Ask The HvacMan
Air Grilles
Air Diffusers
Air Quailty
All Air Systems
All Water Systems
Boilers
Building .Managament Systems ..BMS
Burners
Chillers
Cooling Towers
Cooling Load Calculation
Cryogenics
Energy Saving
Duct
Duct ,Smacna
Dampers ,Air
Dust Collection
Fans
Fire Dampers
Glass Selection
Heating
Heat Exchangers,water
Heat Recovery
Heat Tracing Systems
Hepa Filters
Hvac Applications
Humidifiers / Dehumidifiers
Insulation , Duct
Insulation , Pipe
Insulation , Sound
Nano Tech.,In Building
Occupancy Sensors
Pneumatic Conveying
Piping
Pool Ventilation
Process Piping
Psychrometry
Pumps
Radiant Heating
Refrigerant Systems
Solar Collectors
Sound
Steam Generation
Tables & Charts Gnr.
VAV Sytems
Valves
Ventilation
VRV Systems
STORE
Solar Collectors
Flat Plate Collectors
Evacuated Tube Collectors
Concentrating Collectors
Transpired Collectors
Solar Control Systems
Standalone Systems
Grid Connected Systems
Hybrid Systems
Back-up Systems
Solar Cells
Solar Arrays
Inverters
Change Controller
Turbines
Hybrid Systems
Grid Systems
Water Pumping
Using Wind Energy
Enviromental Aspects
Buyer's Guide
 
Save Energy
Solar Water Heating
Solar Electric Systems
Wind Turbines
Passive Solar Heating
Passive Solar Cooling
Building Material
Water Conservation
Ground Source Heat-Pumps
Green Hotels

Glass &Windows Selection

Wednesday, 25 April 2007 - 3:30 PM

: Aluminum-Dust Explosion

An explosion occurred in equipment that was being used to pulverize aluminum-alloy ingots, to form a powder with small particle size. In this process, air was recycled through a grinder, cyclone product separator, and blower, with a side stream to extract undesired dust to a dust collector. However, the concentration of dust in the circulating air stream was above the Minimum Explosible Concentration in most of the recycle system. Ignition of this dust/air dispersion occurred as a result of an exothermic oxidation of accumulated combustible dust in the return-air ductwork, accelerated by the relatively high temperature of the circulating air. Because the system was not protected against internal explosion, an access door on the grinder was forcibly ejected, and the door struck the LPG cylinder on a nearby forklift truck. Escaping LPG vapors – ignited by the dust fireball from the open grinder door – resulted in a flash fire that caused fatal burn injuries to the forklift driver.
This powder-producing operation initially was a batch process, and it had operated without incident for many years. When a decision was made to convert the batch process to a continuous process, some hazardous changes were introduced that were not recognized. These changes included (1) a much higher rate of dust generation, (2) high concentrations of very fine dust in the recycle stream, and (3) accumulation of heat in the recycle stream. In addition, the installer of the recycle system did not have experience with combustible powders, and no explosion prevention or protection devices or systems were provided.

Among the lessons learned from this incident were: (1) every significant change in a process should be subjected to a Management of Change analysis; (2) producers of hazardous materials (and particularly small-company producers) need to follow Codes and Standards that apply to their processes; (3) code-enforcing authorities should become more familiar with Codes and Standards that apply to dust-explosion hazards; and (4) dust-explosion characteristics need to be included in Material Safety Data Sheets.

 

 

 
Google
 
Web www.iklim.com
  Discuss on the Message Board
   
 
  http://www.iklimnet.com
 
Hotels
Enviroment
Legionnare Disease
Energy Saving
Control Software
Hotel Design Books

Hotel Design