Process Safety Technical Areas

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...

The introduction of alternate fuel vehicles leads to new safety challenges. This is particularly relevant in the case of hydrogen vehicles, as flammable mixtures of hydrogen and air can be very dangerous. Potential hazard scenarios include gaseous or liquid hydrogen leaks, accumulation and ignition...

The use of dynamic modeling for relief system design can result in a considerable reduction in capital expenditure while simultaneously improving plant safety. This paper considers the application of dynamic analysis to two areas, vessel depressurization and flare network design, in order to...

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...

The best time to apply the principles of inherent safety is during the early stages of a design. In particular it is at the early stages that the ?Eliminate? option is best applied. For example, in the early stages of one design the process engineers had come up with a system of three knockout...

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...

Operator competency has been a major challenge for the petrochemical and refining industry for decades. In recent times, human factors are believed to be a consistent contributing cause for a lot of incidents. Current schemes used to determine an operator's competency are subjective and somewhat...

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...

Deflagration to detonation transitions (DDT) were previously observed in a set of large-scale unconfined vapor cloud explosion (VCE) tests involving ethylene-air mixtures in a moderately congested environment. The test rig congested region was 48 feet long by 12 wide by 6 feet high, with a regular...

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...