INVESTIGATION OF HYDROGEN DISTRIBUTION AND COMBUSTION IN ACCIDENT SCENARIOS

Similar documents
Explosion Hazards of Hydrogen-Air Mixtures. Professor John H.S. Lee McGill University, Montreal, Canada

Safety issues of hydrogen in vehicles Frano Barbir Energy Partners 1501 Northpoint Pkwy, #102 West Palm Beach, FL 33407, U.S.A.

The ADREA-HF CFD code An overview

GT ANALYSIS OF A MICROGASTURBINE FED BY NATURAL GAS AND SYNTHESIS GAS: MGT TEST BENCH AND COMBUSTOR CFD ANALYSIS

REVIEW OF METHODS FOR ESTIMATING THE OVERPRESSURE AND IMPULSE RESULTING FROM A HYDROGEN EXPLOSION IN A CONFINED/OBSTRUCTED VOLUME

Report Title: Compilation of Existing Safety Data on Hydrogen and Comparative Fuels EC-JRC, APCI, DNV, FZK, NCSRD, HYDRO, RA, SHELL, VOLVO

INITIAL ASSESSMENT OF THE IMPACT OF JET FLAME HAZARD FROM HYDROGEN CARS IN ROAD TUNNELS AND THE IMPLICATION ON HYDROGEN CAR DESIGN

COMBUSTION. In order to operate a heat engine we need a hot source together with a cold sink

Ultrasonic Gas Leak Detection

December Newsletter by Vincent Dunn Backdraft and flashover, what is the difference?

APPLICATION OF QUALITATIVE AND QUANTITATIVE RISK ANALYSIS TECHNIQUES TO BUILDING SITING STUDIES

Is This Combustible Dust?

INSTALLATION INSTRUCTIONS

CHAPTER 4: OFFSITE CONSEQUENCE ANALYSIS

INTERACTION OF LIQUID MOTION ON MOBILE TANK STRUCTURE

LNG SAFETY MYTHS and LEGENDS

The Behaviour Of Vertical Jet Fires Under Sonic And Subsonic Regimes

Assessment of Hydrocarbon Explosion and Fire Risks. Professor Jeom Paik. The LRET Research Collegium Southampton, 11 July 2 September 2011

Information for HFO-1234yf Automotive Plant and Service Shop Implementation

HVAC Code Requirements

General Confined Space Awareness

CFD simulation of fibre material transport in a PWR core under loss of coolant conditions

On-Site Risk Management Audit Checklist for Program Level 3 Process

TRANSPORT OF DANGEROUS GOODS

Guidance on Process Safety Performance Indicators

Detonation Waves and Pulse Detonation Engines

Ontario Fire Code SECTION 5.13 DIP TANKS. Illustrated Commentary. Office of the Ontario Fire Marshal

CFD Application on Food Industry; Energy Saving on the Bread Oven

Calculation of Liquefied Natural Gas (LNG) Burning Rates

THE DDESB BLAST EFFECTS COMPUTER VERSION 4.0

Process Safety Management of Highly Hazardous & Explosive Chemicals. Safe Work Practices

HYBRID ROCKET TECHNOLOGY IN THE FRAME OF THE ITALIAN HYPROB PROGRAM

Belgian Stress tests specifications Applicable to all nuclear plants, excluding power reactors 22 June 2011

WORKING IN CONFINED SPACES GUIDELINES

The soot and scale problems

Indiana's Academic Standards 2010 ICP Indiana's Academic Standards 2016 ICP. map) that describe the relationship acceleration, velocity and distance.

