Full Scale Experimental Testing of Aerosol Filling Facilities Experiments and Validation

Similar documents
Comparison of Large-Scale Vented Deflagration Tests to CFD Simulations for Partially Congested Enclosures

The Comparison of CFD with a Traditional Method Used in an Incident Investigation Case Happened in Taiwan

CFD Based Approach for VCE Risk Assessment

American Chemical Society (ACS) 246th ACS National Meeting Indianapolis, Indiana September 9, 2013

Internal Explosion Methodologies

Transport of gas tanks for motor vehicles

Experimental determination of deflagration explosion characteristics of methane air mixture and their verification by advanced numerical simulation

Transport of gas tanks for motor vehicles

Section 1.3: PRESSURE VESSEL COMPONENTS AND SYSTEMS AND COMPRESSED GAS CYLINDERS

Hydrogen and fuel cell stationary applications: key findings of modelling and experimental work in the HYPER project

ST/SG/AC.10/C.3/2016/8. Secretariat. United Nations. Transport of gas tanks for motor vehicles. Introduction

CFD Modelling of LPG dispersion

PRACTICAL EXPERIENCES IN THE PRODUCTION OF INSULATION FOAMS WITH HYDROCARBON BLOWING AGENT IN DEVELOPING AND DEVELOPED COUNTRIES

CFD SIMULATIONS OF GAS DISPERSION IN VENTILATED ROOMS

MODELING OF HYDROGEN EXPLOSION ON A PRESSURE SWING ADSORPTION FACILITY

E X T E R I O R L I V E P R O P A N E F I R E P R O P P R O C E D U R E S F O R U S I N G T H E P R O P A N E P R O P

Rotary air valves used for material feed and explosion protection are required to meet the criteria of NFPA 69 (2014)

ANNEX AMENDMENTS TO THE INTERNATIONAL CODE FOR FIRE SAFETY SYSTEMS (FSS CODE) CHAPTER 15 INERT GAS SYSTEMS

Determination of the Design Load for Structural Safety Assessment against Gas Explosion in Offshore Topside

Gas Cabinets and Valve Manifold Boxes: Applying CGA G13- Rev 2015 to Gas Delivery Equipment

REPORT INVESTIGATION OF 3M CLEAN AND STRIP DISKS IN EXPLOSIVE ATMOSPHERES. Client: 3M Norge A/S. Authors: Bjørnar A. Johnsen Geir H.

PSM TRAINING COURSES. Courses can be conducted in multi-languages

Combined Pressure / Vacuum Relief Valve KITO VD/o

Numerical simulation of the ALBA s synchrotron cooling system response to pump start-up and shut-down Page 1

REQUIREMENTS FOR VALIDATION OF MATHEMATICAL MODELS IN SAFETY CASES

The model of thermal response of Liquefied Petroleum Gas Tanks subjected to accidental heat input

Line Pressure Regulator. Class I or Class II. FRS 7../6 Series

SIMULATIONS OF HYDROGEN RELEASES FROM A STORAGE TANKS: DISPERSION AND CONSEQUENCES OF IGNITION

Engineering Models for Vented Lean Hydrogen Deflagrations

ICHEME SYMPOSIUM SERIES NO. 144

ACCUMULATION OF HYDROGEN RELEASED INTO A VENTED ENCLOSURE - EXPERIMENTAL RESULTS

Flexibility Enhancements for Gas Turbines

SPD Pressure Sensor Families

The World Bank Ozone Operations Resource Group (OORG) 18th Meeting, June 12th, 2001

The Influence Of Vessel Volume And Equivalence Ratio In Vented Gas Explosions

Guidance on room integrity testing and its interpretation

CFD SIMULATIONS OF VENTILATION EFFECT ON HYDROGEN RELEASE BEHAVIOR AND COMBUSTION IN AN UNDERGROUND MINING ENVIRONMENT

Ignition modelling Are our approaches aligned?

Vented gas and dust explosions

INTERNATIONAL ASSOCIATION OF CLASSIFICATION SOCIETIES. Interpretations of the. IGF Code

OPTIMIZING THE LENGTH OF AIR SUPPLY DUCT IN CROSS CONNECTIONS OF GOTTHARD BASE TUNNEL. Rehan Yousaf 1, Oliver Scherer 1

MODELING&SIMULATION EXTRAPOLATED INTERNAL ARC TEST RESULTS: A COUPLED FLUID-STRUCTURAL TRANSIENT METHODOLOGY

ISO INTERNATIONAL STANDARD. Small craft Liquefied petroleum gas (LPG) systems

SAFETY PLAN REVIEW ITM

Line Pressure Regulators Class I or Class II. FRS 7../6 Series

Abstract. Geometry Obstructions Ventilation Wind conditions

Example 4 - Airbag. Summary

EXPERIMENTAL STUDY ON HYDROGEN EXPLOSIONS IN A FULL-SCALE HYDROGEN FILLING STATION MODEL

1. PURPOSE This Heathrow Instruction details the restrictions on the storage, transportation and use of acetylene at Heathrow Airport.

