PSA / Membrane N₂

Nitrogen Generation

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Nitrogen Generation: Define the Product Before Comparing Performance

On-site nitrogen generation separates nitrogen from compressed air. Pressure swing adsorption and membrane systems have different operating characteristics. Select and assess a generator against the required flow, pressure, purity, and other product-quality limits.

Manufacturer performance tables must be read at the specified conditions. A maximum flow headline and a maximum purity headline may not describe the same operating point.

References: Atlas Copco — Nitrogen Generation and NGP PSA Generators.

What to Record When Product Quality Changes

Document the analyzer reading and units, product flow, delivery pressure, feed-air condition, alarms, and demand pattern. Record whether the reading represents oxygen concentration or a reported nitrogen-purity value. Do not treat an oxygen-only measurement as proof that every possible impurity meets the process specification.

Have analyzer condition and sampling arrangements checked under the applicable procedure before assuming the separation media has failed. Review the complete feed and product system with qualified personnel.

Worked Example: Electricity per Unit of Nitrogen

Illustrative example: these assumed values demonstrate arithmetic, not actual plant results or recommended operating targets.

Assume the compressor, dryer, and generator auxiliaries together consume an average 45 kW while delivering 150 Nm³/h of nitrogen at the required specification.

Specific electricity consumption = 45 ÷ 150 = 0.30 kWh/Nm³.

At an illustrative tariff of PKR 40/kWh, electricity contributes PKR 12/Nm³. This excludes maintenance, financing, depreciation, backup supply, and other costs. State the normal reference conditions used for Nm³. Use compliant product volume over the same measurement period as the electricity total.

Nitrogen can create an oxygen-deficient atmosphere. Follow the site's ventilation, gas-monitoring, and access procedures; this guide is not a procedure for entering or testing an atmosphere.

Next step: Compare product demand with the generator's performance table at the required specification.

Record observations only where it is safe. Inspection inside equipment, electrical testing, chemical work and changes to protective controls require qualified personnel, approved isolation and the installed equipment manual. Never bypass a trip or repeatedly restart unsafe equipment. Engineering disclaimer

Measurements To Record

  • Product oxygen concentration or verified purity
  • Feed-air pressure and pressure dew point
  • Product pressure and flow at stated reference conditions
  • Cycle and valve alarm history

Maintenance Checklist

  • Log purity, feed pressure and product flow.
  • Maintain filters and dryers to the specified air-quality requirement.
  • Schedule analyser calibration using certified gases and procedures.
  • Inspect ventilation and maintain oxygen-deficiency controls.

Evidence-Based Diagnosis

Product purity below requirement

Possible Causes
Excess product flow; inadequate feed air; faulty analyser; separation-system problem.
Evidence To Collect
Check analyser calibration and sample conditions. Compare flow and feed-air quality with the specified operating envelope.
Qualified Follow-Up
Protect the downstream process using approved off-spec procedures; have the supplier diagnose the separation system.

Low product pressure

Possible Causes
Insufficient feed; leaks; high demand; restricted distribution.
Evidence To Collect
Compare feed, generator outlet and user pressures while recording demand.
Qualified Follow-Up
Investigate supply limitations and leaks, then review buffering and demand with the system designer.

PSA switching alarms

Possible Causes
Valve or actuator problem; control fault; unsuitable feed conditions.
Evidence To Collect
Record the exact alarm and cycle timing; consult the model manual.
Qualified Follow-Up
Use OEM service support for valve and control checks. Do not alter switching logic without approval.

Record The Confirmed Result

Keep the asset model, time, load, ambient conditions, alarm code and relevant readings together. Compare with the last healthy baseline. Record the confirmed cause, approved corrective action and readings after restoration; check that the improvement persists before closing the investigation.

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How It Works

  1. 1

    Clean, dry compressed air enters the CMS bed under pressure.