NUCLEAR ENERGY RESEARCH INITIATIVE

Determination of the enthalpy of combustion using a bomb calorimeter TEC. Safety precautions

Simulation Analysis Optimisation. Computer Aided Engineering

LIQUEFIED PETROLEUM GASES

Hazardous Substance Class Definitions & Labels

Forces on the Rocket. Rocket Dynamics. Equation of Motion: F = Ma

Facilities Perspectives

QUANTITATIVE RISK ASSESSMENT AND MODELING: FIRE RISKS OF CNG-POWERED BUSES

Boiling Water Reactor Systems


FLAMMABLE AND COMBUSTIBLE LIQUIDS. n OSHA Changes

Subject: Magnet Safety. Overview: Environmental Health & Safety Policy/Procedure Effective Date: July 29, 2011

A.17. OXIDIZING PROPERTIES (SOLIDS)

VALIDATION, MODELING, AND SCALE-UP OF CHEMICAL LOOPING COMBUSTION WITH OXYGEN UNCOUPLING

COKE PRODUCTION FOR BLAST FURNACE IRONMAKING

Hydrogen Powered Bus Fleets Hydrogen Supply & Fueling. National Fuel Cell Bus Workshop October 5, New Orleans, LA

Performance of the Boiler and To Improving the Boiler Efficiency Using Cfd Modeling

ALTERNATIVE METHODS FOR INTERNAL ARC TESTS ON 12 KV AND 24 KV METAL-ENCLOSED SWITCHGEARS WITH COMPACT RMU

Consequence Analysis: Comparison of Methodologies under API Standard and Commercial Software

Belgian Stress tests specifications Applicable to power reactors 17 May 2011

AST M F /GSA TS01 T EST R EPO R T. Rendered to: UNI T E D ST A T ES A L U M INU M

Electrical Classification

Exergy Analysis of a Water Heat Storage Tank

Methods of Avoiding Tank Bund Overtopping Using

HSE information sheet. Fire and explosion hazards in offshore gas turbines. Offshore Information Sheet No. 10/2008

Certain specific properties of compressed gases make them highly useful in various research activities.

Energy transformations

HEAT TRANSFER ANALYSIS IN A 3D SQUARE CHANNEL LAMINAR FLOW WITH USING BAFFLES 1 Vikram Bishnoi

Practical Application of Industrial Fiber Optic Sensing Systems

Computational Fluid Dynamics in Automotive Applications

Part IV. Conclusions

ALVERNIA UNIVERSITY OSHA REGULATION: 29 CFR WELDING, CUTTING, AND BRAZING ( HOT WORK ) SECTION: 3600

CONTENTS. ZVU Engineering a.s., Member of ZVU Group, WASTE HEAT BOILERS Page 2

Combustion Pulsation and Noise by Dan Banks, P.E., Banks Engineering Inc.

Carbon Dioxide and an Argon + Nitrogen Mixture. Measurement of C p /C v for Argon, Nitrogen, Stephen Lucas 05/11/10

Factory owners must ensure the boiler is:

5. State the function of pulveriser. The pulverisers are the equipments which are used to powdered coal.

This digital document created and presented by Richard Fleetwood. He is the. Civil Defense Now! ( websites.

ADDITIONAL INFORMATION ON MODERN VVER GEN III TECHNOLOGY. Mikhail Maltsev Head of Department JSC Atomenergoproekt

BB-18 Black Body High Vacuum System Technical Description

High Performance Castable CL-20 Explosive

An experimental study of temperatures in cloud from release of flashing liquid CO 2 in 3m long channel

Static Electricity. A Health and Safety Guideline for Your Workplace. What Are Some Sources of Static Electricity? What is Static Electricity?

CONFINED SPACE PROCEDURE

Eksplosjonsrisiko, værbeskyttelse og optimalisering av design

E - THEORY/OPERATION

BUILDING CONTROL GUIDANCE SHEET REPLACEMENT WINDOWS AND DOORS Last updated 16/11/2010

Laboratory- and sterilisation equipment HMC EUROPE

Vehicle Maintenance Facilities Requirements for CNG and LNG Vehicles

A Response Surface Model to Predict Flammable Gas Cloud Volume in Offshore Modules. Tatiele Dalfior Ferreira Sávio Souza Venâncio Vianna

Fire Development and Fire Behavior Indicators

EVALUATION OF PHOENICS CFD FIRE MODEL AGAINST ROOM CORNER FIRE EXPERIMENTS

TOXIC AND FLAMMABLE GAS CLOUD DETECTORS LAYOUT OPTIMIZATION USING CFD

Determination of the enthalpy of combustion using a bomb calorimeter TEC

NUMERICAL ANALYSIS OF THE EFFECTS OF WIND ON BUILDING STRUCTURES

Excerpts from the Canadian National Building Code (NBC)

Chapter 15: EXPLOSIVES. An explosive article is an article containing one or more explosive substances.

