Abstract
Hydrogen is the next frontier and there is a concerted push to include hydrogen as an energy carrier. The main benefit is emissions reduction—eventually by 100 %. When used as a fuel, hydrogen supplies more energy per unit mass than the popular fuels used today. However, in the near term, there is a very significant cost differential between fossil fuels and hydrogen. Therefore, proposals have been made for the use of hydrogen as an additive to hydrocarbon fuels as a practical approach to the introduction of hydrogen in the energy mix. Enriched Methane (EM, a blend of hydrogen and natural gas) can presage a gradual transition to an eventual hydrogen economy. Besides the techno-commercial challenges for introducing hydrogen (or for that matter a hydrogen–methane blend), another key issue is that of the comparative safety between natural gas and hydrogen concerning the application, storage, transport, etc. Due to prior experience with, e.g. the process or petrochemical industries, it is well known that accidental releases of flammable substances are one of the largest contributors to the hazards of most industrial, domestic, and infrastructure facilities. Assessing the consequences and risks of such accidental releases is thus crucial. The consequences of a release such as cloud size and subsequent explosion like overpressure are dependent on several parameters such as fuel type, concentration, leak rate/direction, environmental conditions, cloud size, ignition location, and presence of any mitigation measures. More importantly, geometrical effects—including congestion and confinement, as well as layout of objects and walls—plays a key role in determining the magnitudes of gas cloud size (following a release) and overpressure/drag loads (following an explosion). Therefore, simple analysis techniques are generally not applicable as these may provide inaccurate results. 3D modelling based on Computational Fluid Dynamics (CFD) needs to be used. The current chapter describes the safety aspects of EM. In general, it can be expected that EM is relatively safer to handle (compared to hydrogen), thus significantly reducing the risk of fire and explosion. This chapter also seeks to evaluate whether EM may be safer than both hydrogen and methane under certain conditions. This is due to the fact EM combines the positive safety properties of hydrogen (strong buoyancy, high diffusivity) and methane (much lower flame speeds and narrower flammability limits as compared to hydrogen). Nonetheless, the explosion risk is by no means insignificant. The work is performed using the CFD software FLACS that has been well validated for safety studies of both natural gas/methane and hydrogen systems. Validation for EM–air explosions is also demonstrated. Practical systems such as vehicular tunnels, garages, etc., are used to demonstrate positive safety benefits of EM with comparisons to similar simulations for both hydrogen and methane.
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Abbreviations
- BFETS:
-
Blast and Fire Engineering for Topside Structures
- BLEVE:
-
Boiling Liquid Expanding Vapour Explosion
- CEA:
-
Commissariat à l’énergie atomique et aux énergies alternatives (English: Atomic Energy and Alternative Energies Commission)
- CFD:
-
Computational Fluid Dynamics
- CMR:
-
Christian Michelsen Research
- DDT:
-
Deflagration to Detonation Transition
- EN:
-
European Norm
- ER:
-
Equivalence Ratio
- EU:
-
European Union
- FhICT:
-
Fraunhofer Institute for Chemical Technology
- FLACS:
-
CFD tool for ventilation, dispersion, explosion, and fire modelling (by Gexcon)
- FZK:
-
Research Centre Karlsruhe (now KIT)
- HSE:
-
Health and Safety Executive
- HSL:
-
Health and Safety Laboratory
- EM:
-
Natural gas–hydrogen blend
- ISO:
-
International Standardisation Organisation
- KIT:
-
Karlsruhe Institute of Technology
- LFL:
-
Lower Flammability Limit
- LNG:
-
Liquefied Natural Gas
- LPG:
-
Liquefied Petroleum Gas
- PRD:
-
Pressure Relief Device
- QRA:
-
Quantitaitive Risk Assessment/Analysis
- TNO:
-
Nederlandse Organisatie voor Toegepast Natuurwetenschappelijk Onderzoek (English: Netherlands Organisation for Applied Scientific Research)
- TNT:
-
Tri-Nitro Toluene (Explosive)
- UFL:
-
Upper Flammability Limit
- ε:
-
Turbulent dissipation
- k:
-
Turbulent kinetic energy
- λ:
-
Detonation cell size
References
Bjerketvedt D, Bakke JR, van Wingerden K (1997) Gas explosion handbook. J Hazard Mat 52:1–150
Dobashi R, Kawamura S, Kuwana K, Nakayama Y (2011) Consequence analysis of blast wave from accidental gas explosions. Proc Comb Inst 33:2295–2301
