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I am proud to announce that SAFTENG and The Chlorine Institute have renewed our partnership for another year (through 2026). Members of The Chlorine Institute receive a FREE SAFTENG membership. If you qualify, please contact me
NOTE: Any trade group interested in becoming a partner with SAFTENG for your Member Companies, please reach out, and I can share the plan
SAFTENG has:
- Over 19,000 categorized unsafe acts/conditions and accident/injury photos
- Over 1,500 ppt's & doc's in the SAFTENG Library
- Over 5,000 Technical Articles on Process Safety, Emergency Response & OSH topics
- Over 450 videos (those not allowed on YouTube Channel)
Many THANKS to my NEW Members and those who CONTINUE to support SAFTENG:
1910.303(g)(1): “Space about electric equipment. Sufficient access and working space shall be provided and maintained about all electric equipment to permit ready and safe operation and maintenance of such equipment.”
1910.303(g)(1)(i): “Working space for equipment likely to require examination, adjustment, servicing, or maintenance while energized shall comply with the following dimensions, except...
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TRANSCAER® recently launched a 27-state training tour to provide education and training sessions on emergency response techniques involving anhydrous ammonia.
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Although both EPA and OSHA use similar definitions to define who is an “incidental contractor” and those contractors who need to be evaluated to work in, on, or adjacent to a “covered process”, there is still much confusion on the intent of the “contractor element” and which type of contractors should be included and the type of review that should really be taking...
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I know that I was shocked when I learned that a cooling tower can BURN TO THE GROUND while it is in service. I have even worked at facilities where I property insurer required us to install sprinkler systems INSIDE the cooling towers. I know it is hard to imagine, but it happens.
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Some interesting data on Anhydrous Ammonia releases in NY state from 1993-1998.
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I have been asked to explain the difference between actions an operator may take during a process leak and the actions that the same operator may take as an “emergency responder” to the leak.
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Many THANKS to my NEW & RENEWING
Corporate Partners in Safety!
since 3/2011
since 3/2011
since 2007
since 2009
since 2/11
2011 Fatality Tracker
Electrical
6
(2010 = 90)
(2009 = 100)
Forklift/Manlift
Mobile Equipment
27
(2010 = 110)
(2009=88)
Mining
48...
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Still today (2011) we come across facilities working so hard to be the best they can be in PSM/RMP and in 99% of their process they are exceeding expectations. They are doing EVERYTHING WELL and running a VERY TIGHT ship…except for the loading and unloading of their Highly Hazardous Chemical (HHC).
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Nonconductive plastics and other nonconductive materials should be avoided in areas where flammable vapors, gases or powders may be present since static charges can accumulate on nonconductors. However, it is not always possible to completely eliminate nonconductors, so the following lists some of the ways to reduce the static hazard associated with these materials:
When it is necessary to use plastic...
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Cleaning small parts and portable equipment with solvents, either using an automatic device or manual cleaning, is a potentially extremely hazardous task relative to static generation and spark ignition of solvent vapors. Significant static electricity charging can occur during cleaning by contact and separation resulting from the following activities:
Solvent spraying, which can involve...
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One option for mitigating the static hazards associated with low conductivity liquids is to raise the conductivity of the liquid. This can be accomplished by either blending the low conductivity liquid with a conductive liquid (e.g., alcohol, ketone) or by adding a static dissipating additive into the low conductivity liquid.
When blending a low conductivity liquid with a conductive one, the...
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Toluene is a widely used low conductivity flammable liquid. Toluene’s vapor pressure is such that one is assured of a flammable vapor/air mixture at the ambient temperatures found in most facilities. The Lower Explosive Limit (LEL) of toluene is 1% and is reached at a temperature of 40°F (4°C). The Upper Explosive Limit (UEL) is 7% and is reached at a temperature of approximately 98°F...
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