Explosive Atmosphere from Residual Hydrocarbons or Chemicals
HighIndustrial vessels that previously contained flammable liquids, gases, or chemicals may retain residues in welds, seams, internal structures, or porous insulation materials. When vessels are opened or subjected to hot work cutting, these residues can volatilise creating flammable vapour concentrations within the explosive limit range. Hydrocarbons including petrol, diesel, oils, and solvents have low flash points and generate explosive atmospheres at relatively low concentrations. Heating during oxy-cutting accelerates vaporisation creating explosive conditions even in vessels considered 'clean'. The confined geometry of vessels prevents vapour dispersal and creates uniform explosive mixtures throughout the vessel volume. Any ignition source including cutting flames, sparks from grinding, static electricity, or hot metal can trigger explosive deflagration with catastrophic consequences.
Consequence: Explosion causing multiple fatalities, severe burns, blast injuries to workers on and off-site, destruction of surrounding structures and equipment, environmental contamination, and major regulatory investigation and prosecution. Historical incidents have caused deaths of workers not directly involved in cutting operations due to blast forces and flying debris.
Oxygen Deficient or Toxic Atmosphere in Confined Vessel Space
HighVessels create confined spaces where oxygen can be depleted through various mechanisms including displacement by inert gases (nitrogen, argon, CO2) used in decommissioning, oxygen consumption by corrosion of internal steel surfaces, biological decomposition of organic residues, or poor ventilation in sealed structures. Oxygen concentrations below 19.5% cause physiological effects with rapid onset. Workers entering oxygen-deficient vessels lose consciousness within seconds without warning symptoms, preventing self-rescue. Toxic atmospheres can also develop from chemical residues, decomposition products, or release of absorbed substances from vessel linings. Hydrogen sulphide from biological decomposition of organic materials is particularly dangerous, causing rapid unconsciousness and death at concentrations above 500ppm.
Consequence: Rapid unconsciousness and death from asphyxiation within 2-3 minutes of exposure to oxygen-deficient atmosphere. Toxic gas exposure causing acute poisoning, respiratory failure, neurological damage, or chronic health effects. Multiple casualties common as rescuers enter without proper equipment attempting to save initial victims.
Hot Work Fire and Ignition Hazards During Vessel Cutting
HighVessel demolition requires hot work operations including oxy-acetylene cutting, plasma cutting, and grinding to sever steel shells and internal structures. These processes create open flames, molten metal, sparks, and hot surfaces capable of igniting flammable materials, vapours, or combustible insulation. Sparks from cutting can travel several metres and penetrate small openings to reach flammable atmospheres in adjacent vessel sections. Hot metal sections can ignite combustible materials hours after cutting. Cutting through multi-layer coatings including bitumen, tar, rubber, or plastic linings releases flammable vapours and burning materials. Internal insulation materials including mineral wool, foam, or organic materials can ignite and create intense fires within confined vessel spaces.
Consequence: Fire within or adjacent to vessel causing burn injuries or fatalities, rapid smoke generation in confined spaces causing asphyxiation, fire spread to adjacent vessels or structures, damage to surrounding plant and equipment, and extended site evacuation. Fires in vessels containing residual chemicals can generate toxic combustion products.
Structural Collapse During Sequential Vessel Cutting
HighLarge vessels derive structural strength from shell continuity and internal support structures including rings, stiffeners, baffles, and cone sections. As cutting progresses, load paths are severed and remaining sections must support increasing loads. Unsupported vessel sections can suddenly collapse inward or buckle outward, crushing workers inside or adjacent to the vessel. Partially cut sections can fall unexpectedly particularly when supporting structures are weakened. Vessels on elevated stands or towers present additional fall hazards as supports are removed. Temperature changes from cutting operations cause thermal expansion and contraction creating unpredictable stresses. Vibration from cutting equipment can trigger collapse of weakened sections. Large diameter horizontal vessels can roll if support points are removed asymmetrically.
Consequence: Workers crushed or trapped by collapsing vessel sections causing multiple fatalities, falling vessel components striking workers below, uncontrolled vessel movement crushing workers or damaging equipment, and secondary injuries during rescue operations in unstable structures.
Confined Space Entry and Egress Difficulties
HighAccessing vessel interiors for inspection, cleaning, and cutting requires entry through small access points including manholes typically 450-600mm diameter. Workers wearing respiratory protection, harnesses, and carrying equipment must fit through restricted openings. Internal ladders, baffles, and structures create obstacles complicating movement. Emergency egress from vessels is severely restricted, with workers potentially requiring several minutes to reach exit points even in non-emergency conditions. Injured or unconscious workers cannot self-rescue from vessels. Standard stretchers do not fit through typical manhole openings requiring specialised retrieval equipment. During emergencies including fire, toxic release, or oxygen deficiency, workers may become disoriented in unfamiliar vessel interiors. Panic and restricted movement during emergency egress has contributed to multiple confined space fatalities.
Consequence: Workers unable to escape rapidly during emergencies leading to toxic exposure, asphyxiation, or burn injuries. Failed or delayed rescue of injured workers due to access restrictions causing preventable deaths. Rescuers becoming secondary casualties when entering vessels without proper procedures and equipment.
Hazardous Coatings and Asbestos Insulation Exposure
HighIndustrial vessels constructed before 1990 frequently have asbestos-containing insulation on external shells and internal components. Asbestos cloths, papers, and spray coatings were commonly applied for thermal insulation and fire protection. Cutting through vessel shells disturbs and releases asbestos fibres creating severe exposure risk. Multiple coating layers may exist with deeper layers containing lead-based paints, chromium compounds, PCBs, or other banned substances. Hot cutting vaporises coating materials creating toxic metal fumes and particulates. Internal vessel linings may contain hazardous materials including epoxy resins, rubber compounds containing carcinogens, or chemical-resistant coatings with toxic components. Shot blasting or grinding to prepare surfaces for cutting generates substantial dust containing these materials.
Consequence: Asbestos exposure causing mesothelioma, lung cancer, and asbestosis with 20-40 year latency period. Lead exposure causing neurological damage, kidney disease, and reproductive harm. Acute toxic exposure to coating fumes during hot work causing respiratory injury, chemical burns, or systemic poisoning. Chronic disease development years after exposure.