VDI 3673 PDF

The VDI Guideline “Pressure Release of Dust Explosions ” published in. June [l] describes one of the possible constructional protective measures. Buy VDI PRESSURE RELEASE OF DUST EXPLOSIONS from SAI Global. 9 Nov Some equipment suppliers use the German VDI guide as a basis for the design of explosion relief vents. This is acceptable, and much of.

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Explosibility; Thermal and pressure conditions; Flammability; Toxicity; Environmental problems.

This asks for a lightweight roof for HFL stores. The relevant Level 2 Criteria are: BS EN 1: Pressure relief needs to take into account the nature of the reaction mixture involved, e.

Hazards that merit consideration include: Influential and widely used. Explosion relief from buildings HSE’s traditional advice for buildings storing flammable liquids has been to ask for a lightweight roof, which will act as explosion relief vdj a vapour cloud ignited fdi the building, and this has not changed as a result of DSEAR.

The material released from an explosion relief vent typically includes quantities of the original, unburnt substance in addition to combustion products.

VDI-Standard: VDI 3673 Pressure release of dust explosions

Existing panels do not need to be replaced, but they should be suitable for the purpose. These factors will have a significant impact on plant layout, design of plant and supporting structures gdi explosion relief routes.

A guide to the prevention, control and mitigation of dust explosions, aimed at operators of such plant, not designers. Prevention of fires and explosions in dryers, Abbott, J. Containment explosion-resistant construction vdu High speed isolation; Segregation keeping catalysts or pyrophoric materials apart from other products ; Explosion pressure relief venting ; Explosion suppression. A European harmonised standard for solvent evaporating ovens prefers alternative precautions for many applications, but in the dust handling industries explosion relief remains a widely used mitigation measure.

Explosion relief This Technical Measures Document refers to the explosion relief measures that can be adopted in plant design to ensure safe operation. Paragraphs 60 to 87 discuss explosion relief and plant design and layout.

Relief points from explosion protection devices should normally be located outside the building containing the plant, but certainly not in the vicinity of regularly occupied areas or plant that would be easily damaged. This website uses non-intrusive cookies to improve your user experience.


Explosion relief

The operator should have shown due consideration of these hazards and taken appropriate measures to provide pressure relief. Useful for understanding the factors that influence an event. Operators need 363 draw a clear distinction between pressure relief designed to protect against an explosion, and relief designed to protect plant from some other cause of overpressure. This provides many cross-references to other sources of information, but some of these are obsolete, and the whole document is about to be rewritten.

However, it is worth noting that even finely powdered solids are significantly less easily dispersed than are gases and volatile liquids – with vdk hazard ranges as a result. Explosion vent panels and doors are considered as autonomous protective systems within the meaning of the ATEX equipment regulations.

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Pressure release of dust explosions | VDI

A dust explosion could then be an initiator of a major accident. Normally the following options should be considered to prevent an explosion inside the plant:. Dust explosions especially in powder transfer and dryers A dust explosion can take place only if a number of conditions are simultaneously satisfied: Measures to prevent major accidents should address all potential initiators.

The reports on the Manro and Chemstar incidents show the possibilities with distillation plant, but inadequate explosion relief was not the prime problem in this case.

These groupings are as follows:. This is because it is often impossible to prevent the formation of dense dust clouds inside the process. However, many toxic materials are handled in fine powder form, and a serious dust explosion could cause a major accident. Provision of ventilation, where plant is within buildings, to reduce the concentration of gas or vapour to a safe value; Construction of plant so as to prevent gas or vapour escaping, forming explosive mixtures with air and reaching ignition sources; Removal or protection of ignition sources, especially electrical sources References For further information on the relevant British Standardsplease access the British Standards web site and use the search facility.


Normally the following options should be considered to prevent an explosion inside the plant: In particular the possibility of pressure piling needs to be considered.

VDI – NFPA 68 – Venting of Explosion

When unstable substances are in vdii, the operator should demonstrate that at the research stage of the product a systematic approach to the identification of hazards relating to the nature of the materials has been followed. Some equipment suppliers use the German VDI guide as a basis for the design of explosion relief vents.

More recently, work within CEN has produced a rationalisation and simplification of the design equations recommended, and this standard should be adopted when it becomes available. These groupings are as follows: It may also be provided on buildings, which contain plant that gives rise to risk of a rapid and substantial release of gas inside the building.

Many different equations have been vdj, each with a restricted range of applicability, and plants will be found which have used all these design equations. The adoption of measures such as these is likely to be necessary where the process of venting could itself lead to the release of sufficient toxic material to create a major accident.

Dust may be grouped into dust explosion classes as determined using standard test apparatus. Section 10, Paragraph Hazards that merit consideration include:. The dust must be explosible refer to table on dust explosion classes ; The dust vdl have a particle size distribution that will allow the propagation of flame The atmosphere into which the dust is dispersed as a cloud or suspension must contain sufficient oxidant to support combustion; The dust cloud must have a concentration within the explosible range; The dust cloud must be in contact with an ignition source of sufficient energy to cause an ignition.

K ST is defined as the maximum rate of pressure rise measured in a 1m3 vessel, it is usually calculated from measurements in smaller test apparatus.