Gas Encyclopedia · Flammable Gas

Coal Gas

Coal gas is a variable fuel mixture produced by coal carbonization, coking or historical town-gas processes. It may contain hydrogen, methane, carbon monoxide, carbon dioxide, nitrogen and sulfur compounds. The coexistence of flammable components and highly toxic carbon monoxide makes single-channel LEL monitoring insufficient for many installations.

Formula: MixtureCAS: MixtureComposition-dependent
Overview

What Is Coal Gas?

Coal gas is a variable fuel mixture produced by coal carbonization, coking or historical town-gas processes. It may contain hydrogen, methane, carbon monoxide, carbon dioxide, nitrogen and sulfur compounds. The coexistence of flammable components and highly toxic carbon monoxide makes single-channel LEL monitoring insufficient for many installations.

Practical definition: Coal Gas should be treated as a release-and-ignition problem, not simply a chemical name. The safety objective determines whether the instrument must measure ppm toxic exposure, percent of lower explosive limit, volume percent, oxygen or process composition.
Formula / typeMixture
CASMixture
Molecular weightComposition-dependent
Gas densityComposition and temperature dependent; may be near or lighter than air

Selected authority references: OSHA — Coke Oven Emissions; NIOSH — Composition of Coalbed Gas; NIOSH Pocket Guide — Carbon Monoxide.

Physical and Chemical Profile

Key Properties and Safety Meaning

Property values describe controlled test conditions. Real releases are influenced by concentration, pressure, temperature, ventilation and surrounding equipment.

PropertyValue or descriptionEngineering significance
Formula or mixtureMixtureDefines whether calibration can use a pure-gas basis or must account for composition.
CAS numberMixtureMixtures may not have one CAS identity.
Molecular weightComposition-dependentUseful for engineering calculations, but not sufficient for detector placement.
Boiling / phase behaviorNot applicable to the mixture as one substanceInfluences vapor generation, cryogenic releases and sample handling.
Relative gas densityComposition and temperature dependent; may be near or lighter than airOne dispersion input among release temperature, pressure, ventilation and geometry.
Appearance and odorUsually colorless; odor depends on sulfur and tar componentsHuman senses cannot provide a quantified or automatic safety response.
FlammabilityComposition-dependentUse the applicable test basis, actual composition and site conditions.
Exposure contextUse component-specific limits. Carbon monoxide and hydrogen sulfide can control worker protection long before a combustible alarm.Toxic, oxygen and combustible measurements serve different purposes.

Gas density alone is not sufficient to determine detector placement. Release point, gas temperature, process pressure, ventilation, air movement, room geometry, obstructions and equipment enclosures must also be considered.

Production and Release Scenarios

Where Coal Gas Comes From

Common sources and release points

  • Coke ovens and by-product plants
  • Coal carbonization and historical gasworks
  • Coke-oven gas holders, mains and compressors
  • Steel mills, reheating furnaces and boiler fuel systems
  • Gas-cleaning, tar-removal and desulfurization equipment
  • Confined spaces connected to old manufactured-gas infrastructure

What changes the release

  • Operating pressure and hole or valve geometry
  • Liquid flashing, evaporation or cryogenic cooling
  • Mechanical ventilation, open doors and weather
  • Startup, shutdown, purging and maintenance
  • Mixture composition and contaminants
  • Obstructions that create pockets or redirect a jet
Industries and Applications

Where It Is Used or Encountered

01

Steel-industry fuel

Potential monitoring points include transfer, storage, process equipment, ventilation paths and occupied access routes.

02

Coke-oven heat recovery

Potential monitoring points include transfer, storage, process equipment, ventilation paths and occupied access routes.

03

Boilers and furnaces

Potential monitoring points include transfer, storage, process equipment, ventilation paths and occupied access routes.

04

Chemical recovery from by-products

Potential monitoring points include transfer, storage, process equipment, ventilation paths and occupied access routes.

05

Historical municipal fuel systems

Potential monitoring points include transfer, storage, process equipment, ventilation paths and occupied access routes.

Health, Fire and Process Hazards

Why Coal Gas Can Be Dangerous

Primary hazards

  • Carbon monoxide may be immediately toxic at concentrations far below the fuel-gas LFL.
  • Hydrogen and methane create a broad flammable mixture whose limits change with composition.
  • H₂S, ammonia, benzene and tar vapors may add toxic, corrosive and fouling hazards.
  • Hot gas and pressure influence dispersion and detector placement.
  • Condensate and tar can block sample lines and poison sensors.

Reactivity and compatibility

  • Control oxygen ingress into gas holders, piping and process vessels.
  • Use materials compatible with condensate, sulfur compounds and tar.
  • Provide drainage and heat tracing without creating ignition hazards.
  • Classify electrical equipment for the credible gas mixture.

