Tuesday, November 13, 2012

Article: From Dust To Death - Six tips to stop dust collector explosions




Preventing combustible dust explosions has been an industry concern for years.   Increasing the stress for emergency health and safety managers trying to find the correct solution and maintain that solution for the future as well.  With so many standards, regulations, and codes one can get easily overwhelmed.  A recent article in ISHN Magazine by industry experts Tony Supine and Mike Walters condense the tedious task into a few informative tips.   

Reviewing the NFPA 654 standard will give you information on how to design a safe dust collection system.  It will also guide you to other NFPA standards regarding deflagration venting, explosion protection where venting is not possible, as well as standards for specific types of combustible dust and industries.   The NFPA has incorporated performance-based options, since 1995 using calculations in its standards for explosion protection equipment.   Since 2006 the NFPA has been allowing real world destructive test data to be used in place of the calculations data, as long as adequate testing has been proven.   Although often overlooked, real world data is permissible and your dust collection supplier may help you with cost savings and from over engineering,  all while not compromising safety.  

A hazard analysis is required to determine the level of fire and explosion protection required.  Testing the dust to determine the KST rating and Pmax by ASTM E 1226-10 standard needs to be established.  Quality is often overruled by a low price.   Is the value what it seems?  As documented a low-end dust collector will most likely need replacing after an explosion, where as a high quality gauge collector often only requires replacing only the explosion vent and filter cartridges.   High quality compliant equipment is reassurance and an investment in the future.   Keeping a clean facility is another key element in preventing dust explosions.  Hazardous levels of dust accumulation are the most common of all OSHA violations, often ending with fines.  The NFPA definition of hazardous surface dust is now 1/64 inch or 0.4mm in depth.   Staying alert of any changing conditions that can contribute to potential explosive problems should be normal practice.