VENTED HYDROGEN-AIR DEFLAGRATION IN A SMALL ENCLOSED VOLUME

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VENTED HYDROGEN-AIR DEFLAGRATION IN A SMALL ENCLOSED VOLUME Rocourt, X. 1, Awamat, S. 1, Sochet, I. 1, Jallais, S. 2 1 Laboratoire PRISME, ENSI de Bourges, Univ. Orleans, UPRES EA 4229, 88 bd Lahitolle, 18000 Bourges, France 2 Air Liquide R&D, Les Loges-en-Josas, BP 126, 78354, Jouy-en-Josas, France 5 TH INTERNATIONAL CONFERENCE ON HYDROGEN SAFETY SEPTEMBER 9-11, 2013 - BRUSSELS - BELGIUM

Context Objectives Problem: Reduce green house gases, pollution and dependency on oil-based fuels Solution: Hydrogen, clean energy carrier (fuel cell) Risk: H 2 leak could fill a small confined volume in a part of a system and could ignite. Few studies at small scale: - McCann (1985), CH 4 /air, V=5.8 dm 3 and 54.9 dm 3 2 Objectives of the study - Sato (2010), C 3 H 8 /air, V=4 dm 3 Vented deflagration in a small confined volume (V=3.4 dm 3 ) with a stoechiometric H 2 /air mixture Evaluate models of literature for vented deflagrations at small scale

Contents Experimental setup Experimental results Molkov correlation Bauwens model Comparison between models 3 Conclusions

Experimental setup Valve Gas outlet 2.5 cm 15 cm Rods 15 cm Gas inlet 15 cm 7.5 cm V=3375 cm 3 4 Walls: Plexiglas H 2 /air, φ=1, regulated by mass flow controllers Ignition by spark: E n =122 mj Pressure transducers PCB Piezotronics (±1.3%) High speed camera Phantom at 15000 fps

Experimental setup Front wall with vent 15cm Rods Enclosure with a back wall ignition Enclosure Enclosure with a with a front center ignition wall ignition 1.2cm 0.8cm 4cm 4cm Pressure transducers 5 3 ignition locations: center back wall front wall 5 centered square vent areas: 225 cm 2, 81 cm 2, 49 cm 2, 25 cm 2 and 9 cm 2 Vent cover: thin polyethylene film

Experimental results Several pressure peaks (Cooper et al. 1986 with a 760 dm 3 cubic vessel): P v : Relief pressure P v P 1 P 1 : Pressure generated by external explosion P 2 P 2 : Pressure generated by internal combustion (flame-accoustic coupling) P 1 or P 2 dominates the internal pressure 6 H 2 /air, φ=1, center ignition, raw signal (black) and filtered signal (1.5 khz low pass filter - blue)

Vent area (cm 2 ) Experimental results Front Center ignition Back wall ignition wall K v ignition P 1 (kpa) P 2 (kpa) P 1 (kpa) P 2 (kpa) P 2 (kpa) 225 1 3.1-5.0-1.3 81 2.8 11.0 2.5 25.0-2.5 49 4.6 13.0 10.0 27.8-6.6 25 9-78.9-61.5 40.0 9 25-278.4-180.8 196.4 7 For P 1 was K v included 4.6 maximal in P 2 overpressures which dominates generated for Kv by 9 external combustion (center and back wall ignition) and back wall ignition P 2 was not noticed for center ignition (K v =1) and back wall ignition (K v 4.6) 2 For K v 9: 3 V Front - maximal wall ignition: overpressures no pressure generated peak by P 1 internal combustion K v = and by center ignition Av Maximal overpressure with K v V Volume (m 3 ) A v Vent area (m 2 )

Models of the literature Actuel standard to predict internal overpressure during venting explosion: NFPA 68 and EN 14994 (2007) based on Bartknecht s equation (1993). Limitations: 10 kpa < P max < 200 kpa initial pressure < 20 kpa static vent activation pressure < 50 kpa 8 deflagration index K G < 55 MPa.m/s

Models of the literature Models to answer these limitations: Molkov (1995) Correlation Vent area Enclosure volume Sound velocity Burning velocity Specific heat Products expansion ratio Bradley number Empirical coefficients Turbulent Bradley number Deflagration Outflow Interaction P max Bauwens (2010) 9 Physic based model Vent area Enclosure lenghts Discharge coefficient Sound velocity Burning velocity Lewis number Specific heat Products expansion ratio Universal gas constant Gases temperature Molar mass Flame wrinkling coefficient External cloud radius Flame area=f(ignition location) P 1, P 2 Flame acceleration at the exit External p max

