Understand Hazard & Risk

The foundation of a risk-based approach which will allow an organization to use this information to allocate limited resources in the most effective manner.

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...

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...

Can Functional Testing Be Replaced by Inspection After Demands?

Mar 14, 2011
Hui Jin
Safety instrumented systems are used to reduce the risk of major accidents in the process industry. To claim a certain risk reduction from such systems, it is necessary to perform reliability analyses, within internationally accepted frameworks, such as the IEC 61511. The main factors that...

Effect of Physical Properties of Particulates on Fires and Dust Explosions

Mar 14, 2011
Konanur Manjunath
There has been a dramatic approach in the way we are implementing process safety guidelines and standards for combustible. This is particularly true for North America where there have been devastating dust explosions occurring for the last 10 years or so. Following this, OSHA has initiated NEP,...

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,...

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...

Ignition of Dust Layers by Mechanical Sparks

Mar 14, 2011
Kees Van Wingerden
Dust explosions represent a considerable safety risk in process industry. Statistical records of dust explosions show that 32.7 % of these explosions are initiated by mechanical sparks or hot surfaces due to mechanical friction [1]. Laboratory investigations however show that direct ignition of...

Inherently Safer Design – Not Only about Reducing Consequences!

Mar 14, 2011
Dennis C. Hendershot
Process risk is a function of both the likelihood of occurance of an incident, and of the consequences of the incident. There is a common perception that inherently safer design focuses solely on reducing or eliminating the consequences. However, inherently safer design can also focus on the...

Safety Studies for Reformatsky Chemistry In a Meso-Scale Continuous Process System

Mar 13, 2011
Gabriel Loh
The production of fine chemicals and pharmaceuticals has been traditionally achieved via batch processes. More recently, there has been interest in using multiscale (meso- and micro-) reactors for the production of these fine chemicals and pharmaceuticals. These efforts in process intensification...

Using LOPA for Sil Assignment: A Tale of Two Plants

Mar 13, 2011
Michael S. Schmidt
Two plants operated by the same company have ?identical? ammonium nitrate (AN) solution pump installations. Yet the LOPA teams concluded that the safety instrumented functions to protect those pumps needed different safety integrity levels (SILs). Despite the similarity of the installations, the...

Inherently Safer Reactor Design for Complex Reactions Based On Calorimetry Studies

Mar 13, 2011
Alba Lucia Pineda
A number of reactive processes of the agrochemical, fine-chemicals and pharmaceutical industries involve thermally unstable and/or toxic reactants, products or intermediates, for which the chemistry, thermochemistry and thermodynamic properties are barely known. They frequently employ multipurpose...

On the Potential of Mitigating Vapour Cloud Explosions Using Flame Inhibitors

Mar 13, 2011
Kees Van Wingerden
Very few measures are taken to mitigate the possible consequences of vapour cloud explosions. The main attention is given to prediction of the consequences, which is used to consider strengthening structurally or re-locate occupied buildings such as control rooms. However little is undertaken to...

Improvement of BLEVE Overpressure Method Using Historical Data

Mar 13, 2011
Fei Chen
The current CCPS/TNO's BLEVE (Boiling Liquid Expanding Vapor Explosion) overpressure methodology is derived from that published by Baker in 1975. This methodology assumes isentropic expansion work and uses Baker's graphical method and high-explosive correlation to calculate BLVE energy and...

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