V. Shentsov, M. Kuznetsov, V. Molkov

Slides:



Advertisements
Similar presentations
Modeling Wing Tank Flammability Dhaval D. Dadia Dr. Tobias Rossmann Rutgers, The State University of New Jersey Piscataway, New Jersey Steven Summer Federal.
Advertisements

Flammable extent of hydrogen jets close to surfaces Benjamin Angers*, Ahmed Hourri*, Luis Fernando Gomez, Pierre Bénard and Andrei Tchouvelev** * Hydrogen.
1 Validation of CFD Calculations Against Impinging Jet Experiments Prankul Middha and Olav R. Hansen, GexCon, Norway Joachim Grune, ProScience, Karlsruhe,
DISPERSION TESTS ON CONCENTRATION AND ITS FLUCTUATIONS FOR 40MPa PRESSURIZED HYDROGEN A. Kouchi, K. Okabayashi, K. Takeno, K. Chitose Mitsubishi Heavy.
ICHS 2007, San Sebastian, Spain 1 SAFETY OF LABORATORIES FOR NEW HYDROGEN TECHNIQUES Heitsch, M., Baraldi, D., Moretto, P., Wilkening, H. Institute for.
Experimental Investigation of Hydrogen Release and Ignition from Fuel Cell Powered Forklifts in Enclosed Spaces Isaac W. Ekoto, William G. Houf, and Greg.
CFD Modeling for Helium Releases in a Private Garage without Forced Ventilation Papanikolaou E. A. Venetsanos A. G. NCSR "DEMOKRITOS" Institute of Nuclear.
0 Copyright; 2007 IAE. All rights reserved. 2nd ICHS 11-13/9/2007 Spain Study of Hydrogen Diffusion and Deflagration in a Closed System Yuki Ishimoto 1,
Volkmar Schröder BAM, D Berlin Folie 1 International Conference on Hydrogen Safety, Pisa, September 8-10, 2005 Explosion Characteristics of Hydrogen-Air.
Natural and Forced Ventilation of Buoyant Gas Released in a Full-Scale Garage : Comparison of Model Predictions and Experimental Data Kuldeep Prasad, William.
Funded by FCH JU (Grant agreement No ) 1 © HyFacts Project 2012/13 CONFIDENTIAL – NOT FOR PUBLIC USE.
Pro-Science 4 th International Conference of Hydrogen Safety, September 12-14, 2011, SAN FRANCISCO, USA EXPERIMENTAL STUDY OF IGNITED UNSTEADY HYDROGEN.
MODEL-BASED DETERMINATION OF HYDROGEN SYSTEM EMISSIONS OF MOTOR VEHICLES USING CLIMATE- CHAMBER TEST FACILITIES Dr. Martin Weilenmann.
ICHS4, San Francisco, September E. Papanikolaou, D. Baraldi Joint Research Centre - Institute for Energy and Transport
Research Activities of HFCV in Korea May 26 ~ 29, th HFCV-SGS Meeting Ministry of Land, Transport and Maritime Affairs, Korea Transportation Safety.
Large-Scale Hydrogen Release In An Isothermal Confined Area J.M. LACOME – Y. DAGBA – D. JAMOIS – L. PERRETTE- C. PROUST ICHS- San Sebastian, sept 2007.
Page 1 SIMULATIONS OF HYDROGEN RELEASES FROM STORAGE TANKS: DISPERSION AND CONSEQUENCES OF IGNITION By Benjamin Angers 1, Ahmed Hourri 1 and Pierre Bénard.
Mitglied der Helmholtz-Gemeinschaft Simulation of the efficiency of hydrogen recombiners as safety devices Ernst-Arndt Reinecke, Stephan Kelm, Wilfried.
Funded by FCH JU (Grant agreement No ) 1 © HyFacts Project 2012/13 CONFIDENTIAL – NOT FOR PUBLIC USE 1.
DEVELOPING FIRE TESTS FOR FCV AND HYDROGEN VEHICLES Glenn Scheffler Consultant for the US Department of Energy August 2010 DEVELOPING FIRE TESTS FOR FCV.
Outline Background Explosion Phenomena Experiments Correlation Conclusion/Summary Questions.
Second International Conference on Hydrogen Safety, San Sebastian, Spain, September 2007 CFD for Regulations, Codes and Standards A.G. Venetsanos.
Preparing for the Hydrogen Economy by Using the Existing Natural Gas System as a Catalyst // Project Contract No.: SES6/CT/2004/ NATURALHY is an.