Lobato J, Cañizares P, Rodrigo MA, Sáez C, Linares JJ (2006) A comparison of hydrogen cloud explosion models and the study of the vulnerability of the damage caused by an explosion of H2. Intl J Hyd Ener 31(12):1780–1790
Dorofeev SB (2007) Evaluation of safety distances related to unconfined hydrogen explosions. Intl J Hyd Ener 32:2118–2124
Ilbas M, Crayford AP, Yilmaz I, Bowen PJ, Syred N (2006) Laminar-burning velocities of hydrogen-air and hydrogen-methane-air mixtures: an experimental study. Intl J Hyd Ener 31:1768–1779
Di Sarli V, Di Benedetto A (2007) Laminar burning velocity of hydrogen-methane/air premixed flames. Intl J Hyd Ener 32:637–646
Gersen S, Anikin NB, Mokhov AV, Levinsky HB (2008) Ignition properties of methane/hydrogen mixtures in rapid compression machine. Int J Hydrogen Energy 33(7):1957–1964
Huang J, Bushe W K, Hill P G, et al. (2006) Experimental and kinetic study of shock initiated ignition in homogeneous methane-hydrogen-air mixtures at engine-relevant conditions. Int J Chem Kinet 38 221–233
El-Ghafour SAA, El-dein AHE, Aref AAR (2010) Combustion characteristics of natural as-hydrogen hybrid fuel turbulent diffusion flame. Intl J Hyd Ener 35(6):2556–2565
Yon S, Sautet JC (2012) Flame lift off height, velocity flow and mixing of EM in oxy-combustion in a burner with two separated jets. Appl Therm Eng 32(1):83–92
Eder A, F Pingten, Mayinger F (2001) Propagation of fast deflagrations and marginal detonations in hydrogen–air-additive mixtures. In: Proceedings of 18th international colloquium on the dynamics of explosions and reactive systems, Seattle, Washington, vol 181
Hansen OR, Middha P (2008) CFD-based risk assessment for hydrogen applications. Proc Saf Prog 27(1):29–34
Patankar SV (1980) Numerical heat transfer and fluid flow. Hemisphere Publishing, ISBN: 0070487405
Launder BE, Spalding DP (1974) The numerical computation of turbulent flows. Comp Meth Appl Mech Eng 3(2):269–289
Arntzen BJ (1998) Modelling of turbulence and combustion for simulation of gas explosions in complex geometries. Dr. Ing. Thesis, NTNU, Trondheim, Norway
Abdel-Gayed RG, Bradley D, Lawes M (1987) Turbulent burning velocities: a general correlation in terms of straining rates. Proc R Soc Lond A 414:389–413
Hansen OR, Storvik I, van Wingerden K (1999) Validation of CFD-models for gas explosions, FLACS is used as example. Model description, experiences and recommendations for model evaluation. Presented at the ‘European meeting on chemical Industry and Environment’, Krakow, Poland, pp 1–3
Johnson DM, Cleaver RP, Puttock JS, van Wingerden CJM (2002) Investigation of Gas Dispersion and Explosions in Offshore Modules, Offshore Technology Conference, Paper 14134. Houston, TX
Hansen OR, Gavelli F, Davis SG, Middha P (2011/2013) Equivalent cloud methods used for explosion risk and consequence studies, Mary Kay O’Connor process safety center 2011 international symposium, College Station, TX, USA, 25–27 October 2011. J Loss Prev Process Ind, 26(3), 511–527
Hansen OR, Renoult J, Bakke JR (2001) Explosion risk assessment: how the results vary with the approach chosen. fall symposium proceedings, Mary Kay O’ Connor Process Safety Centre, Department of Chemical Engineering, Texas A&M University, 3122 TAMU, College Station, TX 77843–3122, pp 395–410
Hansen OR, Gavelli F, Ichard M, Davis SG (2010) Validation of FLACS against experimental data sets from the model evaluation database for LNG vapour dispersion. J Loss Prev Process Ind 23:857–877
Catlin C, Gregory CAJ, Johnson DM, Walker DG (1993) Explosion mitigation in offshore modules by general area deluge, Trans. IChemE, 71, Part B
Hjertager BH, Bjørkhaug M, Fuhre K (1988) Gas explosion experiments in 1:33 scale and 1:5 scale; offshore separator and compressor modules using stoichiometric homogeneous fuel–air clouds. J Loss Prev Process Ind 1:197–205
Hjertager BH, Bjørkhaug M, Fuhre K (1988) Explosion propagation of non- homogeneous methane-air clouds inside an obstructed 50 m3 vented vessel. J Haz Mater 19:139–153
Mercx WPM (1996) Extended modelling and experimental research into gas explosions, CEC EMERGE project final summary report, EV5VCT930274 (TNO)
Selby C, Burgan B (1998) Blast and fire engineering for topside structures, phase 2, final summary report, SCI Publication 253, Steel Construction Institute, UK
Al-Hassan T, Johnson DM (1998) Gas explosions in large-scale offshore module geometries: overpressures, mitigation and repeatability, presented at OMAE-98. Lisbon, Portugal