SAFE TRANSFER OF POWDERS INTO FLAMMABLE LIQUIDS David E. Kaelin Sr., Senior Process Safety Specialist

Sample Written Program. For. Flammable Liquids

New design of a pressure vessel subjected to blast loads

Risk Assessment Instructions

IFE Level 4 Certificate in Fire Science and Fire Safety (HL)

Vacuum drying oven for non-flammable solvents

Originators of the Flexible Water Tube design

Transcription:

Forschungszentrum Karlsruhe in der Helmholtz-Gemeinschaft INVESTIGATION OF HYDROGEN DISTRIBUTION AND COMBUSTION IN ACCIDENT SCENARIOS Introduction Analysis steps I. Mixture generation II. Hazard evaluation III. Combustion simulation IV. Consequence analysis V. Experimental research Summary Applications W. Breitung, A. Kotchourko Institute for Nuclear and Energy Technologies (IKET) Research Center Karlsruhe, Germany (FZK) Technologietag ERCOFTAC Süddeutschland, Stuttgart, 30. September 2005

OBJECTIVES Explosions of large amount of combustible gases mixed with air are responsible for the major part of losses and damages among many industrial accidents Growing utilization of hydrogen as future energy carrier requires better understanding of hydrogen related safety aspects The outcome of a hydrogen related accident depends on many parameters and complex physics Need to develop a mechanistic understanding and complete modeling procedure - to predict accident progress and consequences - to develop efficient mitigation measures - to support development of safe hydrogen technologies - to provide reliable data base for rules, codes and standards The presentation describes approach and current status of FZK analysis methodology

ANALYSIS METHODOLOGY FZK develops numerical codes and methods for consistent analysis of hydrogen behavior in accident scenarios, four main steps: COMBUSTIBLE MIXTURE GENERATION CRITERIA FOR HAZARD POTENTIAL COMBUSTION SIMULATION CONSEQUENCE ANALYSIS Problem geometry Flammability Mitigation y Yes Flame acceleration y Yes Slow deflagration FLAME3D Mechanical and thermal loads Scenario Sources Detonationtransition Detonation on -set y Yes Fast turbulent deflagration COM3D Structural response SDO ABAQUS Distribution GASFLOW GP-Program Detonation DET3D Human effects More than 150 person-years of experience

1. MIXTURE GENERATION Release of cold GH 2 (22K) from LH 2 -tank at bottom of vehicle in garage 1 W energy deposition, 170 g GH 2 /d, 5 x 34g H 2 releases, effect of release rate on risk? COMBUSTIBLE MIXTURE GENERATION Problem geometry Mitigation Scenario Sources Distribution GASFLOW Case1: 3,4 g H 2 /s For 10 s

MIXTURE GENERATION : Case 2 GH 2 source of 0,34 g H 2 /s for 100s duration

MIXTURE GENERATION :Case 2 Calculated H 2 -concentration field for 0.34 g H 2 /s release in a garage, x = 0,6 vol% 20 s 50 s 80 s 120 s 0.00 1.33 2.66 4.00 vol% H 2

II. HAZARD POTENTIAL What hazard is actually presented by the calculated H 2 -air distribution? CRITERIA FOR HAZARD POTENTIAL Flammability yyes Flame acceleration yyes Detonation Detonation- -set transition y Yes Hydrogen hazard is mainly determined by the fastest possible combustion regime of the mixture - slow deflagration - fast turbulent deflagration - detonation Transition criteria were developed to estimate conservative (fastest) combustion regime possible for a given H 2 -air mixture and geometry - inert /slow - slow/fast - deflagration/detonation GP-Program

