, 0.5 – 0.7 MPa
Control SystemSiemens S7-1500 series in explosion-proof enclosure; 10-inch Ex touchscreen panel; supports Modbus TCP and Profibus-DP protocols
Safety InterlocksThree-tier protection covering upper column differential pressure high limit, cold box positive-pressure low limit, motor winding overtemperature, bearing vibration excess, with optional combustible gas detection

The cold box incorporates brazed aluminum plate-fin heat exchangers and structured packing columns. Its outer shell is constructed from welded carbon steel, filled with perlite insulation, and fitted with explosion-proof breather valves to maintain atmospheric pressure. All pressure vessels are designed in accordance with GB/T 150 and ASME Section VIII Division 1, and the installation complies with applicable hazardous area electrical design codes.

 

Industrial Applications

These units are suited for the following service conditions:

  • Petroleum Refining and Petrochemicals: Purging, displacement, and blanketing for hydrocracking, catalytic reforming, and sulfur recovery units-particularly in retrofitting projects where hazardous area zoning is complex.
  • Coal Chemicals and Fine Synthesis: System nitrogen sealing and emergency depressurization for continuous processes such as methanol-to-olefins (MTO), acetic acid synthesis, and BDO production.
  • Oil & Gas Storage and Terminal Loading: Tank blanketing for crude and refined product storage to prevent flammable vapor accumulation; oxygen content control during pipeline purging at loading arms.
  • Pharmaceutical and Electronic-Grade Chemical Production: Production lines with dual sensitivity to cleanliness and safety, where nitrogen serves as a conveying medium and protective atmosphere.
  • Metal Heat Treatment and Powder Metallurgy: Bright annealing, brazing furnaces, and other high-temperature equipment requiring nitrogen as a shielding gas-explosion-proof considerations typically arise from cross-contamination risks due to hydrogen or carbon monoxide leaks in the furnace area.

 

Configuration & Engineering Support

Each explosion-proof cryogenic nitrogen plant is sized based on three inputs: hazardous area class and gas group, required N₂ pressure and purity tolerance, and available utilities (cooling water, instrument air, power or steam).

Adjustable items include:

  • Compressor: centrifugal or screw, motor or steam turbine drive, with auxiliaries placed per zone.
  • Cold box: skid-mounted or field-erected; height can be kept under 4.5 m for indoor fit.
  • Purification: vertical radial-flow molecular sieves; regeneration by electric, steam, or both.
  • Control: load-following, parallel-unit sharing, and auto shutdown/warm-up sequences.

Project support covers zone classification consulting, HAZOP, SIL assessment, Ex equipment selection, site supervision, wiring inspection, commissioning, and operator training. Ex components come with ATEX or IECEx CoC; full systems can be supplied with CE/PED or EAC documentation for EPC projects.

 

Each explosion-proof nitrogen generation unit holds a full-system explosion-proof certification and undergoes a 72-hour loaded test under simulated hazardous atmospheres prior to shipment. From welding procedures to instrument traceability, every step is independently documented, ensuring complete end-to-end traceability.

We welcome your operating parameters-Shenger Gas's technical team can then tailor a solution that balances safety margins with economic viability.

 

 

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