Schneider H, Pförtner H (1983) PNP-Sichcrheitssofortprogramm, Prozebgasfreisetzung- Explosion in der gasfabrik und auswirkungen von Druckwellen auf das Containment
Sherman MP, Tieszen SR, Benedick WB (1989) FLAME facility, the effect of obstacles and transverse venting on flame acceleration and transition to detonation for hydrogen- air mixtures at large scale, Sandia National Laboratories, Albuquerque, NM 87185, NUREG/CR-5275, SAND85–1264, R3, USA
Shirvill LC, Royle M, Roberts TA (2007) Hydrogen releases ignited in a simulated vehicle refuelling environment. In: Proceeding of the 2nd international conference for hydrogen safety, San Sebastian, Spain, pp 11–13
Pförtner H, Schneider H (1984) Tests with jet ignition of partially confined hydrogen air mixtures in view of the scaling of the transition from deflagration to detonation. Final Report for Interatom GmbH, Bergisch Gladbach, Germany, (Fraunhofer ICT Internal Report)
Groethe M, Merilo E, Colton J, Chiba S, Sato Y, Iwabuchi H (2007) Large-scale hydrogen deflagrations and detonations. International Journal of Hydrogen Energy 32, 2125–2133
Lacome JM, Dagba Y, Jamois D, Perrette L Proust Ch. (2007). Large-scale hydrogen release in an isothermal confined area. In: 2nd International conference on hydrogen safety, 11–13 September 2007, San Sebastian, Spain
Gupta S, Brinster J, Studer E, Tkatschenko I (2007) Hydrogen related risks within a private garage: concentration measurements in a realistic full-scale experimental facility. In: Proceedings of the 2nd international conference on hydrogen safety, San Sebastian, Spain
Friedrich A, Grune J, Kotchourko N, Kotchourko A, Sempert K, Stern G, Kuznetsov M (2007) Experimental study of jet-formed hydrogen-air mixtures and pressure loads from their deflagrations in low confined surroundings. In: Proceedings of 2nd international conference on hydrogen safety, San Sebastian, Spain
Shirvill LC, Roberts PT, Roberts T A, Butler CJ Royle M (2006) Dispersion of hydrogen from high-pressure sources. In: Proceedings of hazards XIX conference. Manchester, UK, pp 27–30
Middha P, Hansen OR, Grune J, Kotchourko A (2010) CFD calculations of gas leak dispersion and subsequent gas explosions: validation against ignited impinging hydrogen jet experiments. J Hazard Mater 179:84–94
Houf WG, Evans GH, Merilo E, Groethe M, James SC (2012) Releases from hydrogen fuel-cell vehicles in tunnels. Intl J Hyd Ener 37(1):715–719
Houf WG, Evans GH, Ekoto IW, Merilo E, Groethe M (2013) Hydrogen fuel-cell forklift vehicle releases in enclosed spaces. Intl J Hyd Ener 38(19):8179–8189
Houf WG, Evans GH, Schefer RW, Merilo E, Groethe M (2011) A study of barrier walls for mitigation of unintended releases of hydrogen. Intl J Hyd Ener 36(3):2520–2529
Middha P (2010) Development, use and validation of the CFD tool FLACS for hydrogen safety studies. PhD Thesis, Institute of Physics and Technology, University of Bergen, Bergen, Norway
Royle M, Shirvill LC, Roberts TA (2007) Vapour cloud explosions from the ignition of methane/hydrogen/air mixtures in a congested region. In: Proceedings of 2nd international conference of hydrogen safety, San Sebastian, Spain, pp 11–13
Middha P, Engel D, Hansen OR (2011) Can the addition of hydrogen to natural gas reduce the explosion risk? Intl J Hyd Ener 36(3):2628–2636
Rosas C, Nayak S, Munoz F, Mannan MS (2011) Simulation and validation of methane and hydrogen mixtures explosion using CFD models. In: Mary Kay O´Connor process safety centre 2011 international symposium, College Station, TX, USA
Kang S-K, Bang H-J, Jo H-J (2013) Consequence analysis of hydrogen blended natural gas (HCNG) using 3D CFD Simulation. J Korean Inst Gas, 17(5)
Dan S-K, Moon D-J, Yoon E-S, Shin D-I (2013) Analysis of gas explosion consequence models for the explosion risk control in the new gas energy filling stations. Ind Eng Chem Res 52(22):7265–7273
Dan S-K, Park K-J, Kim T-O, Shin D-I (2011) Explosion simulations for the quantitative risk analysis of new energy filling stations. J Korean Institute Gas 15(1):60–67
Groethe M, Merilo E, Colton J, Chiba S, Sato Y, Iwabuchi H (2005) Large-scale hydrogen deflagrations and detonations. In: Proceedings of the 1st international conference on hydrogen safety, Pisa, Italy
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Middha, P. (2016). Explosion Risks of Hydrogen/Methane Blends. In: De Falco, M., Basile, A. (eds) Enriched Methane. Green Energy and Technology. Springer, Cham. https://doi.org/10.1007/978-3-319-22192-2_13
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DOI: https://doi.org/10.1007/978-3-319-22192-2_13
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