Gas Hazards in Furnaces
Industrial furnaces produce, consume, and leak a range of hazardous gases. Understanding each gas’s source, hazard type, and exposure limits is the foundation of any monitoring strategy.
| Gas | Formula | Source Process | Hazard Type | WEL TWA (ppm) | WEL STEL (ppm) | LEL (%) | UEL (%) | IDLH (ppm) |
|---|---|---|---|---|---|---|---|---|
| Carbon monoxide | CO | Endothermic gas, carburizing, incomplete combustion | Toxic + Flammable | 20 | 100 | 12.5 | 74 | 1,200 |
| Carbon dioxide | CO2 | Combustion products, exothermic gas | Asphyxiant (simple) | 5,000 | 15,000 | — | — | 40,000 |
| Hydrogen | H2 | Endothermic/exothermic gas, dissociated ammonia, bright annealing | Flammable (explosive) | — | — | 4.0 | 75 | — |
| Nitrogen | N2 | Protective atmospheres, purging, vacuum backfill | Asphyxiant (simple) | — | — | — | — | — |
| Ammonia | NH3 | Nitriding, carbonitriding, dissociated ammonia | Toxic + Corrosive | 25 | 35 | 15 | 28 | 300 |
| Hydrogen cyanide | HCN | Carbonitriding (NH3 + CO at temp), cyanide salt baths | Toxic (highly lethal) | 0.9 | 4.5 | 5.6 | 40 | 50 |
| Methane | CH4 | Natural gas supply, enrichment gas, endothermic generator | Flammable + Asphyxiant | — | — | 5.0 | 15 | — |
| Propane | C3H8 | Fuel gas, endothermic generator feed, enrichment | Flammable + Asphyxiant | — | — | 2.1 | 9.5 | — |
| Hydrogen sulphide | H2S | Sulphur-bearing steels at temp, quench oil decomposition | Toxic + Flammable | 5 | 10 | 4.3 | 46 | 100 |
| Methanol | CH3OH | Nitrogen/methanol atmosphere systems | Toxic + Flammable | 200 | 250 | 6.0 | 36 | 6,000 |
| Quench oil mist | CxHy (mixed) | Oil quench baths, sealed quench furnaces | Flammable + Irritant | 5 mg/m³ | 10 mg/m³ | ~1.0 | ~6.0 | — |
| Argon | Ar | Vacuum furnace backfill, inert atmosphere | Asphyxiant (simple) | — | — | — | — | — |
| Helium | He | High-pressure gas quench (vacuum furnaces) | Asphyxiant (simple) | — | — | — | — | — |
Workplace Exposure Limits (EH40)
UK Workplace Exposure Limits are set in HSE document EH40/2005 (4th edition, 2020). These are legally binding under COSHH Regulations 2002.
TWA vs STEL
| Measure | Meaning | Period |
|---|---|---|
| TWA | Time-Weighted Average – maximum average concentration over a normal 8-hour working day and 40-hour week | 8 hours |
| STEL | Short-Term Exposure Limit – maximum 15-minute average; not to exceed 4 times per shift with at least 60 min between | 15 minutes |
Monitoring Requirements
- Personal sampling: Badge or pump-mounted sampler worn in the breathing zone of the worker. Required where exposure is likely to exceed the WEL.
- Area monitoring: Fixed or portable instruments measuring ambient concentrations. Useful for leak detection and alarm triggering but does NOT replace personal monitoring for COSHH compliance.
- Frequency: COSHH Reg 10 – at intervals not exceeding 12 months, or when there is a change to process/controls.
