Fire and Explosion Risk Assessment in a Combined Cycle Power Plant

Document Type : Research Article

Authors

1 Department of Occupational Health and Safety, School of Public Health and Safety, Shahid Beheshti University of Medical Sciences, Tehran, I.R. IRAN

2 School of Mechanical Engineering, Amir Kabir University of Technology, Tehran, I.R. IRAN

3 Crisis Management Research Center, Malek-e-Ashtar University of Technology, Tehran, I.R. IRAN

Abstract

Fire and explosion are the most prevalent accidents in chemical and process industries. Hence, identification of the hazard factors and the methods of controlling these two major accidents are very important in the process industries. In this paper, fire and explosion hazards of some process units at a combined cycle power plant have been estimated using the Dow fire and explosion index. The results of this study show that methane fueled turbine has the highest value of Dow index which is 321, turbine unit with gas oil and gas oil storage site have the Dow index values of 147.5 and 35.5 respectively. The loss control credit factor for methane fueled turbine unit was 0.36 and the Actual Maximum Probable Property Damage was 4.12 US million dollars. Maximum Probable Days Outage is estimated to be 50 days and finally, the loss due to unit pauses is calculated to be 3.03 US million dollars. In addition, the findings of the current study show that the gas oil storage unit suffers the highest amount of loss due to business interruption. The findings of the present study can be used for the improvement of inherent safety and can also be applied to estimate the losses due to fire and explosion.

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[1] Prugh RW. Life‐Safety Concerns in Chemical Plants, Process Saf Progr, 35(1):18-25 (2016).
[2] Klein JA, Vaughen BK, “Process Safety: Key Concepts and Practical Approaches”, CRC Press,  ‎Boca Raton (2017).
[3] Suardin J., Sam Mannan M., El-Halwagi M., The Integration of Dow's Fire and Explosion Index (F&EI) Into Process Design and Optimization to Achieve Inherently Safer Design, J. Loss Prevent Pro. Ind., 20(1):79-90 (2007).
[4] Babapoor A., Bab V., Ahamdi Sabegh M., A New Investigation on Tunnel Pool Fire Phenomenon Using CFD Technique, Iran. J. Chem. Chem. Eng. (IJCCE), 37(2): 171-182 (2018).
[5] Husin M.F., Hassim M.H., Ng D.K., Johari A., Kamaruddin M.J., Ngadi N., Guidelines for Process Safety Hazard Assessment Based on Process Information, Journal of Engineering and Technological Sciences (JESTEC), 50(2): 272-90 (2018).
[6] Jabbari M., Kavousi A., “Consequence Analysis of Flammable Chemical Releases from a pipeline”, Fourth International Joint Conference on Computational Sciences and Optimization, IEEE (2011).
[7] Mahoney D.G., “Large Property Damage Losses in the Hydrocarbon-Chemical Industries: A Thirty-Year Review”, M & M Protection Consultants (1997).
[8] Çetinyokuş S., Consequences Modeling of the Akçagaz Accident through Land Use Planning (LUP) Approach, Iran. J. Chem. Chem. Eng. (IJCCE), 37(4): 253-264 (2018).
[10] Zaranejad A., Ahmadi O., Fire and Explosion Risk Assessment in a Chemical Company by the Application of DOW Fire and Explosion Index, Journal of Occupational Health and Epidemiology (JOHE), 4(3): 163-75 (2015).
[11] Etowa C., Amyotte P., Pegg M., Khan F., Quantification of Inherent Safety Aspects of the Dow Indices, J Loss Prev Process Ind, 15(6): 477-87 (2002).
[12] Khan F.I., Sadiq R., Amyotte P.R., Evaluation of Available Indices for Inherently Safer Design Options, Process Saf. Progr., 22(2):83-97 (2003).
[14] Roy P.K., Bhatt A., Rajagopal C., Quantitative Risk Assessment for Accidental Release of Titanium Tetrachloride in a Titanium Sponge Production Plant, J. Hazard Mater., 102(2): 167-186 (2003).
[15] Bernatik A., Libisova M., Loss Prevention in Heavy Industry: Risk Assessment of Large Gasholders,
J Loss Prevent Proc Ind., 17(4): 271-278 (2004).
[17] Junjie F., Bing Z., Wei X., Bing S., Fan Z., Jie J., Development of Index System for Inherently Safer Process Design Using an Integrated Approach, Chin. J. Chem. Eng, Pre-proof (2019).
[18] Roshan S.A., Gharabagh M.J., Economic Consequence Analysis of Fire and Explosion in Petrochemical Feed and Product Pipelines Network, Health Scope, 2(2): 90-94 (2013).
[19] Jafari M.J., Zarei M., Movahhedi M., The Credit of Fire and Explosion Index for Risk Assessment of Iso-Max Unit in an Oil Refinery. Int. J. Occup. Hyg (IJOH), 4(1): 10-16 (2012).
[20] Ahmadi S., Adl J., Mirzaei M., Zarei M., Determination of Fire and Explosion Loss in a Chemical Industry by Fire and Explosion Index. J. Qazvin Univ. Med. Sci (JQUMS), 15(4): 68-76 (2012).
[21] Ahmadi S., Adl J., Varmazyar S., Risk Quantitative Determination of Fire and Explosion in a Process Unit By Dow’s Fire and Explosion Index, Iran Occupational Health Journal, 5(1): 39-46 (2008).
[22] Ibrahim T.K., Mohammed M.K., Awad O.I., Abdalla A.N., Basrawi F., Mohammed M.N., Najafi G., Mamat R., A Comprehensive Review on the Exergy Analysis of Combined Cycle Power Plants. Renew Sust Energ Rev. 90: 835-850 (2018).
[23] Zohuri B., McDaniel P., Gas Turbine Working Principals.,  “Combined Cycle Driven Efficiency
for Next Generation Nuclear Power Plants
”, Springer, Berlin (2018).
[24] Glauco E., Cinquegrani La., Rigoni L., System, Method and Apparatus for Minimizing Heat Loss in a Heat Recovery Steam Generator, Google Patents, (2019).
[25] Breeze P., “Power Generation Technologies”, Newnes, (2019).
[26] Alyah M., Ashman J., Arisoy A., Astley E., Herbst E., Jennings P., Gusev A., Emelyanov R., and Radevsky, R., Combined Cycle Power Plants. IMIA Annual Conference, Merida, Mexico, Sept (2015).
[27] Chemicals D., “Dow’s Fire & Explosion Index Hazard Classification Guide”, AIChE Technical Manual (1994).
[28] Jensen N., Jørgensen S.B., Taking Credit for Loss Control Measures in the Plant with the Likely Loss Fire and Explosion Index (LL-F&EI), Process Saf Environ, 85(1):51-8 (2007).
[32] Assael M.J, Kakosimos K.E, “Fires, Explosions, and Toxic Gas Dispersions: Effects Calculation and Risk Analysis”, CRC Press, Taylor & Francis Group, New York. (2010).
[33] Suardin J., Sam Mannan M., El-Halwagi M., The Integration of Dow's Fire and Explosion Index (F&EI) Into Process Design and Optimization to Achieve Inherently Safer Design, J Loss Prevent Proc Ind, 20(1): 79-90 (2007).