Does your facility have a dust problem: Methods for evaluating dust explosion hazards

• Published in: Journal of loss prevention in the process industries Vol. 24; no. 6; pp. 837 - 846
• Main Authors: Davis, Scott G., Hinze, Peter C., Hansen, Olav R., van Wingerden, Kees
• Format: Journal Article
• Language: English
• Published: Kidlington Elsevier Ltd 01.11.2011; Elsevier Science Ltd
• Subjects: Dispersion; Dust; Dust explosion; Dust Explosion Simulation Code (DESC); Explosion modeling; Health risk assessment; Occupational hazards; Occupational safety; Process safety; Risk assessment; Risk reducing measures; USA; Europe; Process safety; Risk reducing measures; Dust Explosion Simulation Code (DESC); Explosion modeling; Dust explosion; Risk assessment
• ISSN: 0950-4230; 1873-3352
• DOI: 10.1016/j.jlp.2011.06.010

The hazards of dust explosions prevailing in plants are dependent on a large variety of factors that include process parameters, such as pressure, temperature and flow characteristics, as well as equipment properties, such as geometry layout, the presence of moving elements, dust explosion characteristics and mitigating measures. A good dust explosion risk assessment is a thorough method involving the identification of all hazards, their probability of occurrence and the severity of potential consequences. The consequences of dust explosions are described as consequences for personnel and equipment, taking into account consequences of both primary and secondary events. While certain standards cover all the basic elements of explosion prevention and protection, systematic risk assessments and area classifications are obligatory in Europe, as required by EU ATEX and Seveso II directives. In the United States, NFPA 654 requires that the design of the fire and explosion safety provisions shall be based on a process hazard analysis of the facility, process, and the associated fire or explosion hazards. In this paper, we will demonstrate how applying such techniques as SCRAM (short-cut risk analysis method) can help identify potentially hazardous conditions and provide valuable assistance in reducing high-risk areas. The likelihood of a dust explosion is based on the ignition probability and the probability of flammable dust clouds arising. While all possible ignition sources are reviewed, the most important ones include open flames, mechanical sparks, hot surfaces, electric equipment, smoldering combustion (self-ignition) and electrostatic sparks and discharges. The probability of dust clouds arising is closely related to both process and dust dispersion properties. Factors determining the consequences of dust explosions include how frequently personnel are present, the equipment strength, implemented consequence-reducing measures and housekeeping, as risk assessment techniques demonstrate the importance of good housekeeping especially due to the enormous consequences of secondary dust explosions (despite their relatively low probability). The ignitibility and explosibility of the potential dust clouds also play a crucial role in determining the overall risk. Classes describe both the likelihood of dust explosions and their consequences, ranging from low probabilities and limited local damage, to high probability of occurrence and catastrophic damage. Acceptance criteria are determined based on the likelihood and consequence of the events. The risk assessment techniques also allow for choosing adequate risk reducing measures: both preventive and protective. Techniques for mitigating identified explosions risks include the following: bursting disks and quenching tubes, explosion suppression systems, explosion isolating systems, inerting techniques and temperature control. Advanced CFD tools (DESC) can be used to not only assess dust explosion hazards, but also provide valuable insight into protective measures, including suppression and venting. ► A semi-quantitative short-cut risk analysis method (SCRAM) has been presented. ► SCRAM assesses dust explosion risk & reveals the most hazardous areas in facilities. ► SCRAM studies adequate preventive and protective measures to reduce high-risk areas. ► SCRAM provides a process hazard analysis of the facility and process per NFPA 654. ► An advanced tool (DESC) can greatly help engineers designing powder-handling plants.