Chemical Process Safety (PSM/RMP)

Not following National Board code for repairs to PVs can be very costly

On Dec. 3, 2004, a 50,000-pound steel pressure vessel violently exploded at the southwest Houston Marcus Oil and Chemical facility. The pressure vessel contained flammable hydrocarbons such as hexane. The pressure vessel was a horizontal tank 12 feet in diameter, 50 feet long, and operated at a pressure of approximately 67 psi. Marcus Oil did…...

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Not following National Board code for repairs to PVs can be very costly Read More »

Leak Testing a PV kills worker

On January 15, 2008, a pressure vessel at a New Jersey foundry exploded, killing one 60-year-old worker instantly while injuring eight other workers with shrapnel. The pressure vessel in question was used to pressurize/depressurize molten aluminum to prevent/eliminate porosity from the metal. The incident occurred while two (2) workers, including the one who was killed,…...

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Halon Cylinder is dropped and becomes projectile

In June 2008, a cylinder was dropped, and its top valve hit a concrete platform. The impact of the cylinder valve on the concrete caused the threads on the screw connection, which held the valve on the cylinder, to fail, resulting in complete separation of the valve from the cylinder. The cylinder’s internal pressure was…...

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Hot Water Heater catastrophically fails, killing two (2) workers

At 11:30 p.m. on March 19, 2009, Solus Industrial Innovations LLC employees from the third shift had just come to work. Their employer is a manufacturer of plastic conveyor parts. One employee (Employee #1) pointed out to the on-shift supervisor that there was a pool of water near an 80-gallon water heater that was being…...

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Compressed Air Receiver Catastrophic Failure

In May 2009, a compressed air tank failed, blowing the bottom off of the tank and sending fragments flying into a concrete wall, puncturing the wall. The investigation following the incidentrevealed several serious problems with the condition of the tank, including severe corrosion and rust at the bottom of the tank, where it failed, and…...

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GAS MAIN acts as a PROJECTILE during PRESSURE-TESTING

On March 3, 2010, a Peoples Gas worker died, and another was seriously injured after they were struck by a pipe while pressure-testing an underground gas main…. Membership Required You must be a member to access this content.View Membership LevelsAlready a member? Log in here...

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Relief valve system failure during unplanned CNG release

Summary On the days leading to January 6, 2014, unusual weather conditions with high-temperature variations caused a large pressure rise inside the three storage vessels at the Brookhaven National Laboratory (BNL) compressed natural gas (CNG) fueling facility. The pressure increase reached the point where the relief valve on each vessel opened automatically and released gas…...

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Line Break gone bad (pulling blind flange)

Worker Fatality During Attempted Removal of Blind Flange on Cell 14 Magnet Cooling Water System Summary On October 21, 2015, two National High Magnetic Field Laboratory (NHMFL) mechanical technicians were involved in an incident while attempting to remove a Victaulic blind flange from supply piping on a Magnet Cooling Water (MCW) System. The mechanical technicians…...

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How many worst-case release scenarios must be analyzed and documented in the RMP?

As a part of the hazard assessment requirements in 40 CFR Part 68, Subpart B, I must analyze worst-case release scenarios and document certain analyses in my risk management plan (RMP). How many worst-case release scenarios must be analyzed, and how many analyses must be specifically documented in the RMP?… Membership Required You must be...

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Differences between EPA’s RMP and EPCRA

How do the Clean Air Act (CAA) risk management program requirements differ from the hazardous chemical reporting requirements under the Emergency Planning and Community Right-to-Know Act (EPCRA)?… Membership Required You must be a member to access this content.View Membership LevelsAlready a member? Log in here...

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May be a bit out of spec for API 570

This is safety satire on a Friday afternoon after a long week! I may not be a Certified Welding Inspector (CWI) or a Visual Level II inspector certified per ASME V Supplemental NDE Certification requirements. Still, I believe API 570, Section 8 Repairs, Alterations, and Rerating of Piping Systems allows only a dozen or fewer…...

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Engineering & Code Review; What is it and Why do it?

I have spent much time with clients doing “Engineering and Code Reviews.”  These have been instrumental in avoiding many issues when it comes time for the INITIAL PHA. Depending on the process size and complexity, these can take 0.5 – 3 days, but that time is spent ensuring the primary containment systems and all the…...

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