GP-CODE All criteria implemented in interactive GP-code f( p 0, T 0, x H2, x O2, x H2O, x N2,D) 0.8 0.7 p = 0.1 MPa 0 T 0 = 400 K Example for H 2 -air-steam mixtures - mixtures above 60 vol% are inert - flammability and flame acceleration limits nearly coincide on the rich side - the DDT limit is scale dependent, in larger system (D) leaner mixtures can undergo a deflagration-todetonation transition Volume fraction hydrogen 0.6 0.5 0.4 0.3 0.2 0.1 D = 1m D = 5m DDT limit Flame acceleration limit Flammability limit 0.0 0.0 0.1 0.2 0.3 0.4 0.5 0.6 Volume fraction steam

Criteria are evaluated on-line in GASFLOW from known H 2 -distribution CASE 1: - significant and stable volume of combustible mixture - potential for flame acceleration and DDT exists during and shortly after release CASE 2: - only small volume is able to support deflagrations, disappears shortly after end of release - no DDT hazard - inherent mixing mechanisms sufficient to dilute source H 2 release in confined spaces above a certain critical rate (here 0.3 g/s) requires additional measures for hazard control HAZARD FOR GARAGE EXAMPLE 180 160 140 120 100 80 60 40 20 CASE 1 CASE 2 d (cm) cc 0 0 0.8 10 20 30 40 50 60 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 0 3 10 20 30 40 50 60 2.5 2 1.5 1 0.5 3.4 g H 2 /s, 10s.34 g H 2 /s, 100s 0 0 10 20 30 DDT V (m³) fa no DDT D 7λ 40 50 60 90 80 70 60 50 40 30 20 10 d (cm) cc 0 0 50 100 150 200 250 0.12 0.10 0.08 0.06 0.04 0.02 V (m³) fa 0 0 50 100 150 200 250 1.4 1.2 1.0 0.8 0.6 0.4 0.2 no DDT D 7λ 0 0 50 100 150 200 250

III. COMBUSTION SIMULATION COMBUSTION SIMULATION Different physics involved in different combustion modes Slow deflagration FLAME3D Fast turbulent deflagration COM3D Three CFD codes under development and in use at FZK Codes model stable combustion regimes, while transition phenomena are covered by criteria Detonation DET3D

LOCAL EXPLOSION IN CONFINED VOLUME COMBUSTIBLE MIXTURE GENERATION Plant geometry Mitigation Scenario Sources Distribution GASFLOW CRITERIA FOR HAZARD POTENTIAL Flammability y Flame acceleration y Test chamber at FZK for hydrogen release and local explosion experiments in confined spaces under controlled flow conditions - volume 160 m 3 - air ventilation up to 24,000 m 3 /h Air supply Duct work Detonation on -set y GP-Program COMBUSTION SIMULATION Slow deflagration FLAME3D Fast turbulent deflagration COM3D Detonation DET3D CONSEQUENCE ANALYSIS Structural stability against dynamic pressure loads tested under conservative conditions - stoichiometric, homogeneous mixture - locally concentrated (2-16g H 2 ) - obstacles to reach high flame speeds Test chamber Lower compartment Mechanical and thermal loads Structural response ABAQUS Human effects

COM3D SIMULATION FOR FZK TEST CHAMBER Fast local turbulent H 2 -air deflagration in FZK test chamber - 8 g H 2 - p0 = 0.1 MPa - x H2 = 29.8 vol% Numerical simulation COM3D: x = 3.45 cm, total ~ 7 10 6 cells Fast combustion followed by detonation of 8 g H 2 in stoichiometric mixture in cube 69 x 69 x 69 cm

IV. CONSEQUENCE ANALYSIS Output of CFD combustion calculation allows to estimate the consequences CONSEQUENCE ANALYSIS Mechanical and thermal loads Structural response SDO ABAQUS Human effects Overpressure [bar] Overpressure [bar] 0.5 0.4 0.3 0.2 0.1 0.0-0.1-0.2 Time [s] Experiment Simulation 8g H 2-0.3 0.18 0.19 0.20 0.21 0.22 0.23 0.3 0.2 0.1 0.0-0.1 Sensor 20 wall, near Sensor 14 floor Experiment Simulation Overpressure [bar] Overpressure [bar] 0.3 0.2 0.1 0.0-0.1 0.6 0.4 0.2-0.0 Experiment Simulation 8g H 2 0.19 0.20 0.21 0.22 0.23 0.24 Time [s] Sensor 6 upper corner Sensor 16 wall, far Experiment Simulation -0.2 8g H 2 0.19 0.20 0.21 0.22 Time [s] Time [s] Example: Pressure loads of 8g H 2 test in FZK facility 8g H 2-0.2 0.19 0.20 0.21 0.22 0.23 0.24

