Process Safety Technical Areas

LOPA – Validating Human IPLs and Ies

Mar 14, 2011
Bill Bridges
Layer of Protection Analysis (LOPA) is a simplified risk assessment method that provides an order of magnitude estimate of the risk of a potential accident scenario. Humans can be the cause on an accident scenario (the Initiating Event [IE]) or human can serve as an independent protection layer (...

Using the HAZOP Study and LOPA to Generate Ideas for Inherently Safer Designs

Mar 14, 2011
Steven T. Maher
Fundamental changes in a chemical process are most cost-effective at early stages of a design, and specific Inherently Safer Design evaluations are frequently performed at these early stages to identify fundamental improvements that can signicantly decrease the magnitude of the consequences...

The Buncefield Explosion: Were the Resulting Overpressures Really Unforeseeable?

Mar 14, 2011
Jérôme R. Taveau
On Sunday 11 December 2005, a severe unconfined vapour cloud explosion followed by several tank fires occurred at the Buncefield oil storage depot in England, causing widespread damage to homes and businesses surrounding the site, hopefully without any victim. The damage caused by the resulting...

It's People, Stupid! Human Factors In Incident Investigation

Mar 14, 2011
Mike Broadribb
People have inherent strengths and weaknesses which can affect their performance. Issues such as fatigue, emotional stress, and motivation can adversely affect performance. Their performance is also influenced by factors external to the individual, such as poor equipment design, inadequate training...

A Key Factor In Hazardous Processes: Safety Culture

Mar 14, 2011
Charles A. Soczek
The significance of Safety Culture is becoming increasingly recognized as a key factor to achieve the safe operation of hazardous processes. This paper describes the four stages that manufacturing companies go through in their journey to a world class safety culture and applies this concept to...

An Analysis of CSB Investigation Reports for Inherent Safety Learnings

Mar 14, 2011
Paul R. Amyotte
The Chemical Safety and Hazard Investigation Board (CSB) is an independent, nonregulatory federal organization in the United States dedicated to investigating serious accidents in the chemical industry. Accidents are investigated by a team of CSB employees and from the evidence collected a list of...

Best Practice for An Evergreening Pressure Relief Systems Management Program

Mar 14, 2011
Nitin Talreja
Most oil and gas refining and petrochemical organizations have a Process Safety Management (PSM) program that stems from the requirements outlined under OSHA's 29 CFR 1910.119. Some have a very extensive program that covers most of the 14 elements of PSM and is managed via an integrated platform...

Inherently Safer Acids - A Case Study on the Application of Polyelectrolytes

Mar 14, 2011
Elliot M. Wolf
Strong acids, such as aqueous hydrochloric acid, are commonly used in the chemical process industry to purify streams or remove particulates from raw material, product, and waste streams. The benefits of HCl are its' low cost, large dissociation constant, and stability over time. However, the...

Implementation of PSM In Capital Projects

Mar 14, 2011
Charles A. Soczek
It is critical to embed Process Safety Management in the capital project system to help achieve a safe start-up. This is the foundation for assuring safe operations throughout the life of the process, especially in the construction of facilities for high process hazards. Today's PSM system,...

Methods for Precluding the Existence of a Dust-Explosion Hazard

Mar 14, 2011
Richard Prugh
The "generic" standard for preventing fires and explosions involving combustible dusts is the National Fire Protection Association publication NFPA 654. In this document, fifteen of the requirements are prefaced with the phrase "if an explosion hazard exists", and an additional four requirements...

Making Existing Process Plants Inherently Safer

Mar 14, 2011
Victor H. Edwards
Making process plants inherently safer has obvious advantages and is easiest to do when designing a new plant. Modification of existing plants to make them inherently safer can often be much more difficult and costly, including any costs due to lost production. However, an inherently safer design...

Secondary Dust Explosions: How to Prevent Them or Mitigate Their Effects?

Mar 14, 2011
Jérôme R. Taveau
Dust explosions are frequent and particularly devastating in the process industries, and secondary dust explosions are the most severe ones. A secondary dust explosion can occur when the blast wave from a primary explosion entrains dust layers present in the plant, creating a large dust-air...

Analysis of Independent Protection Layers Used In Three Typical Chemical Processes

Mar 14, 2011
Herb W. H. Meyer
Independent protection layers (IPLs) used to mitigate most severe consequences are analyzed for three chemical processes: Olefins, Low-density Polyethylene, and an intermediates chemical plant. The IPLs are categorized by type (i.e., interlocks, PSVs, independent alarms, etc.), by function (...

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