IESVic 1 QUANTITATIVE IMAGING OF MULTI-COMPONENT TURBULENT JETS Arash Ash Supervisors: Dr. Djilali Dr. Oshkai Institute for Integrated Energy Systems University.
Experimental and numerical studies on the bonfire test of high- pressure hydrogen storage vessels Prof. Jinyang Zheng Institute of Process Equipment, Zhejiang.
HIGH PRESSURE HYDROGEN JETS IN THE PRESENCE OF A SURFACE P. Bénard, A. Tchouvelev, A. Hourri, Z. Chen and B. Angers.
Detection of Hydrogen Released in a Full-scale Residential Garage Thomas Cleary & Erik Johnsson Fire Research Division Engineering Laboratory National.
Preparing for the Hydrogen Economy by Using the Existing Natural Gas System as a Catalyst // Project Contract No.: SES6/CT/2004/ NATURALHY is an.
Pressure Relief Devices: Calculation of Flammable Envelope and Flame Length Vladimir Molkov Hydrogen Safety Engineering and Research Centre
Sandra Nilsen et. al Determination of Hazardous Zones Case study: Generic Hydrogen Refuelling Station.
MULTI-COMPONENT FUEL VAPORIZATION IN A SIMULATED AIRCRAFT FUEL TANK C. E. Polymeropoulos Department of Mechanical and Aerospace Engineering, Rutgers University.
Engineering Safety in Hydrogen-Energy Applications
Consequence Analysis 1.2.
S.G. Giannissi1,2, I.C.Tolias1,2, A.G. Venetsanos1
ICHS 2015 – Yokohama, Japan | ID195
SIMULATION ANALYSIS ON THE RISK OF HYDROGEN
Tsinghua University, Beijing, China
Novel Simulation Model for GM type Orifice Pulse Tube Cryocooler
Venting deflagrations of local hydrogen-air mixture
6th International Conference of Hydrogen Safety
Blast wave from hydrogen storage rupture in a fire
ICHS 2015 – Yokohama, Japan | ID October, 20th
Continuous Codes and Standards Improvement
International Conference on Hydrogen Safety
ABE 223 ABE Principles – Machine systems Bernoulli’s Law Tony Grift
7th International Conference on Hydrogen Safety
VAPOUR CLOUD EXPLOSIONS FROM THE IGNITION OF METHANE/HYDROGEN/AIR MIXTURES IN A CONGESTED REGION Mark Royle(1) Les Shirvill(2) and Terry Roberts(1) (1)
Component Availability Effects
Audrey DUCLOS1, C. Proust2,3, J. Daubech2, and F. Verbecke1
E.Vyazmina / S.Jallais October 2015 ICHS 2015
International Conference on Hydrogen Safety
HOMOGENEOUS HYDROGEN DEFLAGRATIONS IN SMALL SCALE ENCLOSURE
S.G. Giannissi1 and A.G. Venetsanos1
IA-HySafe Standard benchmark exercise SBEP-V21: Hydrogen release and accumulation within a non-ventilated ambient pressure garage at low release rates.
Anubhav Sinha, Vendra Chandra and Jennifer X. Wen
ICHS - October 2015 Jérôme Daubech
Risk Reduction Potential of Accident Mitigation Features
Analysis of acoustic pressure oscillation during vented deflagrations
Flammable extent of hydrogen jets close to surfaces
Modeling and Analysis of a Hydrogen Release in a Large Scale Facility
Les Shirvill1, Mark Royle2 and Terry Roberts2 1Shell Global Solutions
Non-monotonic overpressure vs
Telemark University College,
E. Papanikolaou, D. Baraldi
Flammability profiles associated with high pressure hydrogen jets released in close proximity to surfaces ICHS 6 Yokohama Hall, J., Hooker,
Natural and Forced Ventilation of Buoyant Gas Released in a Full-Scale Garage : Comparison of Model Predictions and Experimental Data Kuldeep Prasad, William.
ICHS5 – 2013 September, Brussels, Belgium | ID161
Context R&D activities in H2 technologies in France is driven by industrial research targeting real applications (DIMITHRY, H2E, HYPE, ...) Safety management.
Gilles Bernard-Michel (CEA)
D. Baraldi (Joint Research Centre – European Commission)
Presentation transcript:

