Chemical Process Safety (PSM/RMP)

Management of Organizational Change (OSHA Letter to RAs)

March 31, 2009 MEMORANDUM FOR:     REGIONAL ADMINISTRATORS THROUGH:        DONALD G. SHALHOUB DEPUTY ASSISTANT SECRETARY   FROM:                RICHARD E. FAIRFAX, DIRECTOR DIRECTORATE OF ENFORCEMENT PROGRAMS  SUBJECT:          Management of Organizational Change This memorandum addresses the application of 29 CFR 1910.119 (l), Process Safety Management (PSM) – Management of Change (MOC), to […]

EPA Can Improve Implementation of the Risk Management Program for Airborne Chemical Releases (EPA OFFICE OF INSPECTOR GENERAL)

EPA can improve its program management and oversight to better assure that facilities covered by the Clean Air Act’s Risk Management Program submit or re-submit an RMP. EPA had not established national procedures for identifying covered facilities that had not submitted RMPs. For the 5 States reviewed, we identified 48 facilities in 3 States that

Not enough water is a bad thing and too much water is a bad thing in Anhydrous Ammonia Processes

This article is for ANYONE with anhydrous ammonia, regardless if you have 100 pounds or 100,000 pounds of ammonia and your primary means of containment is Carbon Steel. I have written numerous times about the Stress Corrosion Cracking (SCC) failure mode and shared numerous accidents and alerts regarding this failure mode. In this article, I

MAJOR CHEMICAL DISASTERS IN INDIA

MAJOR CHEMICAL DISASTERS IN INDIA   Origin of accident Year Date Location Products involved Number of Deaths Injured Evacuated Explosion (warehouse) 1992 29.04 New Delhi Chemicals 43 20   Fire at a chemical store 1994 13.11 New Delhi Toxiccloud (chemicals)   500   Leakage 1984 03.12 Bhopal* Methyl isocyanate 2800 50,000 200,000 Leakage 1989 05.05

National Board Inspection Code vs. API 510

This article discusses how a facility would need to get one of its coded pressure vessels repaired, altered, or re-rated. The article will cover pertinent code and jurisdiction requirements and the differences among the American Society of Mechanical Engineers (ASME) Code, the National Board Inspection Code (NBC), and American Petroleum Institute (API) requirements, as well

Process Hazards Analysis Techniques (Methodolgies, Resources, and Time)

A Process Hazard(s) Analysis is a thorough, orderly, and systematic approach for identifying, evaluating, and controlling the hazards of processes involving highly hazardous chemicals. The facility shall perform a process hazard analysis on all processes covered by EPA’s RMP rule and/or OSHA’s PSM standard. The process hazard analysis methodology selected must be appropriate to the

What chemicals require hydrostatic relief valves on piping?

While virtually any liquid trapped in a “blocked-in” section of pipe can cause a rupture due to thermal expansion, specific chemicals are strictly regulated by OSHA 1910.119 (PSM) and NFPA 30 because of their volatility or toxicity. The requirement for a hydrostatic relief valve (HRV) is generally triggered by the chemical’s physical state (liquefied under

BLEVE Hazad Zones

Immediate Lethal Zone — Fireball Radius Typical range: 160–820 ft Hazards: Used for: absolute exclusion zone. Severe Burn Zone — High Thermal Radiation Typical range: 820–1,300 ft Thermal radiation: ~12.5–37.5 kW/m² Effects: Used for: firefighter withdrawal line unless cooling operations are effective. Moderate Burn Zone — Pain/Blistering Typical range: 1,300–2,600 ft Thermal radiation: ~5–12.5 kW/m²

The roles of Visual Inspector & Examiner in B31.3 piping

To understand what certification is needed for the visual examination of welds under ASME B31.3, it is critical to distinguish between the two (2) distinct roles defined by the Code:1) the Examiner and2) the Inspector While in fact, B31.3 requires 100% visual examination of fabrication (341.4.1), the “certification” depends on which of these two roles

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