    Feed air must be clean and dry: oil-free or well-filtered compressed air at 7–8 bar, 1 µm and 0.01 µm coalescing filters, activated carbon, and a dryer giving −40 °C dew point. Oil or water reaching the carbon molecular sieve poisons it permanently — pre-treatment is the whole life of the machine.

  2. 2

    Oxygen and moisture adsorb on the sieve; nitrogen passes through.

    Inside the CMS vessel the sieve's pore size (~3 Å) lets the smaller, faster-diffusing oxygen molecules enter the micropores while nitrogen slips past. Oxygen, CO₂ and residual moisture are adsorbed under pressure; nitrogen leaves the top of the bed at product purity.

  3. 3

    Second bed regenerates by depressurization.

    As the online bed saturates, the second bed is vented to atmosphere. Dropping the pressure releases the adsorbed oxygen (this is the 'swing' in pressure swing adsorption) and regenerates the sieve with no heat and no consumables. A short pressure-equalisation step between beds recovers energy and steadies purity.

  4. 4

    Beds alternate to give continuous N₂ flow into a buffer tank.

    Solenoid or angle-seat valves swap the beds on a fixed cycle (typically 60–120 s) so product flow is continuous. The buffer tank absorbs the switch-over ripple, and an inline O₂ analyser diverts off-spec gas to vent until purity recovers. Higher purity means more air per unit of nitrogen — 95 % N₂ needs ~2.5 Nm³ air/Nm³, 99.999 % needs ~10.

Key Components

Air Pre-treatment
Filters + dryer, remove oil & water

Cyclone separator, 1 µm and 0.01 µm coalescing filters, activated carbon tower and a refrigerated + desiccant dryer chain. Target: <0.003 mg/m³ oil and −40 °C PDP. This is the single most important maintenance item on a PSA plant.

CMS Vessels
Adsorb O₂ under pressure

Twin carbon-molecular-sieve towers, snowstorm-filled and spring-loaded so the bed cannot fluidise and dust. Sieve life is 8–10 years if kept dry and oil-free; a sudden purity fall usually means bed dusting, channelling or contamination.

Switching Valves
Sequence adsorption / regeneration

Fast-acting angle-seat or butterfly valves with pilot solenoids, sequenced by the PLC (adsorb → equalise → vent → repressurise). Millions of cycles per year — seat leakage is the most frequent purity fault, so the annual valve/seal kit is not optional.

N₂ Buffer Tank
Stabilises purity & flow

Receiver downstream of the beds that smooths the cyclic delivery, holds pressure during bed switching, and provides surge capacity for intermittent large users (blanketing, purging, packaging).

O₂ Analyser
Continuous purity monitoring

Zirconia or electrochemical cell reading residual oxygen in ppm or %. Interlocked to a vent valve that dumps off-spec gas before it reaches the plant. Calibrate monthly with span gas; a drifting cell silently sends off-spec nitrogen to process.

Typical Operating Parameters

These reference ranges are illustrative context, not approved operating limits. Verify the installed model, duty, fuel or water conditions and applicable site requirements before use.

Purity
95 – 99.999 %
Pressure
6 – 8 bar(g)
Air Factor
2.5 – 10 (purity dependent)
Dew Point
≤ −40 °C

Safety Notes

  • •Asphyxiation hazard — N₂ displaces O₂ in confined spaces.
  • •Install O₂ monitors in enclosed rooms.
  • •Always vent to safe location.

Maintenance Schedule

  • •Monthly: check O₂ analyser calibration.
  • •6-monthly: inlet coalescing/carbon filters.
  • •Annual: valve cycle test, CMS life check.

Problem Solving Matrix

Listed causes are hypotheses, not confirmed findings. Any corrective work requires qualified assessment, approved procedures and follow-up measurements.

IssueLikely causeFix
Purity dropContaminated CMS / valve leakCheck pre-treatment, cycle valves
Low flowHigh demand / low air pressureVerify compressor & buffer

Equipment Running-Cost Estimate

Use measured electrical input, operating hours and your actual electricity tariff to estimate energy costs for nitrogen generation. Compare replacement options before setting a project budget.

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