Dangerous Substances & Explosive Atmospheres Regulation 2002 The Basics. Richard Cowen Dip SH, Dip RSA, CMIOSH, MIIRSM, FRSPH, GI Fire E

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Transcription:

Dangerous Substances & Explosive Atmospheres Regulation 2002 The Basics Richard Cowen Dip SH, Dip RSA, CMIOSH, MIIRSM, FRSPH, GI Fire E

DSEAR Regulations 2002 Sets minimum requirements for the protection of workers from fire & explosion risks arising from dangerous substances and potentially explosive atmospheres These regulations consider hazardous areas due to the likely presence of explosive atmospheres ( Under atmospheric conditions ) These are created by dangerous substances consisting of a mixture with air of flammable substance in the form of a gas vapour or mist / dust. This then can be classified as a Hazardous Area

Objectives of the Regulation Identify the circumstances of work, the amount of dangerous substance used and the process of application Review activities and risk assess Review the effectiveness of the existing control measures Identify the probability of a flammable atmosphere being created & its duration Identify the likelihood of an ignition source Identify the scale of the fire or explosion Consider other places of work that the fire / explosion may effect

DSEAR - Fundamentals Risk Assessment must be available from the 1 st July 2003 Workplaces already in use are given up to July 2006 to comply If the workplace was in use before July 2003 but modified before July 2006 must comply at the time of the modification Where the workplace is brought into use after July 2003 must comply.

DSEAR In a nutshell! Employers and the self employed must; Carry out a risk assessment of any work activity involving dangerous substances Provide technical & organisational measures to eliminate or reduce sfarp the identified risks Provide equipment & procedures to deal with accidents and emergencies Provide information & training to employees Classify places where explosive atmospheres may occur into zones & mark zones

The Triangle of Fire Remove anyone of these & the fire will not occur!

Basic Terminology Flash point The lowest temperature at which the surface of a liquid gives off sufficient vapour to form a flammable mixture Auto Ignition Temperature The ignition temperature of a gas or vapour is the lowest surface temperature to which the most easily ignited fuel - air ratio of a flammable atmosphere has to be exposed to cause ignition Flammable range A mixture of fuel & air/ oxygen is only capable of being ignited if it is between the upper & lower explosive limits. Above UEL - Flammable mixture is too rich to ignite Below LEL - Flammable mixture is too weak to ignite Oxygen enrichment?

Basic Terminology Ventilation & Vapour density Good - rapid dilution of any gas or vapour that will reduce the atmosphere below the LEL. Vapour Density Heavier than / lighter than air Grade of Release Normal / Abnormal. Type of release Continuous Primary Secondary

Flash Point What is flash point? What impact will ambient temperature have on the chemical?

Prevention of a dust explosion

(Lower Explosive Limit) 10% 0% Lets start your car UEL (Upper Explosive Limit) Explosive Range Mixture of air and flammable gas is explosive if ignited LEL 100%

Basics of the BIG three Regs Reg 5 - Risk Assessment. (supporting the requirements MHSR 1999) Reg 6 Defines scope and priority of risk control measures (prescriptive) Reg 7 Hazardous area classification and diagrams

Reg 5 (2) Hazard Identification Reg 5 (2) risk assessment SHALL include Hazardous Properties Hazards consider the following Flash Point Acetone, -20 (HFL) Styrene based resin (Crystic), 31 to 40 (FL) Propane (LPG) -104 (EF) Kerosene 37-65 (FL)

Signage / GHS Explosive Stray electric currents Radiation Hot surfaces What's in your local Flam Cabinet! Are these chemicals stored correctly!

Basis of Safety - Methods of Control Eliminate Do we need to do the job Can it be done in a different way Substitute Do we need to do it with that substance Can we change the process/ remove ignition sources or surface temperatures Segregate Change location Enclose the process Engineering Control LEV Correct ex protection for equipment Bonding and Earthing Managerial Controls Permits to work Removing staff from the area etc Article 3 99/92/EC Prevention Avoidance Mitigation

Mitigation Control Measures Reduce Quantities 6(4)a Prevention of an ex atmosphere 6(4)d Avoid adverse conditions 6(4)f ii Minimise no of employees 6(5)a Avoid / minimise the release 6 (4b) Release to be contained 6(4)e Segregation of incompatible substances 6(4) g Avoid propagation of fires / explosions 6(5)b Control release at source 6(4)c Avoiding Ignition sources 6(4)f Design of Storage 6 (8) Provision of pressure relief 6(5)c Explosion suppression 6(5)d&e Provision of suitable PPE 6(5)f

Ignition sources

Temperature Classification Classification It is necessary to classify places where explosive atmospheres may occur into zones and mark these zones where necessary. Zone-t-21) is likely to occur in normal operation occasionally

Lets link our discussion together! UEL % LEL % TEMPERATURE

Reg 7 Hazardous Area Classification Developed over 50 years by the oil and chemical industries Takes no account of the consequences of an ignition Should be applied more systematically than in the past (requirements in Schedules to Regs) New specific link between the zone and equipment allowed in it

Zone Classification Classification It is necessary to classify places where explosive atmospheres may occur into zones and mark these zones where necessary. Zone-t-21) is likely to occur in normal operation occasionally Area c lassification does Identifies the point of release Estimates the extent & the duration of the flammable atmosphere Allocates grades & sizes to the hazardous areas Area classification does not Take account of the consequences of the ignition Specify the correct equipment to use

Reg 7(2) Equipment for use in hazardous zones Schedule 3 gives details of Category. Cat 1 in Zone 0/20, Cat 2 in Zone 1/21, Cat 3 in Zone 2/22 Zone 2 Zone 1 Zone 1 Zone 0 Zone 0

Zoning & Extent of the zone Zone boundaries are either calculated or identified via codes EN 60079-10-1/2 Petro chemical Gas storage Ammonia systems Zone boundaries will change in shape to allow for overlapping zones

Selection of apparatus & zoning

No ignition source No ignition source No fuel No ignition source

No oxygen No oxygen No fuel No fuel via restricted breathing

ATEX Marking

Intrinsic Safety Products for use in Hazardous Area : The released energy must be under the safety threshold also in case of fault. The risks are: high temperature sparks

Reg 7(3) Mark areas with signs at point The EX triangle sign is shown in Schedule 4. Use based on risk assessment and added safety value of entry 29

Questions?