Chemical Process Safety (PSM/RMP)

Ammonia Gas Explosion

Explosion at Belle Vue: 2 injured between life and death Tuesday, September 27, 2011, 17:11 An explosion occurred this morning at the Belle-Vue brewery Leeuw-Saint-Pierre. Two people were seriously injured. Their prognosis is engaged. The leak was stopped. An ammonia leak occurred around 8:50 Tuesday when three workers from an outside firm conducted the dismantling of an old installation. ” The

“Operator Rounds” in a PSM/RMP Covered Process

In many chemical processes around the world, operators are making their rounds checking on those items that have been deemed “critical to process safety”.  These rounds usually include checking pressure, temperature, tell-tale gauges, tank levels, heat tracing, taking samples, etc.  But in many instances involving these checklists, one item is painfully obvious after an incident–

ASME B31.5 Pressure Testing and Leak Testing Requirements for Ammonia Refrigeration Processes

2015 UPDATE: Some of my refrigeration PSM buddies reminded me that the industry now has its own RAGAGEP for piping installation, ANSI/IIAR 4-2015, Installation of Closed-Circuit Ammonia Refrigeration Systems.  I do applaud the IIAR for their work in establishing this ANSI standard for the industry, but for those so happy to “correct me” I like to point

AMMONIA SPILLS IN WISCONSIN 1993-2009

Some interesting data put together each year by the Wisconsin Department of Public Health Services.  2009 is the most recent update to their data.  Here are the summaries: Since 1993, Wisconsin has had 768 uncontrolled ammonia releases, representing approximately 45 releases per year. 445 (58%) of Wisconsin’s ammonia releases involved refrigeration systems. A total of 302 people have sustained injuries as

Establishing Safe Upper and Lower Limits

This regulatory requirement is often mismanaged, which oftentimes results in many other related issues within a process safety management system. In this article, I will discuss a methodology a facility can apply in establishing its “safe upper and lower limits.” In this example, I will use process pressure, as it is the easiest to illustrate,

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