Do not use odor as the only warning. Odor thresholds vary, mixtures may be odorized or unodorized, people differ in sensitivity and a smell provides no quantified concentration or automatic shutdown.

LEL, UEL and Ignition

Understanding the Flammable Range

Composition-dependent. Flammability limits are test-derived reference values, not universal boundaries for every pressure, temperature, oxygen concentration or gas mixture.

01

Below the LFL

The mixture is too lean under the stated test conditions, but continuing leakage can increase concentration and create a flammable zone.

02

Within the range

An ignition source can produce flame propagation, flash fire or explosion depending on confinement, congestion and turbulence.

03

Above the UFL

The mixture is too rich under the stated conditions, but dilution with air can move it back through the flammable range.

%LEL is not volume percent. A reading of 10% LEL means one tenth of the detector's configured lower flammability reference, not 10% gas by volume. Conversion depends on the target gas and calibration basis.

Gas Detection Strategy

Define the Measurement Objective First

Life and fire safety

Use suitable fixed or portable combustible-gas detection, alarm actions, ventilation interlocks and emergency isolation where justified.

Worker exposure

Add toxic-gas or oxygen channels when the gas or its impurities create hazards below the combustible range.

Process control

Volume-percent analyzers, gas chromatography or component-specific instruments may be needed for composition and quality.

Alarm settings depend on the gas, application, jurisdiction, instrument, applicable standards and site-specific risk assessment. Do not copy a workplace limit into a combustible alarm or treat the instrument range as an alarm recommendation.

Sensor and Detector Technologies

How Coal Gas Is Detected

A gas sensor is the sensing element. A detector packages the sensor with electronics and alarms. A monitor may calculate exposure or log trends. An analyzer measures composition or quality. A leak detector may identify a release without reporting area concentration.

Multi-channel fixed system

Uses separate LEL, CO, H₂S and O₂ sensors.

Technology
Suitable useArea and confined-space protection.
AdvantagesMatches the combined hazards.
LimitationsRequires coordinated alarms, maintenance and cross-sensitivity review.
Verification pointsConfirm calibration gas, cross-sensitivity, oxygen dependency, temperature, humidity, response time and maintenance requirements.

Catalytic or IR LEL

Measures combustible content on a calibration basis.

Technology
Suitable useFire/explosion warning.
AdvantagesStandard safety channel.
LimitationsMixture correction can change with hydrogen/methane ratio; hydrocarbon IR may miss hydrogen.
Verification pointsConfirm calibration gas, cross-sensitivity, oxygen dependency, temperature, humidity, response time and maintenance requirements.

Electrochemical CO/H₂S

Electrode current measures toxic components.

Technology
Suitable useLow-ppm toxic protection.
AdvantagesSensitive and portable/fixed.
LimitationsCross-sensitivity and high-concentration over-range.
Verification pointsConfirm calibration gas, cross-sensitivity, oxygen dependency, temperature, humidity, response time and maintenance requirements.

Gas chromatography / process analyzer

Separates mixture components.

Technology
Suitable useHeating value, process control and calibration definition.
AdvantagesDetailed composition.
LimitationsNot a substitute for fast local alarms.
Verification pointsConfirm calibration gas, cross-sensitivity, oxygen dependency, temperature, humidity, response time and maintenance requirements.

Ultrasonic

Detects pressurized leakage.

Technology
Suitable useOpen gas-holder and compressor areas.
AdvantagesEarly complement.
LimitationsNo composition or concentration.
Verification pointsConfirm calibration gas, cross-sensitivity, oxygen dependency, temperature, humidity, response time and maintenance requirements.
Detector Placement

Where Detectors Should Be Installed

Priority locations

  • Near ovens, exhauster houses, gas holders, valves and compressors
  • At occupied routes and enclosed process buildings
  • At low and high points selected from actual hot/cold release and ventilation analysis
  • At confined-space entries with remote sampling for O₂, LEL, CO and H₂S
  • Inside sample panels with tar/condensate conditioning and flow-fault alarms

Placement review checklist

  • Credible release points and failure modes
  • Gas temperature, pressure and release momentum
  • Supply and exhaust airflow under normal and failed conditions
  • Room geometry, ceilings, pits, trenches and obstructions
  • Worker breathing zones and egress routes
  • Access for calibration, bump testing and replacement
  • Sampling-line delay and representative sample pickup

Gas density alone is not sufficient to determine detector placement. Validate the proposed layout against real operating modes and ventilation states.

Calibration, Bump Testing and Maintenance

Keep the Monitoring System Dependable

Functional checks

  1. Inspect the instrument, inlet, filter, power and alarm path.
  2. Apply the correct challenge gas to confirm response and alarm action.
  3. Calibrate at the specified interval or when the check fails.
  4. Verify relays, ventilation, shutdowns and remote annunciation.
  5. Document results, faults, sensor age and corrective work.

