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Testing and consulting on the explosion risks associated with devices and processes which use or produce hydrogen
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Safe storage or processing requires an understanding of the possible hazards associated with sensitivity to variations in temperature

Adiabatic Calorimetry
Data demonstrate the consequences of process upsets, such as failed equipment or improper procedures, and guide mitigation strategies including Emergency Relief System (ERS) design
Reaction Calorimetry
Data yield heat and gas removal requirements to control the desired process chemistry
Battery Safety

Testing to support safe design of batteries and electrical power backup facilities particularly to satisfy UL9540a ed.4

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Develop critical safety data for inclusion in SDS documents

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Evaluate electrical cables to demonstrate reliability and identify defects or degradation
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Testing and analysis to ensure that critical equipment will operate under adverse environmental conditions
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Analysis and testing to identify and prevent unwanted hydraulic pressure transients in process piping
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Fauske & Associates fulfills the requirements of ISO/IEC 17025:2017 in the field of Testing

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Fauske & Associates fulfills the requirements of ISO 9001:2015
Dust Hazards Analysis
Evaluate your process to identify combustible dust hazards and perform dust explosion testing
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On-site safety studies can help identify explosibility and chemical reaction hazards so that appropriate testing, simulations, or calculations are identified to support safe scale up
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Design emergency pressure relief systems to mitigate the consequences of unwanted chemical reactivity and account for two-phase flow using the right tools and methods
Deflagrations (Dust/Vapor/Gas)

Properly size pressure relief vents to protect your processes from dust, vapor, and gas explosions

Effluent Handling

Pressure relief sizing is just the first step and it is critical to safely handle the effluent discharge from an overpressure event

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FATE (Facility Flow, Aerosol, Thermal, and Explosion) is a flexible, fast-running code developed and maintained by Fauske and Associates under an ASME NQA-1 compliant QA program.

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Adiabatic Safety Calorimeters (ARSST and VSP2)

Low thermal inertial adiabatic calorimeters specially designed to provide directly scalable data that are critical to safe process design

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Products and equipment for the process safety or process development laboratory

FERST

Software for emergency relief system design to ensure safe processing of reactive chemicals, including consideration of two-phase flow and runaway chemical reactions

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Recent Posts

An Explosion Accident Case Review and Investigation: PSM

Posted by Fauske & Associates on 04.16.14

 

process safety evaluationA deflagration incident (explosion) occurred during the cleaning procedure of a pan coater that was used in an encapsulation process where a latex coating was spray-applied intermittently to small beads of an oxidizing chemical. This case study describes the incident, and investigation including reviewing testing results, providing process hazard evaluation (PHA) and outlining benefits of process safety management (PSM) systems and best practices for fire and explosion protection due to combustible dust.                             

Incident Description

The company employed four pan coaters in series. Each had an exhaust tube connected to a common duct leading to a wet dust collector as well as an air connection utilizing a common air supply. On the day of the incident, two of the four pan coaters required cleaning due to a layer of latex and chemical that adhered to the inside of the pan. The cleaning process presented a challenge since the pan geometry made it difficult to clean, and the well-cured coating adhering to the pan proved stubbornly resistant to scraping, chipping and other physical means of attack.

In frustration at the difficulty of removing the residual coating, an employee began to chisel at it forcefully with a large and heavy steel pry bar.  The repeated blows from the pry bar caused a roughly 2 inch diameter area on the exterior of the pan to glow red from heat. Two employees then observed the red spot rapidly grow to approximately 6 to 8 inches in size. At this time, they chose to evacuate the room. Approximately 20 seconds later an explosion occurred.

There was no explosion isolation in place between the pan coaters to prevent deflagration propagation between the interconnected pieces of equipment. Such isolation is recommended by NFPA 654, Standard for the Prevention of Fire and Dust Explosions from the Manufacturing, Processing, and Handling of Combustible Particulate Solids. As a result the deflagration pressure wave and fire generated from the incident spread out of the pan coater mouth and through the exhaust ductwork to the other interconnected coaters.  Due to overpressure, the exhaust system ductwork ruptured.  Residual coating material in the other dirty pan coaters also ignited.  Thankfully, no personnel were injured.

Incident Testing Results

In an effort to characterize the events that led to the incident, several Differential Scanning Calorimetry (DSC) tests were performed using several ratios of coating to oxidizer material. The most energetic sample was then tested in various forms for drop weight impact (BAM Fallhammer) testing. It should be noted that samples 3 and 6 were wet material.

 drop impact sensitivity testing   differential scanning calorimetry tests

Integrated Solution

Though this process was not covered by OSHA Process Safety Management (PSM), several elements of PSM were utilized to reduce risk, improve methods, review management systems and ensure that personnel were aware of critical tasks.

Incident Investigation

  • Root cause analysis identified impact sensitivity, lack of appropriate procedures and inappropriate cleaning tools

Process Safety Information (PSI)

  • Thermal stability and impact sensitivity were not known
  • Cleaning procedures were not available/reviewed during the PHA 

Process Hazard Analysis (PHA)

  • PHA was performed, however PSI was not complete
  • Appropriate personnel were not involved
  • Change in raw material was not considered regarding the impact on the process

Mechanical Integrity (MI)

  • Usage and wear of equipment was reviewed to determine appropriate maintenance and replacement schedules
  • Reviewed MI program with employees to define expectations and unacceptable repair methods

Procedures

  • Job Hazard Analyses (JHAs) were conducted with employees to identify hazards associated with operations cleaning and maintenance tasks associated with equipment used for this process

Training

  • Operators were trained regarding updated procedures, as well as the functionality of the MI and Management of Change (MOC) programs and how to access these programs

Facility Siting & Human Factors                          

  • New production facility was designed incorporating industry best practices

 

Conclusion

Updated process safety information was used to reduce risks associated with this process:

  1. Several alternative cleaning strategies were investigated and a non-impact method was selected.

  2. Spray methodology was changed to reduce the accumulation of coating on the inside wall of the pan coaters by improving the angle of the spray and reducing the timing of the spray.

  3. Employee involvement in the review of procedures was critical to understand current practices, evaluate potential alternatives and obtain employee support for the procedure changes that followed

 
Process Safety Management (PSM) Overview

Topics: Combustible Dust, Process Safety, Process Hazards Analysis, Flammability

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