EH40 Table – Furnace-Relevant Gases
| Substance | CAS No. | TWA (ppm) | TWA (mg/m³) | STEL (ppm) | STEL (mg/m³) | Notes |
|---|---|---|---|---|---|---|
| Carbon monoxide | 630-08-0 | 20 | 23 | 100 | 117 | Toxic. Reduces O2 carrying capacity of blood |
| Carbon dioxide | 124-38-9 | 5,000 | 9,150 | 15,000 | 27,400 | Simple asphyxiant at high conc. |
| Ammonia | 7664-41-7 | 25 | 18 | 35 | 25 | Corrosive to eyes/respiratory tract |
| Hydrogen cyanide | 74-90-8 | 0.9 | 1 | 4.5 | 5 | Skin notation – absorbed through skin |
| Hydrogen sulphide | 7783-06-4 | 5 | 7 | 10 | 14 | Olfactory fatigue above 100 ppm |
| Methanol | 67-56-1 | 200 | 266 | 250 | 333 | Skin notation |
| Oil mist (mineral) | — | 5 mg/m³ | 5 | 10 mg/m³ | 10 | Inhalable fraction. Includes quench oil |
| Formaldehyde | 50-00-0 | 2 | 2.5 | 2 | 2.5 | Carcinogen Cat 1B. Can form from oil decomposition |
| Nitrogen dioxide | 10102-44-0 | 0.5 | 0.96 | 1 | 1.91 | Burner combustion product |
Portable Gas Detectors
Portable detectors are essential for personal protection, confined space entry, and spot-checking around furnace equipment. The “standard 4-gas” configuration (O2/LEL/CO/H2S) covers most scenarios, but furnace environments often require additional channels.
Detector Categories
Single-Gas
Dedicated to one gas. Compact, low cost. Common for CO personal alarm or O2 monitor in nitrogen-purged areas. Typical cost £80–250.
4-Gas (Standard)
O2, LEL (catalytic bead), CO, H2S. The industry workhorse for general entry and personal monitoring. Typical cost £400–900.
5/6-Gas & PID
Adds channels for NH3, CO2, or PID (photoionisation for VOCs/oil mist). Needed for nitriding bays, quench areas, or carbonitriding lines. Cost £1,200–3,500.
Portable Detector Comparison
| Model | Manufacturer | Gases | Sensor Life | Battery | IP Rating | Weight | Pump/Diffusion | Approx. Price |
|---|---|---|---|---|---|---|---|---|
| MicroClip XL | BW (Honeywell) | 4-gas: O2/LEL/CO/H2S | 2 yrs (CO/H2S), 3 yrs (O2) | 18 hr Li-ion | IP66/IP67 | 198 g | Diffusion | £450–550 |
| X-am 2500 | Dräger | 4-gas: O2/LEL/CO/H2S | 2 yrs (EC), 3+ yrs (cat bead) | 12 hr alkaline or rechargeable | IP67 | 220 g | Diffusion (pump option) | £500–650 |
| X-am 5600 | Dräger | 6-gas: O2/LEL/CO/H2S + 2 (e.g. NH3, CO2) | 2 yrs (EC), IR sensor 5+ yrs | 20 hr Li-ion | IP67 | 350 g | Diffusion or pump | £1,800–2,500 |
| Altair 4XR | MSA | 4-gas: O2/LEL/CO/H2S | 2 yrs (XCell sensors) | 24 hr Li-polymer | IP68 | 213 g | Diffusion | £550–700 |
| Altair 5X | MSA | 5-gas: O2/LEL/CO/H2S + PID or IR | 2 yrs (EC), 5 yrs (IR) | 17 hr Li-ion | IP67 | 397 g (diffusion), 539 g (pump) | Diffusion or integral pump | £2,200–2,800 |
| BW Ultra | Honeywell | 5-gas: O2/LEL/CO/H2S + PID | 2 yrs (EC), 3 yrs (PID lamp) | 24 hr Li-ion | IP66/IP68 | 348 g | Integral pump | £2,500–3,200 |
| T4 | Crowcon | 4-gas: O2/LEL/CO/H2S | 2 yrs (EC), 3 yrs (cat bead) | 18 hr rechargeable | IP65 | 182 g | Diffusion | £400–500 |
Fixed Gas Detection Systems
Fixed systems provide continuous, 24/7 monitoring of furnace areas. They connect to building alarm systems, ventilation controls, and emergency shutdowns. System design must consider gas density, ventilation patterns, and SIL requirements.
System Components
Detection Side
- Sensor heads / transmitters: Field-mounted devices that detect gas and transmit a signal. May be point detectors (measure at one location) or open-path (IR beam across a zone).
- Controllers / panels: Receive signals from sensor heads, display readings, manage alarm logic. Typically 4–32 channel units in a control room or locally on a furnace panel.
- Communications: 4–20 mA analogue loop (most common, one pair per sensor), HART digital overlay, Modbus RTU/TCP for integration with SCADA/BMS systems.
Response Side
- Local alarms: Beacon + sounder at the detection point. Audible ≥85 dB(A) at 1 m.
- Relay outputs: Volt-free contacts to start extraction fans, close gas supply valves, trip furnace power.
