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Risk assessment screening study for fire, explosion and toxicity effects of hydrocarbons stored in a sphere and bullet

Autorzy
Treść / Zawartość
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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
A fast and economical approach was used to assess impact of fires, explosions and toxicity for a LPG gas storage facility using Fire Explosion and Chemical (FEC) Indices, the TNT and TNO multi energy methods, which are part of a process hazard analysis study. The assessment identified high consequence events for radiation, toxicity and overpressure due to catastrophic rupture of spheres and bullets holding LPG. The FEC Indices indicated that further investigation was needed to determine the extent of blast overpressure whereas toxicity was not identified as a high consequence. The TNO method was used to assess overpressure for congested volumes and unconfined vapour cloud explosions for a bullet, whereas the TNT method was used to predict overpressure occurring on a sphere with no congestion. The FEC indices can be used to screen for high consequence events in order to save time and identify the level of risk complexity needed for process equipment, whereas the TNO method can be easily applied when determining safety distances from LPG facilities for various building constructions provided that the degree of congestion is known.
Twórcy
autor
  • Oman LNG Department of Process Safety Engineering P.O. Box 888 Sur, P.C.: 411, Oman
autor
  • Cracow University of Technology Institute of Automobiles and Internal Combustion Engines Jana Pawla II Av. 37, 31-864 Krakow, Poland tel.:+48 12 6283688, fax: +48 12 6283690
Bibliografia
  • [1] Abbasi, T., Abbasi, S.A., The boiling liquid expanding vapour explosion (BLEVE): Mechanism, consequence assessment, management, Journal of Hazardous Materials 141 pp. 489-519, 2007.
  • [2] Atkinson, G., Cusco, L., Painter, D., Tam, V., Interpretation of Overpressure Markers and Directional Indicators in Full-Scale Deflagrations and Detonations, Journal of Hazards XXI, IChemE Symposium Series No. 155, Crown Copyright, pp. 500-501, 2009.
  • [3] Behari, N, QRA for Hydrocarbon Storage Facilities, Master Thesis, University of Sheffield, 2005.
  • [4] Van den Berg, A. C., The multi-energy method: A framework for vapour cloud explosion blast prediction, Journal of Hazardous Materials, Vol. 12, Is. 1, pp. 1-10, 1985.
  • [5] Van den Bosch, C. J. H., Twilt, L., Damage caused by heat radiation in Methods for the determination of possible damage to people and objects resulting from releases of hazardous materials, Chapter 1 in a Green Book, CPR 16E, Ministry of Social Affairs and Employment First Edition, The Hague, 1992.
  • [6] Van den Bosch C. J. H. (ed.) and Weterings R. A. P. M. (ed.): Chapter 5 Vapour cloud explosion in Methods for the calculation of physical effects of the escape of dangerous material (liquids and gases), Yellow Book, CPE 14E, Ministry of Social Affairs and Employment, Third Edition, Second Revised Print, The Hague, 2005.
  • [7] Cozzani, V., Gubinelli, G., Antonioni, G., Spadoni, G., Zanelli, S., The assessment of risk caused by domino effect in quantitative area risk analysis, Journal of Hazardous Materials A127, pp. 14-30, 2005.
  • [8] Etowa, C., Amyotte, P., Pegg, M., Khan, F., Quantification of inherent safety aspects of the Dow indices, Journal of Loss Prevention in the Process Industries, 15, pp. 477-487, 2002.
  • [9] Gowland, R., A Progressive Risk Assessment Process For A Typical Chemical Company: How To Avoid The Rush to QRA, IChemE Symposium Series No. 153, European Process Safety Centre, U.K. 2007.
  • [10] Jiang, J., Liu, Z. G., Kim, A. K, Comparison of blast prediction models for vapor cloud explosion, Institute for Research in Construction, The Combustion Institute/Canada Section, Spring Technical Meeting, pp. 23.1-23.6, 2001.
  • [11] Lees, F. P., Loss Prevention in the Process Industries Volume 1, Third Edition, pp. 1399- 1401, 2005.
  • [12] Mohammad, J. J., Mohsen, Z., Mohammad, M., The Credit of Fire and Explosion Index for Risk Assessment of Iso-Max Unit in an Oil Refinery, Occupational Health Association (IOHA) IIJOH 4, pp. 10-16, 2012.
  • [13] Olechowski, A. (ed.), Piaścik, M. (ed.), LPG market in Poland in 2016, Annual Report, POGP, Warszawa 2017.
  • [14] Planas-Cuchi, E., Salla, J. M., Casal, J., Calculating overpressure from BLEVE explosions, Journal of Loss Prevention in the Process Industries, 17, pp. 431-436, 2004.
  • [15] Suardin, J., The Integration of Dow’s Fire and Explosion Index Into Process Design andOptimization To Achieve An Inherently Safer Design, , Masters Degree Thesis, Texas A&M University, pp. 21-47, 2005.
  • [16] A Summary of the Dow Chemical Company’s quick method to calculate toxic vapour dispersion, The Dow Chemical Company, New York 2006.
  • [17] DNV-GL, Process Hazard Analysis Safety Techniques, Phast Software, UK 2005.
  • [18] Gexcon, Handbook of Gas Explosion Chapter 7 Blast Waves, Accessed 27th of December 2015: http://www.gexcon.com/article/handbook-chapter-7.
  • [19] Guidelines for Chemical Process Quantitative Risk Assessment, American Institute of Chemical Engineers, Centre for Chemical Process Safety, Second Edition, ISBN 978-0-8169-0720-5, New York 2000.
  • [20] Sasol, (F&EI) and (CEI) Screening Assessment Tool, Rosebank, South Africa 2007.
  • [21] Sasol, Overpressure Screening Assessment Tool, Rosebank, South Africa 2007.
Uwagi
PL
Opracowanie ze środków MNiSW w ramach umowy 812/P-DUN/2016 na działalność upowszechniającą naukę (zadania 2017).
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-069054b0-048b-455e-a2a4-e7090f042f1d
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