Molkov 1999 Correlation of Molkov proposed in 1995, and updated several times 1999, 2001, 2008, 2013 Correlations applied with our experimental setup configurations Ignition Location Absolute average deviations for all vent areas (%) Molkov 1999 Molkov 2001 Molkov 2008 Molkov 2013 Center 27 60 93 142 Back wall 42 92 66 70 Front Wall 133 185 361 434 10 Molkov 1999 correlates better than other updated versions with small scale experimental results Molkov 1999 has been chosen to be compared to Bauwens model

Molkov 1999 Molkov Center ignition Back wall ignition Front wall ignition A V (cm 2 K ) v (1999) Measured Dev. Measured Dev. Measured Dev. P max (kpa) P max (kpa) (%) P max (kpa) (%) P max (kpa) (%) 225 1 2 3.1-35.5 5-60 1.3 53.9 81 2.8 9 11-18.2 25-64 2.5 260 49 4.6 22 13 69.2 27.8-20.1 6.6 233.3 25 9 71 78.9-10 61.5 15.5 40 77.5 9 25 274 278.4-1.6 180.8 51.6 196.4 39.5 Correlation rather consistent with center ignition Overestimation for front wall ignition 11 Not conservative for center and back wall ignition

Bauwens model Assumptions for Bauwens model: P 2 asymptotically approaches a constant volume explosion pressure P cv = 811.7 kpa when Av 0m 2 (Bauwens 2012) Initial flame velocity=laminar flame velocity S L =2.14 m.s -1 (Le 0.9 for stoechiometric H 2 /air mixture S u0 =0.9L e -1 S L ) Bauwens model: vented gas composed of 90% of products and 10% of reactants 100% products considered in the present study New fitting value of k T =9.26 m -1 (for P 1 ) based on Bauwens (2010, 2011) and Chao (2011) experiments with a linear law. 12 Flame wrinkling factor Ξ A =1 (for P 2 ) to avoid higher overpressures generated at large scale (S u =Ξ A S L )

A V (cm 2 ) Bauwens model P 1 Center ignition Back wall ignition P K 1 (kpa) P 1 (kpa) v Measured Bauwens Deviation Measured Bauwens Deviation (%) (%) 225 1 3.1 4.9 58.1 5.0 8.6 72.0 81 2.8 11.0 7.1-35.5 25.0 19.9-20.4 49 4.6 13.0 8.3-36.1 27.8 31.6 13.7 25 9-10.1 - - 66.3-9 25-13.6 - - 269.3 - Deviations varying from -36% to 58% for center ignition 13 Deviations varying from -20% to 72% for back wall ignition Not conservative for some configurations

Bauwens model P 2 A V P (cm 2 K 2 (kpa) P 2 (kpa) P 2 (kpa) ) v Dev. Dev. Dev. Measured Bauwens Measured Bauwens Measured Bauwens (%) (%) (%) Center ignition Back wall ignition Front wall ignition 225 1-0.6 - - 0.4-1.3 0.6-53.9 81 2.8 2.5 5.6 124-3.8-2.5 4.4 76 49 4.6 10 15.7 57-10.8-6.6 11.8 78.8 25 9 78.9 58.8-26 61.5 41.6-32.4 40 43.4 8.5 9 25 278.4 295.9 6 180.8 235 30 196.4 237.5 20.9 Model more accurate for small vent areas K v 9 14 Not conservative for some configurations

Comparison between models - P max 15 P max modeled is compared to P max measured ( P 1 or P 2 ) Ignition Location Absolute average deviations for all vent areas (%) Molkov 1999 P max Bauwens Center 27 26 Back wall 42 33 Front Wall 133 48 Bauwens model is globaly more accurate than Molkov 1999 Results of both models are close for center and back wall ignition Molkov 1999 overpredicts pressure for front wall ignition but is conservative for this location

Comparison between models - P max Consideration of ignition location given P max for each vent areas Absolute average deviations for all vent areas (%) Ignition Location Molkov 1999 P max Bauwens Locations for P max 31 26 The critical case is only considered for each vent area Both models give similars results 16 Bauwens model for K v 4.6 Molkov model for K v > 4.6

Conclusions Experimental results Influence of the vent area and the ignition location on the internal overpressure for a small confined volume (H 2 /air, Φ= 1, V = 3375 cm 3 ) 3 pressures peaks: vent failure pressure, external combustion, internal combustion with flame-acoustic interaction P max obtained with center ignition for K v 9 and back wall ignition for K v 4.6 P 2 is dominant for small vent areas (K v 9) Molkov 1999 correlation and Bauwens model 17 Approximately similar results when comparing with experimental maximal overpressures (either P 1 or P 2 ) for center and back wall ignition Models results close to experimental data (Bauwens 26%, Molkov 31%) for a safe approach.

Thanks for your attention 18 Any questions?