- Integration: 4–20 mA / Modbus to BMS, SCADA, or fire alarm panel.
- SIL rating: Safety Integrity Level per IEC 61508/61511. SIL 1 typical for alarm-only; SIL 2 for automatic gas isolation; SIL 3 for high-hazard zones (rare in standard furnace rooms).
Point vs Open-Path Detection
Point Detectors
Measure gas at one specific location. Best for localised leak detection near valves, seals, furnace doors. Typical detection range: 0–100% LEL or 0–toxic range. Response time: 10–30 seconds (T90).
Open-Path (Line-of-Sight)
IR beam between transmitter and receiver covering 5–200 m path. Measures gas in ppm·m (concentration × path length). Best for perimeter monitoring of large areas. Not suitable for pinpointing leak location.
Fixed System Manufacturer Comparison
| Manufacturer | Key Products | Sensor Types | Comms | SIL Rating | Strengths |
|---|---|---|---|---|---|
| Honeywell Analytics | Searchline Excel (open-path), Sensepoint XCL (point), Touchpoint Plus (controller) | EC, Cat bead, IR, Open-path IR | 4–20 mA, HART, Modbus | SIL 2 (Sensepoint XCL) | Wide range, global support, SIL-certified sensors |
| MSA Safety | Ultima X5000 (point), Ultima XIR (IR point), Ultima OPIR-5 (open-path), SUPREMATouch (controller) | EC, Cat bead, Dual IR (Xtinguish), NDIR | 4–20 mA, HART, Modbus TCP | SIL 2 (Ultima X5000) | XCell sensor platform, fast T90, poison-resistant cat bead option |
| Dräger | Polytron 8000 (point), Polytron 7000 (LEL), PIR 7000 (IR), REGARD 3900 (controller) | EC, Cat bead, IR, Dual IR | 4–20 mA, HART, Modbus, FOUNDATION Fieldbus | SIL 2 (Polytron 8000) | Premium quality, excellent EC sensors, Fieldbus support |
| Crowcon | Xgard IQ (point, smart), Xgard Bright (fixed point), IRmax (open-path), Gasmaster (controller) | EC, Cat bead, IR, Open-path IR, PID | 4–20 mA, HART, Modbus, RS-485 | SIL 2 (Xgard IQ) | UK-based, good support, cost-effective for multi-point |
| Det-Tronics | GT3000 (toxic point), FlexSight LS2000 (open-path), Eagle Quantum Premier (controller) | EC, MOS, IR, UV/IR flame | 4–20 mA, HART, Modbus, FOUNDATION Fieldbus | SIL 2 (GT3000), SIL 3 (EQP controller) | Oil & gas heritage, robust controllers, SIL 3 capable |
Sensor Technologies
Understanding sensor operating principles is critical for specifying the right detection for each furnace environment. No single sensor type covers all gases.
Electrochemical (EC) Sensors
How it works
Target gas diffuses through a membrane and reacts at a sensing electrode, generating a small current proportional to gas concentration. A reference electrode provides a stable potential.
Target gases
CO, H2S, NH3, O2, HCN, NO2, Cl2
Key characteristics
- Typical life: 2–3 years (O2 cells 1–2 years)
- T90 response: 15–30 seconds
- Temperature range: −20°C to +50°C
- Cross-sensitivity: CO sensors respond to H2 (10–25%)
- Humidity affects accuracy below 15% RH
- Low power consumption – ideal for portable instruments
Catalytic Bead / Pellistor (LEL)
How it works
Two matched platinum coils (active + reference) in a Wheatstone bridge. Flammable gas oxidises on the active bead, raising its temperature and resistance. The bridge imbalance is proportional to gas concentration.
Target gases
All flammable gases measured as %LEL. Typically calibrated on methane or propane.
Key characteristics
- Typical life: 3–5 years
- T90 response: 10–20 seconds
- Requires oxygen to function (min ~10% O2)
- Poisoning risk: Silicones, lead, sulphur compounds permanently damage the catalyst
- Cannot detect gas above UEL (output drops to zero)
- Needs regular bump testing to verify catalyst integrity
Infrared / NDIR Sensors
How it works
Gas absorbs infrared light at specific wavelengths. A dual-beam design compares absorption at the target wavelength with a reference wavelength, making it immune to contamination and drift. Non-contact – no chemical reaction.