Factors that shorten intervals

  • Exposure to high gas concentrations or sensor poisons
  • Extreme temperature, humidity, dust or condensation
  • Mechanical shock, vibration or enclosure damage
  • Long sample lines, pumps and multiple sample points
  • Critical safety interlocks or regulatory requirements
  • Manufacturer alerts, failed checks or unexplained drift
Engineering Controls and Emergency Response

Control the Source Before Relying on Alarms

Engineering and administrative controls

  • Leak-tight design, suitable materials and preventive maintenance
  • Ventilation sized for credible release conditions
  • Emergency isolation and shutdown from a safe location
  • Ignition control, bonding, grounding and classified equipment
  • Permit, purge, confined-space and hot-work procedures
  • Alarm actions that are trained, documented and periodically exercised

During an alarm or suspected leak

  1. Leave the affected area and warn others.
  2. Do not enter an unknown atmosphere.
  3. Eliminate ignition only when it can be done safely and remotely.
  4. Contact trained emergency responders.
  5. Use appropriate respiratory and protective equipment.
  6. Follow the facility emergency plan before re-entry.

Do not attempt rescue without training and protection. A flammable atmosphere may also be oxygen deficient, toxic or immediately dangerous to life and health.

Sampling and Cross-Sensitivity

Common Measurement Challenges

Sampling system considerations

  • Tar, moisture and condensate can delay or block the sample.
  • Heated lines or conditioning may be required for process analysis.
  • Do not remove a toxic component in a scrubber or filter before the safety sensor unless intentionally designed and validated.
  • Record transport time and response for every component and sample point.

Cross-sensitivity and correction

Combustible sensors may respond differently to the calibration gas and the actual gas. A correction factor is instrument-, sensor- and condition-specific. Mixed fuels can change both sensor response and the true flammability basis.

Verify oxygen dependency, catalyst poisoning, optical selectivity, temperature and humidity effects, pressure, response time and over-range recovery with the instrument documentation and site test program.

Common Misconceptions

Practical Answers to Frequent Mistakes

“Coal gas is just methane.”

It may contain substantial hydrogen and carbon monoxide plus other components.

“A clear LEL reading means the atmosphere is safe.”

CO can be dangerous far below flammable concentrations.

“One IR detector covers every component.”

Hydrocarbon IR may not respond to hydrogen or CO.

“The mixture is stable.”

Composition changes with coal, oven operation and gas cleaning.

Technology Comparison

Comparing Detection Approaches

TechnologySuitable useAdvantagesLimitations
Multi-channel fixed systemArea and confined-space protection.Matches the combined hazards.Requires coordinated alarms, maintenance and cross-sensitivity review.
Catalytic or IR LELFire/explosion warning.Standard safety channel.Mixture correction can change with hydrogen/methane ratio; hydrocarbon IR may miss hydrogen.
Electrochemical CO/H₂SLow-ppm toxic protection.Sensitive and portable/fixed.Cross-sensitivity and high-concentration over-range.
Gas chromatography / process analyzerHeating value, process control and calibration definition.Detailed composition.Not a substitute for fast local alarms.
UltrasonicOpen gas-holder and compressor areas.Early complement.No composition or concentration.
Frequently Asked Questions

Coal Gas FAQ

What is coal gas made of?

It can contain hydrogen, methane, carbon monoxide, carbon dioxide, nitrogen and sulfur compounds in varying proportions.

Does coal gas have one LEL?

No. The flammable range depends on the actual mixture and conditions.

Why is carbon monoxide monitoring needed?

CO can cause toxic exposure at concentrations far below the LFL.

Which detectors are used for coal gas?

LEL, CO, H₂S and oxygen channels are commonly combined, with process analyzers for composition.

Can methane NDIR detect all coal gas?

No. It may miss hydrogen and does not measure CO toxicity.

Where should detectors be installed?

Near gas equipment, occupied areas, ventilation paths and confined-space access points based on release scenarios.

Why are sample lines difficult?

Tar and condensate can absorb gas, block flow and contaminate sensors.

Is coal gas still used?

Coke-oven gas remains important in steelmaking, while historical town-gas infrastructure may still present legacy hazards.

What calibration gas should be used?

Use a representative mixture or manufacturer-approved strategy based on current process composition.

What should happen during a coal-gas alarm?

Evacuate, isolate remotely, prohibit entry and have trained responders evaluate LEL, oxygen and toxic components.

Authority Links

Sources and Further Reading

Values and requirements may differ by jurisdiction, standard, composition and test condition. Confirm the rules and product documentation that apply to the project.

Educational content only: This page does not replace emergency services, a site risk assessment, local fire and electrical codes, occupational hygiene advice or qualified engineering judgement.

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