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An experimental study of flame acceleration and deflagration to detonation transition in representative process piping
Authors:Geraint Thomas  Gwyn Oakley  Richard Bambrey
Institution:1. Combustion Hazard Research DDTExperts, PO Box 217, Aberystwyth SY23 3XT, UK;2. Aber Shock and Detonation Research Limited, Maes-y-Deri, Rhydlewis, Llandysul, Ceredigion SA44 5RE, UK;1. Chongqing Key Laboratory of Fire and Explosion Safety, Logistical Engineering University, Chongqing 401311, China;2. School of College of Power Engineering, Chongqing University, Chongqing 400030, China;1. School of Civil Engineering, Hefei University of Technology, Hefei 230009, Anhui, China;2. Warwick FIRE, School of Engineering, University of Warwick, Coventry CV4 7AL, United Kingdom;3. Tianjin Fire Research Institute, Tianjin 300381, China;1. CAS Key Laboratory of Mechanical Behavior and Design of Materials (LMBD), University of Science and Technology of China, Hefei 230026, Anhui, PR China;2. State Key Laboratory of Fire Science, University of Science and Technology of China, Hefei 230026, Anhui, PR China
Abstract:The paper summarizes the results of experimental tests and accompanying analyses to investigate the factors that govern flame acceleration and potential transition to detonation in a relatively long unobstructed piping system. The overall aim of the work was to obtain sufficient experimental data so as to be able to develop and evaluate methodologies for classifying and predicting potential detonation flame acceleration and deflagration to detonation transition (DDT) hazard in industrial process pipes and mixtures. The present results show that the flame acceleration process in an unobstructed pipe exhibit three distinct phases: an initial establishment phase; a second rapid acceleration phase and a final transition to detonation phase. Test results with ethylene indicate that the acceleration process is not sensitive to initial pressure (all other parameters remaining constant) but can be sensitivity to initial pipe wall temperature or possibly mixture humidity. The presence of bends increases the local rate of turbulent combustion, an effect attributed to the additional turbulence generated downstream of the bend. For straight pipes, detonation was only observed to develop for hydrogen–air and ethylene–air mixtures. Detonation was not observed with methane, propane or acetone as fuel in the present piping apparatus.
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