Ingenieur Vol 68 Oct-Dec 2016 | Page 76

INGENIEUR storage tank resulting in an escape of unleaded petrol and the formation of a cloud of flammable vapour that ignited. The causes which were uncovered during the investigation highlighted the failure of multiple levels of protection due to: ●● inappropriate procedures in testing and operation, ●● failure to pass critical design knowledge down the supply chain of safety systems, ●● lapses in maintenance and fault reporting, and ●● poor interface design. The initial failures leading to the accident were a combination of a stressful working environment, and undocumented filling and handover procedures. Similar to the Bhopal accident, it was shown here that major accidents often result from interaction among components – caused by the occurrence of a variety of flaws and deficiencies, together forming a ‘bedding’ for the accident to happen [7]. The accidents which have been discussed have to be linked with changes driven by competition, cost pressure, management methods and human behaviour. The complexity of the process installations and technologies are observable but are not dominant in causing the accidents [7]. The accidents can be linked to; ●● poor management, ●● weak competency, ●● extreme operating conditions, ●● focus only on reducing cost and saving time, but at the same time loss of knowledge and expertise, ●● complex safeguarding and control systems, and ●● slipping maintenance and unclear responsibilities, All these produced conditions in which risk awareness slowly declined. It can be seen that due to such scenarios which can be linked to the complex causation mechanism, process safety incidents will still happen. Process Safety Management Operations supported by multiple layers of protection may result in increased security for employees, the public and increased profits. It is 6 74 VOL - DECEMBER 2016 VOL68 55OCTOBER JUNE 2013 important though to acknowledge that not all the layers totally cov er the entire potential risk. Each of the layers has its own weaknesses as previously mentioned e.g. complex control systems, slipping maintenance, low reliability of safeguards etc. However, together, the whole suite of layers offers a thick blanket of protection. Nonetheless it is not enough to have these layers of protection and to design systems to reduce the risks. It is also important to consider how these layers of protection and consequent chemical process safety, can be managed. The promulgation of 29 CFR 1910.119 Pro c e s s S afe t y M anagement (P SM) of Highly Hazardous Chemicals Standards by Occupational Safety and Health (OSHA) US applies the principles of management systems to the safety of chemical processes [8]. The bulk of PSM Standards contains general requirements which are performance based and not site - specific. The PSM standard emphasises the management of hazards through a comprehensive programme that integrates technologies, procedures, and management practices. The standard has 14 elements that are fundamental to running a safe chemical operation. These include procedures to; ●● ensure employee participation, ●● train employees and contractors, ●● ensure mechanical integrity of equipment, ●● manage change procedures, ●● investigate incidents, ●● plan for and respond to emergencies, ●● audit for compliance. Requirements to establish the PSM on-site include information on the chemicals, equipment and technology of the process, hazard analysis, written operating procedures for the facility, and detailed documentation of data collected to assure for mechanical integrity. The challenge with PSM is that it is not an easy standard to understand or implement. But as processes become more complex and the number of operational conditions to be controlled becomes more overwhelming, the PSM standards offer a systematic and structured approach to identification, prevention, and mitigation of risks associated with hazardous chemicals to ensure safe operation.