Confined-space entry Manholes, tanks, vessels, and sewers | Oxygen, flammable gases or vapors, and likely toxic gases such as hydrogen sulfide or carbon monoxide | Oxygen: 0–25% vol; flammables: 0–100% LEL; toxic-gas ranges selected for the gases expected, commonly H₂S 0–100 ppm and CO 0–500 ppm | Check that all required sensors are fitted; review alarm settings, response time, sampling method, and suitability for remote probe sampling if needed | Test the atmosphere at multiple levels before entry and continue monitoring as required by the site procedure. Follow applicable confined-space rules and permit requirements. |
Wastewater and sewer work Wet wells, lift stations, and drainage systems | Hydrogen sulfide, oxygen deficiency, and flammable gas | H₂S: often 0–100 ppm or wider where the risk assessment requires it; oxygen: 0–25% vol; flammables: 0–100% LEL | Consider humidity and contamination resistance, a suitable sampling hose or probe, clear alarms, and a range that covers expected peaks | Do not choose a range solely from routine readings: assess potential peak concentrations and the applicable exposure limits. |
Industrial maintenance Boilers, engines, and process areas | Carbon monoxide, oxygen, and combustible gases, depending on the process | CO: commonly 0–500 ppm; oxygen: 0–25% vol; flammables: 0–100% LEL | Check sensor range and resolution, alarm configuration, operating temperature limits, battery life, and the required ingress protection | For catalytic-bead LEL sensors, confirm the atmosphere contains enough oxygen for measurement and assess possible sensor poisons or inhibitors. |
Solvent handling and spill response Paints, coatings, and chemical storage | Volatile organic compounds (VOCs), plus oxygen or flammable-gas hazards where relevant | PID instruments commonly display VOC readings in ppm as isobutylene equivalent; available ranges vary by instrument, often from low ppm levels to thousands of ppm | Verify lamp energy, compound response factors, humidity effects, calibration requirements, and whether the reading is suitable for the target chemical | A PID is a screening tool and does not identify every compound. Check the instrument’s detection limits and response data for the specific chemicals involved. |
Refrigeration and industrial cooling Plant rooms and equipment service | The refrigerant specified for the system; oxygen displacement may also be a concern in enclosed areas | Select a range and detection method specifically intended for the refrigerant and the expected leak levels | Confirm refrigerant compatibility, detection limit, cross-sensitivity, response time, and whether the instrument is intended for personal safety or leak locating | Refrigerants differ in properties and sensor response. A general-purpose combustible-gas sensor may not be appropriate for every refrigerant. |
Remote or extended-duration work Field inspection, utilities, and infrastructure | Choose the gas set from the site risk assessment; common combinations include oxygen, LEL, CO, and H₂S | Match each sensor’s full-scale range to the expected concentrations and required alarm thresholds | Consider operating duration, battery endurance, data logging, audible/visual/vibration alarms, environmental rating, and ease of bump testing | Check that the detector remains within its stated operating conditions and that bump tests, calibration, and maintenance can be completed on schedule. |