STRUCTURAL RESPONSE: Test chamber results Response of FZK test chamber simulated with ABAQUS - input : P(t) at 8000 locations (COM3D ABAQUS) - output: stress and strain Maximum displacement in frame (mm) Maximum stress in inner wall (MPa) Result: Walls and framework structure can confine tested fast local combustions, limiting H 2 mass estimated with model

STRUCTURAL RESPONSE: Damage thresholds for civil buildings Comparison of measured blast wave parameters in FZK test chamber to known damage limits of civil buildings. 10 6 p + I + Positive overpressure p + [Pa] 10 5 10 4 Unconfined gaseous detonations FZK experiments 2g H 2 16g H 2 glass breakage 2g H 2 16g H 2 Partial demolition 50%-75% of walls destroyed Major structural damage, some wrenched load bearing members fails Minor structural damage wrenched joints and partitions t 10 3 10 0 10 1 10 2 10 3 10 4 Positive impulse I + [Pa*s] p-i data from W.E. Baker et al

HUMAN EFFECTS: Injury thresholds Comparison of measured blast wave parameters in FZK test chamber to known injury thresholds 10 6 p + I + Unconfined gaseous detonations 2g H 2 16g H 2 Lung rupture t Positive overpressure p + [Pa] 10 5 10 4 10 3 FZK experiments 2g H 2 16g H 2 NASA ear drum rupture Temporary ear threshold shift Skull fracture (60 kg body weight) 10 0 10 1 10 2 10 3 10 4 10 5 Positive impulse I + [Pa*s] 50% ear drum rupture Lethality from whole body impact (60 kg body weight) -Threshold data converted from W.E.Baker et al - Gaseous detonation data from S.B. Dorofeev et al

HUMAN EFFECTS: Injury thresholds Comparison of measured blast wave parameters p + and T + in FZK test chamber to known injury thresholds 10 6 p + I + T + =2I + / p + Unconfined gaseous detonations 16g H 2 Lung rupture T + t Positive overpressure p + [Pa] 10 5 10 4 10 3 2g H 2 FZK experiments 2g H 2 16g H 2 NASA ear drum rupture Temporary ear threshold shift 50% ear drum rupture Skull fracture (60 kg body weight) 10-4 10-3 10-2 10-1 10 0 10 1 Positive impulse duration T + [s] Lethality from whole body impact (60 kg body weight) -Threshold data converted from W.E.Baker et al - Gaseous detonation data from S.B. Dorofeev et al

TEST SITE AT FZK FOR HYDROGEN EXPERIMENTAL RESEARCH Experimental studies: Development of transition criteria Validation of CFD tools Development of scaling methodology Facility for H 2 release and distribution studies under controlled flow conditions Large-scale facilities for combustion studies Combustion tubes

LARGE-SCALE COMBUSTION EXPERIMENTS Facilities of scales relevant to industrial dimensions Multipurpose vessels for research connected with combustion processes in large scales A3 30 m 3 A1-100 bar A3-60 bar A1 110 m 3

MEDIUM-SCALE COMBUSTION EXPERIMENTS Study of combustion, turbulent deflagration, DDT and detonation Partially vented geometry Confined geometry

SUMMARY A mechanistic procedure for analysis of hydrogen behavior was developed. The methodology is based on 3D CFD tools. It addresses: - prediction of accident consequences - development of efficient mitigation measures - support of safe use of hydrogen technologies Two examples for hydrogen behavior in confined spaces were presented - hydrogen release is safe up to a critical release rate, which depends on details and which can be evaluated - structural damage of the enclosure can be modeled (ABAQUS) - combustion of up to 16 g hydrogen can cause : - glass fraction but no structure damage to normal civil buildings - ear damage but no lung rupture - blast effects from local explosions (2-16g H 2 ) are restricted to ear damage