Loss Prevention in the Process Industries: Hazard Identification, Assessment and Control, Volumen 1

accidents alarm ammonia ammonium nitrate assessment atmosphere autoignition temperature calculated cause chemical reactors chlorine cloud explosions codes combustion compressor concentration corrosion damage deflagration density described detonation distance dust effect electrical energy Engineers equation equipment ethylene ethylene oxide factor Factories Act failure rate fault tree flame flammability limit flash point Flixborough disaster flow gases given in Table heat hydrogen important Inspectorate installations instrument Item Kletz layout legislation liquid loss prevention maintenance Major Hazards materials maximum measures method mixture normal nuclear occur overpressure parameters particular Petroleum pipe pressure relief pressure vessels probability problem process computer protection pump reaction reactor Regulations release reliability risk safety Selected references shown in Figure standard steam steel storage stress tank temperature tion toxic trip system UKAEA unconfined vapour cloud vapour cloud explosions velocity vent