Target gases
CO2, CH4, C3H8, other hydrocarbons. Cannot detect H2 or CO (no IR absorption).
Key characteristics
- Typical life: 5–10+ years (no consumable elements)
- T90 response: 5–15 seconds
- Not poisoned by silicones or other contaminants
- Works in inert (zero O2) atmospheres
- Fail-safe – reports fault if beam blocked
- Higher cost than catalytic bead
Photoionisation Detector (PID)
How it works
UV lamp ionises gas molecules; ions are collected at an electrode. Current is proportional to gas concentration. Different lamp energies (9.8, 10.6, 11.7 eV) detect different compounds.
Target gases
VOCs, benzene, toluene, quench oil vapour, solvents. Broad-spectrum – does not identify specific compounds.
Key characteristics
- UV lamp life: 2,000–6,000 hours depending on type
- Very fast response: <5 seconds
- Sensitive: sub-ppm detection
- Affected by humidity (water vapour absorbs UV)
- Cannot detect methane, CO, CO2 (ionisation energy too high)
Other Sensor Types
Paramagnetic (O2)
Exploits the paramagnetic properties of oxygen. Two nitrogen-filled glass spheres in a magnetic field; O2 displaces them proportionally. Very accurate (±0.1% O2), long life, no consumables. Used in process analysers and high-accuracy fixed systems.
Thermal Conductivity (TC)
Measures the thermal conductivity of a gas mixture relative to a reference. Used for H2 and He detection (both have TC ~6× air). Limited selectivity – responds to any gas with different TC. Best for binary mixtures (e.g. H2 in N2).
Metal Oxide Semiconductor (MOS)
Heated tin-oxide film changes resistance when gas adsorbs. Very sensitive but poor selectivity. Useful for general flammable gas “sniffer” applications. Low cost, long life, but high cross-sensitivity.
Cross-Sensitivity Reference
Sensors designed for one gas may also respond to others. This table shows typical cross-sensitivity as a percentage of reading for common furnace gases.
| Sensor Target | CO (cross) | H2 (cross) | H2S (cross) | NH3 (cross) | NO2 (cross) | CH4 (cross) |
|---|---|---|---|---|---|---|
| CO sensor (EC) | 100% | 10–25% | <2% | <1% | −5% | <1% |
| H2S sensor (EC) | <5% | <3% | 100% | <1% | 15–30% | <1% |
| NH3 sensor (EC) | <3% | <5% | −10% | 100% | −20% | <1% |
| O2 sensor (EC) | <0.1% | <0.1% | <0.1% | <0.1% | <0.1% | <0.1% |
| LEL sensor (Cat bead) | ~50% | ~50% | Poison | ~30% | Nil | 100% |
| CO2 sensor (NDIR) | Nil | Nil | Nil | Nil | Nil | <2% |
Calibration & Maintenance
Gas detectors are life-safety devices. Without regular calibration and bump testing, they cannot be relied upon. UK HSE guidance and manufacturer requirements are clear: untested detectors are worse than no detectors (false confidence).
Bump Test vs Full Calibration
Bump Test (Functional Check)
- Frequency: Before each use / start of shift (daily minimum)
- Purpose: Confirms sensors respond to target gas and alarms trigger
- Method: Brief exposure (30–60 seconds) to calibration gas at known concentration above alarm setpoint
- Pass criteria: Sensor reads within ±20% of applied concentration AND alarm activates
- Duration: ~60 seconds per instrument
- Does NOT adjust: No changes to calibration factors
Full Calibration (Span Adjustment)
- Frequency: Every 6 months (manufacturer recommendation), or when bump test fails, or after sensor replacement
- Purpose: Adjusts sensor response to match a known reference gas concentration
- Method:
- Zero cal: Expose to clean air or zero gas (N2) – set baseline
- Span cal: Apply calibration gas at target concentration – adjust reading to match
- Duration: 5–15 minutes per sensor channel
- Records: Date, gas batch, before/after readings, engineer signature
Calibration Gas Cylinder Specifications
Standard calibration gas mixture for 4-gas detectors in furnace environments:
| Component | Concentration | Purpose | Cylinder Type | Typical Shelf Life |
