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Three (3) MUST DO with Excess Flow Valves (EFV)
These were found as I was doing a design spec for a new NH3 Supply Business.  These items are directly from the owner’s manual and were presented to the engineering firm after a “debate” on the reliance on Excess Flow Valve(s).  These are about the three best manufacturer’s rules for EFVs I have ever seen!  When so many companies are going weaker in their spec’s...
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TSD ERTF Resport
FLAMMABLE LIQUID (TDG) EMERGENCY RESPONSE CHART – A DISCIPLINED APPROACH
Our friends to the North have once again outdone themselves with an Emergency Response Task Force that developed two (2) new charts to aid in large scale-high hazard responses, such as a High-Hazard Flammable Trains (HHFT) incident.  You can read the entire DOCUMENT ( A MUST READ for ALL responders – ESPECIALLY OFFICERS who may fill the IC role during such an incident).  This document...
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Welding Inspectors and their documentation
We have discussed the requirements for welder certification and their documentation, pressure and leak testing and its documentation, but the one area that I have not covered yet is the documentation of the Welding Inspector(s).  As we have said, the certified (“coded”) welder makes the weld(s) and then BEFORE any testing, a certified welding inspector will perform an inspection of...
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NH3 seal leak
A shaft seal failure on a compressor in a refrigeration system released approximately 5lbs of ammonia (Technical Safety BC)
INCIDENT OVERVIEW An ammonia release resulted in the temporary shutdown of an ammonia plant in an industrial food processing facility. Ammonia refrigeration systems are designed to operate at 250 pounds per square inch gauge (Psig). The major components of the system like compressors, evaporators, liquid receivers, piping, and fittings, etc. are installed in a machinery room. The compressor sucks refrigerant...
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Intermittent compressor shaft seal leak resulted in multiple ammonia releases (Technical Safety BC)
DESCRIPTION Ammonia compressor seal failure   INCIDENT OVERVIEW An intermittent compressor shaft seal leak resulted in multiple ammonia releases which activated low level (<50 ppm) ammonia detector alarms. The premises were not evacuated as the release was contained in a well ventilated mechanical room and the detector did not initiate a high-level evacuation alarm. … HomeRead More...
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Black liquor pulp by-product released from ruptured SAE 304 stainless steel piping elbow (Erosion/Corrosion - Technical Safety BC)
DESCRIPTION Kraft paper pulping, strong black liquor was sprayed onto buildings and equipment.   INCIDENT OVERVIEW Erosion of a stainless steel pressure piping elbow located on top of a black liquor storage tank resulted in strong black liquor being sprayed onto buildings, equipment, and the and surrounding area.   INVESTIGATION CONCLUSIONS Black liquor is the by-product of the Kraft pulping...
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Main shaft seal compressor failure releases ammonia (Technical Safety BC)
DESCRIPTION Failure of the main shaft seal ( mechanical seal ) of compressor #2 released ammonia vapor from the refrigeration system into the machinery room. INCIDENT OVERVIEW There was an ammonia leak from the main shaft seal, isolated to compressor #2 in the machinery room. INVESTIGATION CONCLUSIONS … HomeRead More »
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Compressor valve packing failed to maintain a seal to prevent Ammonia saturated oil leak (Technical Safety BC)
Damage description: Compressor valve packing failed to maintain a seal to prevent fluid escape.   INCIDENT OVERVIEW Ammonia saturated oil leaked from the two-way valve packing of a compressor into the machine room. The ammonia gases escaped from the leaked oil and triggered the machine room ammonia detector. … HomeRead More »
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Crack in suction header pressure gauge line results in a NH3 leak (Technical Safety BC)
INCIDENT OVERVIEW A hairline crack formed in a suction header pressure gauge line resulting in a minor leakage of ammonia. INVESTIGATION CONCLUSIONS The suction header pressure gauge line in question was ¼ inch steel tubing which connected the ammonia suction header to the pressure gauge installed in front of the engineer’s control room so that engineer on watch can visually monitor the pressure in...
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Separation Distances in NFPA Codes and Standards (Final Report)
Have you ever wondered where all the “separation distances” we see in OSHA Standards, NFPA Codes, Fire Codes, etc. come from?  Who came up with them, what are they based on, etc.?  All legitimate questions and you are NOT alone!!   Many of these requirements have historical undocumented origins. Guidance, which may inform a sound technical basis for adjusting these distances,...
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Circuitizing your piping for maintenance/inspections (API 570/574)
Anyone who has attended one of my Process Safety training courses has heard me use the phrase “circuitizing your piping” when we discuss the mechanical integrity aspect for piping.  API 570 is our baseline RAGAGEP for our Piping Inspection Program, but API 574 is how these inspections will actually be conducted and this standard is chock full of great information and is a MUST READ...
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EPA EPCRA/CERCLA citations @ water treatment facility (157 pound Cl2 release & $21K)
Respondent is a municipality in the Commonwealth of Virginia. According to information provided to EPA, a release of chlorine gas, (CAS # 7782-50-5), occurred at the Facility on October 19, 2017, at approximately 11:40 a.m. due to a rupture of tubing connected to a chlorine tank in the chlorine room. On December 12, 2018, EPA representatives conducted an inspection of the Facility following the Release...
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