Major Hazards of Process Equipment Failures in the Chemical Process Industry

2015 ◽  
Vol 735 ◽  
pp. 75-79 ◽  
Author(s):  
N.E. Hussin ◽  
Anwar Johari ◽  
Kamarizan Kidam ◽  
Haslenda Hashim

Process equipment failures play significant roles in most accidents that occur and recur in the chemical process industry resulting in fire, explosion, and toxic release. In this study, 50 equipment-related accident investigation reports were used to analyze type and severity of incidents. The comprehensive accident report data were retrieved from U.S. Chemical Safety and Hazard Investigation Board (CSB) and U.S. National Transportation Safety Board (NTSB) accident databases with a mean year of 2005. Among the identified process equipment failures were piping systems (32%), storage tanks (20%), process vessels (16%), separation equipment (10%), reactors (8%), heat transfer equipment (8%), and others (6%). The analysis shows that 32% of the cases led to fire and explosion, followed by toxic release (26%), and explosion (22%) incidents. A total of 126 fatalities, 590 injuries, 260 exposures, four shelter-in-place, and 13 evacuations were reported. In most accident cases, fire, explosion, and/or toxic release incidents occur simultaneously. The synergy between major hazards results in catastrophic accidents with severe consequences in numbers of fatalities, injuries, exposures, shelter-in-place, and evacuations. To minimize the losses, plant and equipment should be designed and prepared for the worst-case scenario, not just adapting to any ‘applicable’ standards or guidance.

2015 ◽  
Vol 75 (6) ◽  
Author(s):  
Nor Afina Eidura Hussin ◽  
Kamarizan Kidam ◽  
Siti Suhaili Shahlan ◽  
Anwar Johari ◽  
Haslenda Hashim

Process equipment failures play significant roles in most accidents that occur and recur in the chemical process industry (CPI). In this study, 50 equipment comprehensive accident investigation reports, extracted from the U.S. Chemical Safety and Hazard Investigation Board (CSB) and U.S. National Transportation Safety Board (NTSB) were analyzed to generate lessons learned. Based on the analysis, the synergy between major hazards i.e. fire, explosion, and toxic release has resulted in catastrophic accidents in the CPI. The emphasis on procedural equipment failure prevention does not provide sufficient hierarchy of controls in the CPI. Balance and integrated accident prevention is required to solve human unreliability that often leads to improper problem-solving, inappropriate actions, and ill-timed responses. To minimize losses, facilities and equipment should be designed and prepared for the worst-case scenario. Moreover, occurrence and recurrence of the accidents could be prevented using inclusive and updated communication systems through cooperation between various governmental agencies, industry players, and the public to disseminate lessons learned and promote safety in the industry. 


2013 ◽  
Vol 321-324 ◽  
pp. 2456-2459
Author(s):  
Ming Liang Chen ◽  
Zhi Qiang Geng ◽  
Qun Xiong Zhu

The hazard of chemical process equipment consists of two parts: the inherent hazard of process equipment and the hazard from domino effect among equipments. The inherent hazard of equipment depends on the properties of the substance present in the equipment and the specific process conditions. The domino effect is responsibility for many most destructive accidents in the chemical process industry. However, domino effect is either not considered at all or is done with much less rigour than is warranted. A method was proposed to evaluate the hazard of chemical process equipment. The inherent hazard and the hazard from domino effect were considered in the method. The procedure for the domino effect analysis among equipments was presented to evaluate the hazard from the domino effect. The method was implemented in a case study. The results show that it can be used to select the process equipment which should be intensive monitored.


2015 ◽  
Vol 75 (6) ◽  
Author(s):  
N.E. Hussin ◽  
K. Kidam ◽  
Jihan J. Jalani ◽  
A. Johari ◽  
H. Hashim ◽  
...  

Recent accident analyses show that the accident rates in the chemical process industry (CPI) were still not decreasing. In the paper, the issues and challenges of risk reduction strategies were discussed. A case study using accident cases, extracted from the U.S. Chemical Safety and Hazard Investigation Board (CSB) database was conducted. The results of the accident analysis were discussed and then compared to previous analysis of the Failure Knowledge Database (FKD, Japan). The CSB analysis shows that the industry had moved from procedural risk reduction strategies to inherently safer and add-on engineered strategies. After 10years improvement, the industry was approaching towards more balanced safety management to prevent occurrence and recurrence of accidents with the emphasis on both management and engineering risk reduction strategies.  


2015 ◽  
Vol 75 (6) ◽  
Author(s):  
Jihan A. Jalani ◽  
Kamarizan Kidam ◽  
Siti Suhaili Shahlan ◽  
Hamidah Kamarden ◽  
Onn Hassan ◽  
...  

Accident rate in the chemical process industry (CPI) is high and causing loss of lives, massive property and environmental damage. Continuous improvement on accident knowledge and understanding is vital for process safety. Thus, an initiative to study the latest trends of accident was taken by analyzing 75 completed investigation reports of US Chemical Safety and Hazard Investigation Board (CSB) accident cases occurred in CPI from 1995 to 2011. The result of the analysis shows that the CPI accepted the concept of Prevention trough Design (PtD). However, 71% of accident cases are similar due to incorrect corrective action taken. 


Alloy Digest ◽  
2004 ◽  
Vol 53 (7) ◽  

Abstract ATI 425 was originally developed for hot-rolled armor plate to provide ballistic protection comparable to Ti-6Al-4V and has been evaluated against a variety of projectile threats for use as armor. While processing the alloy for armor plate applications, it was observed that the material exhibited very good hot workability, permitting a more lenient window of processing parameters than necessary for Ti-6Al-4V. Versatility then expanded, and applications now exist in the chemical process industry (CPI) and in the aerospace industry. This datasheet provides information on composition, physical properties, and tensile properties as well as fracture toughness and fatigue. It also includes information on corrosion resistance. Filing Code: TI-133. Producer or source: ATI Wah Chang, Allegheny Technologies. Originally published March 2004, revised July 2004.


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