|---|---|---|---|---|
| Carbon monoxide (CO) | 100 ppm | Span calibration of CO sensor (alarm at 20/100 ppm) | Disposable 34L or refillable 58L | 12–24 months |
| Hydrogen sulphide (H2S) | 25 ppm | Span calibration of H2S sensor (alarm at 5/10 ppm) | Disposable 34L or refillable 58L | 12 months (reactive gas) |
| Methane (CH4) | 2.5% vol (50% LEL) | Span calibration of LEL sensor | Disposable 34L or refillable 58L | 24–36 months |
| Oxygen (O2) | 18% vol | Span check of O2 sensor (alarm at 19.5%) | Included in 4-gas mix | 24–36 months |
| Balance gas | Nitrogen (N2) | Inert carrier gas | — | — |
- NH3: 50 ppm in N2 (for nitriding bay detectors)
- CO2: 5,000 ppm in N2 (for IR CO2 sensors)
- H2: 2% vol in N2 (50% LEL for H2-specific sensors)
- Isobutylene: 100 ppm in air (standard PID calibrant – use correction factors for other VOCs)
Record Keeping Requirements
- Instrument serial number and location
- Date and type of test (bump / full calibration)
- Gas cylinder batch number and expiry date
- Before-calibration readings (as-found) and after-calibration readings (as-left)
- Name and signature of competent person
- Any corrective actions (sensor replacement, instrument swap-out)
Furnace Monitoring Setups
Each furnace type presents different gas hazards depending on the atmosphere, temperature, and process. These recommended configurations are based on practical experience and HSE/IGEM guidance.
Sealed Quench Furnace (Endo Atmosphere)
Atmosphere: 20% CO, 40% H2, 40% N2 (typical endothermic)
| Sensor | Location | Alarm 1 | Alarm 2 | Notes |
|---|---|---|---|---|
| CO (EC, H2-compensated) | 1.5 m height, within 2 m of furnace front door | 20 ppm | 100 ppm | CO is slightly lighter than air (SG 0.97) but released warm, so rises initially |
| LEL (catalytic bead or IR) | 1.5 m height, near quench vestibule door | 20% LEL | 40% LEL | Detects general flammable gas leak (mixed CO/H2/CH4) |
| H2 (TC or EC) | Ceiling level (H2 SG 0.07 – rises rapidly) | 1% vol | 2% vol | Critical: H2 accumulates at ceiling and is not detected by IR sensors |
| O2 | Breathing zone (1.5 m) | <19.5% | <18% | Atmosphere gas displaces oxygen; required for confined space assessment |
Relay actions: Alarm 1 → audible/visual warning + increase ventilation. Alarm 2 → evacuate area, isolate furnace gas supply, emergency ventilation max speed.
Vacuum Furnace Room (Ar/N2 Backfill)
Hazard: Oxygen depletion from argon or nitrogen release
| Sensor | Location | Alarm 1 | Alarm 2 | Notes |
|---|---|---|---|---|
| O2 (EC or paramagnetic) | 300 mm above floor level (Ar SG 1.38, N2 SG 0.97) | <19.5% | <18% | Argon is denser than air and pools at floor; N2 disperses more evenly |
| O2 (second unit) | Breathing zone 1.5 m, near furnace loading area | <19.5% | <18% | Redundant sensor at worker height |
Special considerations: Vacuum furnace rooms with bulk Ar storage can experience rapid O2 depletion if a large-bore valve or pipe fails. Calculate worst-case leak rate and ensure ventilation capacity exceeds it. BCGA CP30 provides guidance.
Nitriding Bay (NH3 Atmosphere)
Atmosphere: Undissociated NH3 or NH3/N2/H2 mix
| Sensor | Location | Alarm 1 | Alarm 2 | Notes |
|---|---|---|---|---|
| NH3 (EC) | 1.5 m height, within 3 m of furnace | 25 ppm (TWA) | 35 ppm (STEL) | NH3 is lighter than air (SG 0.59), pungent odour detectable at ~5 ppm |
| NH3 (second sensor) | Near exhaust/vent point | 25 ppm | 35 ppm | Monitors exhaust system effectiveness |
| H2 (TC or EC) | Ceiling level | 1% vol | 2% vol | Dissociated ammonia is 75% H2 – significant explosion risk |
| LEL (IR preferred) | 1.5 m, near furnace front | 20% LEL | 40% LEL | Use IR to avoid NH3 poisoning of catalytic bead |
Relay actions: Alarm 1 → warning + check exhaust fans. Alarm 2 → evacuate, isolate NH3 supply, max ventilation. NH3 is corrosive to eyes at >50 ppm.