V. Shentsov, M. Kuznetsov, V. Molkov 6th International Conference on Hydrogen Safety, 19-21 October, 2015, Yokohama, Japan The pressure peaking phenomenon: validation for unignited releases in laboratory-scale enclosure V. Shentsov, M. Kuznetsov, V. Molkov Hydrogen Safety Engineering and Research Centre (HySAFER)

Presentation outline What is pressure peaking phenomenon (PPP) Calculation of PPP: 2 steps methodology Experimental facility and validation tests at KIT Ulster theory versus KIT experiments Conclusions

The problem Hydrogen stored as compressed gas @ 350-700 bar Even if unignited, the release of hydrogen has been shown to result in unacceptable overpressures indoors capable of destroying the structure (pressure peaking phenomenon, see Brennan & Molkov, 2013) The experimental results were absent for PPP validation before the project www.hyindoor.eu This study presents the experimental validation of PPP existence and the Ulster theory validation

The pressure peaking phenomenon Example of garage Typical garage of size LxWxH=4.5x2.6x2.6 m with a “brick” size vent. Mass flow rate 390 g/s (350 bar, 5.08 mm TPRD orifice). Pressure limit for structures to withstand Engineering solution: decrease PRD orifice size (by increasing fire resistance of storage tank)

2-steps methodology Cyber-laboratory (free access) Step 1: Make an estimation of PPP existence inside the compartment of interest. PPP exists only when hydrogen leak and vent size are such that there will be only outflow of hydrogen through the vent outside the enclosure, i.e. 100% hydrogen accumulation with time will be reached. Calculate hydrogen concentration in an enclosure using nomogram/model (Molkov et. al 2014) or engineering tool www.h2fc.eu/cyber-laboratory. If the calculated concentration is 100% then the second step has to be applied to calculate the PPP overpressure. Step 2: Use the model/nomogram (Brennan and Molkov 2013) implemented as an engineering tool at www.h2fc.eu/cyber-laboratory to calculate the over-pressure resulting from PPP.

Experimental facility (KIT) Validation tests 19 experiments on PPP were carried out by KIT (Germany) in the enclosure with sizes HxWxL=1x0.98x0.96 m. Round vent of diameter either 11 mm or 16.5 mm was located centrally at the top of the front panel or at the bottom. Three gases were tested: air, helium and hydrogen Internal diameter of the release nozzle is specified to 5 mm, located at the centre of enclosure 10 cm above the floor directed vertically. Release rates ranges 0.1-2.8 g/s. Rear wall Left wall Front wall

Validation Air and helium releases Air, 1.444 g/s, CD=0.72 Helium, 0.22 g/s, Top vent 0.95 cm2, CD=0.72 Helium, 0.22 g/s Bottom vent, CD=0.72 WP1 - Task 1.1 - Presentation title

Validation Helium releases PPP is independent on vent location Helium, 0.985 g/s Bottom vent Vent 0.95 cm2, CD=0.85 Helium, 0.985 g/s, Top vent 0.95 cm2, CD=0.82 Helium, 1 g/s, Vent 2.14 cm2,CD=0.72 Helium, 0.5 g/s, Vent 0.95, CD=0.72 WP1 - Task 1.1 - Presentation title PPP is independent on vent location

Validation Hydrogen releases Hydrogen, 0.108 g/s Vent 0.95 cm2 CD=0.65 Due to higher pressure the experimental enclosure starts to “breathe” resulting in the additional vent area increase of 0.8 cm2 Hydrogen, 1.08 g/s Vent 2.14 cm2, CD=0.9 Hydrogen, 1.08 g/s Vent 0.95 cm2,CD=0.72 WP1 - Task 1.1 - Presentation title

Validation Effect of “breathing” on CD Hydrogen, 0.549 g/s Vent 2.14 cm2, CD=0.54 Hydrogen, 0.108 g/s Vent 0.95 cm2, CD=0.56 The CD scatter 0.54-0.9 is thought due to the “breathing” of the enclosure, i.e. the existence of “additional openings” (non-controllable process) will be “compensated” in the calculations by larger value of discharge coefficient CD. WP1 - Task 1.1 - Presentation title

Leak in fully “closed” box “Breathing” effect Closed camera Leak in fully “closed” box Hydrogen, 0.287 g/s Maximum opening of 0.67 cm2 with CD=0.72 WP1 - Task 1.1 - Presentation title

Concluding remarks Experiments with release of air, helium and hydrogen performed by KIT proved the existence of the pressure peaking phenomena predicted theoretically at Ulster in 2013. The discharge coefficient was found to be in the range CD=0.54-0.90 for performed experiments (“breathing effect”). The average value of CD through the series of test is CD=0.72, the conservative value is CD=0.54. PPP should be considered as an essential part of hydrogen safety engineering for all indoor use of HFC systems.

Acknowledgements Thank you for attention! The authors would like to acknowledge the financial support of Fuel Cells and Hydrogen Joint Undertaking under the HyIndoor project (grant agreement No. 278534), and the European Commission for funding through H2FC project.