NFPA’s 2 – Hydrogen Std and pipe labeling
Occasionally, we see some pipe labeling requirements that exceed those found in ASME A13.1. NFPA 2, 2023 has a few: (emphasis by me)
Occasionally, we see some pipe labeling requirements that exceed those found in ASME A13.1. NFPA 2, 2023 has a few: (emphasis by me)
It is good that we are finding fewer and fewer facilities without pressure testing and leak testing records on their process piping. But now comes the difficult question: Is pressure and leak testing required after maintenance or alterations on piping systems? So, most companies will have their newly installed piping pressure tested and leak tested
Ammonia is held for sale by a retailer in a large storage tank. The retailer sells ammonia as an agricultural fertilizer and a coolant for air conditioning systems. Section 311(e)(5) of EPCRA exempts from the definition of a hazardous chemical “(a)ny substance to the extent it is used in routine agricultural operations or is
The Department of Homeland Security’s Chemical Facility Anti-Terrorism Standards (CFATS) impose comprehensive federal security regulations for high-risk chemical facilities. Do the CFATS alter the requirements that apply to a facility covered under both CFATS and either the Emergency Planning and Community Right-to-Know Act (EPCRA) or the Clean Air Act §112(r) (i.e., the Risk Management Program
The current list of delegated states and counties is: NOTE: Kentucky, Puerto Rico, and the Virgin Islands no longer implement the program, and the regional office has taken over the implementation of those areas.
During a recent design review, we encountered some questionable “normal breathing” designs. I have always used the simplest of tests to ensure the tank has ADEQUATE venting during filling and emptying. Although OSHA allows the designer to use API 2000 (1968) or “other accepted standards,” the simplest test is that the VENTING capability MUST be
“We were doing some cleaning at the end of yesterday. I boiled some water in the HLT to pump through the heat exchanger. At the end of the day, there were 40-50 gal left in our 3bbl HLT. I turned off the heat and went home for the night. The next morning, I came into
An ISO container, partly filled with Monoethylene Glycol (MEG), imploded on the back deck of a ship, spilling around two cubic meters (528 gallons) of MEG onto the deck and to sea and causing unrepairable damage to the tank itself. There were no injuries. The tank was a 26-cubic-meter tank containing ten cubic meters (6600
The following incident is a precautionary example of the potential hazards of improperly depressurizing piping to remove a hydrate. During production operations, a control room operator observed a decrease in gas lift pressure supplied through a pipeline to a remote well location. The control room operator notified the onboard platform operators of the pressure drop
The Emergency Planning and Community Right-to-Know Act (EPCRA) requires businesses that store and/or manufacture, process, or use certain chemicals to complete the Tier II (EPCRA 311 and 312) Report and/or the Toxics Release Inventory (EPCRA 313) Report, also called the Form R. Section 112(r) of the Clean Air Act focuses on risk management for accident
I have written many articles discussing evacuating hazardous materials from a piping system. Over my career, I learned that using an open-top container can have disastrous results. It may sound silly or petty, but when something fails in the tasks and the hazardous material erupts from the open-top container, making contact with the worker(s), you
Two people were severely injured after a Nitrogen cylinder catastrophically failed during refilling/pressurization. Person 1 shut off the air and nitrogen gas supplies before yelling to the workshop to call the HSE leader (nurse). Person 2, who was holding the cylinder, suffered severe injuries to his legs and one hand. Person 3 was injured when