Carburizing Furnace (CO-Rich)
Atmosphere: 20–25% CO (endothermic + enrichment)
| Sensor | Location | Alarm 1 | Alarm 2 | Notes |
|---|---|---|---|---|
| CO (EC, H2-compensated) | 1.5 m, at furnace front and rear | 20 ppm | 100 ppm | Minimum 2 sensors per furnace – front and rear doors |
| CO (additional) | Operator rest area / control desk | 20 ppm | 50 ppm | Lower Alarm 2 for occupied areas where response time is critical |
| LEL | Near flame curtain / door seal | 20% LEL | 40% LEL | Flame curtain failure allows atmosphere gas escape |
Hydrogen Furnace (Bright Annealing)
Atmosphere: 75–100% H2
| Sensor | Location | Alarm 1 | Alarm 2 | Notes |
|---|---|---|---|---|
| H2 (TC sensor) | Ceiling – directly above furnace entry/exit | 0.5% vol (12.5% LEL) | 1.6% vol (40% LEL) | H2 is extremely buoyant (SG 0.07) – ceiling mounting essential |
| H2 (second TC) | Ceiling – at highest point in room | 0.5% vol | 1.6% vol | H2 migrates to highest point; check for roof voids/dead spots |
| LEL (IR) | 1.5 m near furnace entry/exit | 20% LEL | 40% LEL | IR cannot detect H2 directly but catches hydrocarbon leaks |
| O2 | 1.5 m breathing zone | <19.5% | <18% | H2 furnace purge can displace O2 |
Quench Oil Area
Hazard: Oil vapour, mist, and decomposition products
| Sensor | Location | Alarm 1 | Alarm 2 | Notes |
|---|---|---|---|---|
| LEL (IR preferred) | Above quench tank, 300–500 mm from rim | 10% LEL | 25% LEL | Lower setpoints than standard – oil flash fires escalate rapidly |
| PID (VOC) | 1.5 m breathing zone, downwind of tank | 5 ppm (as isobutylene) | 25 ppm | Detects oil vapour/decomposition products. Apply correction factor for quench oil (~0.8) |
| CO | Near quench tank cover seal | 20 ppm | 100 ppm | Endothermic atmosphere escapes when charge is transferred to quench |
Additional controls: Local exhaust ventilation (LEV) over quench tank is mandatory. Oil temperature monitoring with high-temp alarm (typically 80°C for fast quench oils, 120°C for marquench). Water contamination of quench oil causes explosive foaming – moisture sensors in oil circuit recommended.
Alarm Levels & Response Procedures
Gas detection alarm setpoints must be set below dangerous concentrations with sufficient margin for response time. Two-stage alarms are standard: Alarm 1 (warning) and Alarm 2 (action/evacuate).
| Gas | Alarm 1 (Warning) | Alarm 2 (Action) | Dangerous Level | Alarm 1 Response | Alarm 2 Response |
|---|---|---|---|---|---|
| Oxygen (O2) | <19.5% or >23.5% | <18% or >25% | <16% impairment, <6% fatal | Investigate source of O2 depletion/enrichment. Check ventilation. Increase air flow. | Evacuate immediately. Do not re-enter without SCBA. Isolate inert gas supplies. Emergency ventilation. |
| LEL (flammable gas) | 20% LEL | 40% LEL | 100% LEL = lower explosive limit | Warning alarm. Investigate leak source. Increase ventilation. Remove ignition sources. | Evacuate area. Isolate gas supply. Do not operate electrical switches. Emergency services if uncontrolled. |
| Carbon monoxide (CO) | 20 ppm | 100 ppm | IDLH 1,200 ppm | Investigate source (furnace seal, flame curtain, exhaust). Increase ventilation. | Evacuate to fresh air. Isolate furnace atmosphere. Anyone with symptoms to medical attention (CO blood test). Do not re-enter without portable CO monitor. |
| Hydrogen sulphide (H2S) | 5 ppm | 10 ppm | IDLH 100 ppm. >100 ppm olfactory paralysis | Investigate source. Check quench oil system. Increase ventilation. | Evacuate immediately. H2S causes rapid incapacitation at high concentrations. SCBA for re-entry. |
| Ammonia (NH3) | 25 ppm | 35 ppm | IDLH 300 ppm. Corrosive to eyes/lungs | Check nitriding furnace seals and exhaust. PPE (ammonia respirator cartridge, goggles). | Evacuate. Isolate NH3 supply. Water spray to knock down ammonia cloud (NH3 is water-soluble). Medical attention for eye/respiratory exposure. |
| Hydrogen (H2) | 0.5% vol (12.5% LEL) | 1.6% vol (40% LEL) | LEL 4% vol. Wide flammable range 4–75% | Investigate leak. Check furnace seals, gas supply connections. Increase ventilation at ceiling level. | Evacuate. Eliminate all ignition sources (static, electrical). Isolate H2 supply. Ventilate at ceiling level. H2 flames are invisible – approach with caution. |
- Never assume a single gas – where one gas leaks, others may be present
- Buddy system for all emergency response – never enter a gas alarm zone alone
- SCBA (self-contained breathing apparatus) for any atmosphere with O2 <19.5% or unknown composition
- Gas-free certificate required before any maintenance work in areas that have been under alarm
- Treat all CO exposures as medical emergencies – symptoms may be delayed
LEL / UEL Reference
The Lower Explosive Limit (LEL) is the minimum concentration of a gas in air that can sustain a flame. The Upper Explosive Limit (UEL) is the maximum. Between LEL and UEL, the mixture is explosive if an ignition source is present.
Key Concepts
- Below LEL: Too lean to burn – insufficient fuel
- LEL to UEL: Flammable/explosive range
- Above UEL: Too rich to burn – insufficient oxygen
- Stoichiometric: Ideal combustion ratio (maximum explosion pressure)
- Gas detectors read 0–100% LEL (not 0–100% gas volume)
- 20% LEL alarm = 20% of the way to the explosive limit
Factors Affecting LEL/UEL
- Temperature: LEL decreases ~0.5% per 100°C rise (wider flammable range)
- Pressure: LEL relatively unaffected; UEL increases with pressure
- Oxygen enrichment: LEL decreases, UEL increases dramatically
- Inert dilution: Both LEL and UEL converge (narrower range)
- Mixtures: Use Le Chatelier’s mixing rule for multi-gas LEL calculation
Complete LEL/UEL Table – Furnace-Relevant Gases
| Gas | Formula | LEL (% vol) | UEL (% vol) | Flammable Range | Auto-Ignition Temp (°C) | Min. Ignition Energy (mJ) | Flame Speed (m/s) | Vapour Density (Air=1) |
|---|---|---|---|---|---|---|---|---|
| Methane | CH4 | 5.0 | 15.0 | 10.0% | 537 | 0.28 | 0.40 | 0.55 |
| Propane | C3H8 | 2.1 | 9.5 | 7.4% | 450 | 0.25 | 0.46 | 1.52 |
| Hydrogen | H2 | 4.0 | 75.0 | 71.0% | 500 | 0.017 | 3.46 | 0.07 |
| Carbon monoxide | CO | 12.5 | 74.0 | 61.5% | 609 | 0.30 | 0.47 | 0.97 |
| Ammonia | NH3 | 15.0 | 28.0 | 13.0% | 651 | 680 | 0.15 | 0.59 |
| Methanol | CH3OH | 6.0 | 36.0 | 30.0% | 464 | 0.14 | 0.52 | 1.11 |
| Acetylene | C2H2 | 2.5 | 100.0 | 97.5% | 305 | 0.017 | 1.53 | 0.90 |
| Hydrogen sulphide | H2S | 4.3 | 46.0 | 41.7% | 260 | 0.077 | 0.45 | 1.19 |
| Ethylene | C2H4 | 2.7 | 36.0 | 33.3% | 490 | 0.07 | 0.80 | 0.97 |
| Butane | C4H10 | 1.8 | 8.4 | 6.6% | 405 | 0.25 | 0.45 | 2.01 |
| Hydrogen cyanide | HCN | 5.6 | 40.0 | 34.4% | 538 | — | 0.52 | 0.93 |
LELmix = 100 / (C1/LEL1 + C2/LEL2 + ... + Cn/LELn)
Where Cn is the percentage of each component in the fuel mixture (fuel only, excluding air). Example: Endothermic gas (20% CO + 40% H2 + 1% CH4, rest is N2/CO2). Fuel fraction: CO 33%, H2 66%, CH4 1.6%. LELmix = 100 / (33/12.5 + 66/4 + 1.6/5) = 100 / (2.64 + 16.5 + 0.32) = 5.1% vol in air.