Limited quantities of compressed gases.

Model 10E Enviro-Line Environmental Pressurization System Installation & Operation Manual

RESIDENTIAL AND COMMERCIAL REGULATORS FOR ABNORMAL OPERATING CONDITIONS (AOC) WITH 3 FOOT CLEARANCE INSTALLATION REQUIREMENTS.

CFD Modelling of Blast Waves from BLEVEs

Simulations of hydrogen releases from high pressure storage systems

Fire and Safety for Offshore drilling and production Ajey Walavalkar ANSYS Inc.

The Relationship Between Automation Complexity and Operator Error

TEST REPORT. Solamatrix Inc. GLASS-GARD GGL1200 Multi-ply Window Film and Wetglaze Anchoring System on Single 6mm (1/4 ) Annealed Glass.

New Findings for the Application of Systems for Explosion- Isolation with Explosion Venting

INTERNATIONAL SKATING UNION

STRESS ANALYSIS OF BICYCLE PADDLE AND OPTIMIZED BY FINITE ELEMENT METHOD. S. Abeygunasekara 1, T. M. M. Amarasekara 2

SHAPA TECHNICAL PAPER 10 (Revised) SIZING OF EXPLOSION RELIEF VENTS DAVID BURN FIKE UK LTD

MEGR-1912 Instruction Manual

S300 Series. Valve Link. Features. Fisher Controls

Sprinkler Protection for Cloud Ceilings. SUPDET 2013 Jason Floyd, Ph.D. 28 February 2013

DSEAR- Storage, Use and handling of gas cylinders guidance.

MK 3 Passive Operating Guide

Simulation and modelling of water spray in the 3D explosion simulation program FLACS. Elin Kristin Dale

CASH VALVE TYPE KP BACK PRESSURE VALVES

Determination of the wind pressure distribution on the facade of the triangularly shaped high-rise building structure

Pipe-Away Pressure Vacuum Vent /Conservation Vent

Valve Proving System VDK 200 A S02

Valve Proving System VDK 200 A S06*

INHERENTLY SAFER DESIGN CASE STUDY OF RAPID BLOW DOWN ON OFFSHORE PLATFORM

ANL Bubble Chamber Superheated Active Target System

Application of Computational Fluid Dynamics to Compressor Efficiency Improvement

Dow s New Practice for Locating Temporary Portable Buildings. P. Partridge 9/29/05 UNRESTRICTED - May be shared with anyone Slide 1

Fire safety of staircases in multi-storey buildings The results of measurements in Buildings and Simulations

Overview EUSSAM12. Carry out tightness testing and direct purging of gas installations

North American 7337A/B/C-4 High Pressure Gas Regulators

VENTED EXPLOSION OF HYDROGEN / AIR MIXTURE: AN INTER COMPARISION BENCHMARK EXERCISE

CONSIDERATION OF DENSITY VARIATIONS IN THE DESIGN OF A VENTILATION SYSTEM FOR ROAD TUNNELS

PRAGMATIC ASSESSMENT OF EXPLOSION RISKS TO THE CONTROL ROOM BUILDING OF A VINYL CHLORIDE PLANT

BUTANE TS-MSDS 44 1 IDENTIFICATION OF THE SUBSTANCE & OF THE COMPANY / UNDERTAKING IDENTIFICATION OF THE SUBSTANCE OR PREPARATION:

Investigation of Cargo Tank Vent Fires on the GP3 FPSO, Part 2: Analysis of Vapour Dispersion

Mooney * Noise Controller Installation, Operation, and Maintenance Manual

Management of Change (MOC) Could Have Prevented Death

Figure 1 FSM 250 roof anchor system

THE PERFORMANCE OF PLANING HULLS IN TRANSITION SPEEDS

GAS FUEL VALVE FORM AGV5 OM 8-03

Internal Arc Simulation in MV/LV Substations. Charles BESNARD 8 11 June 2009

Improving Accuracy of Frequency Estimation of Major Vapor Cloud Explosions for Evaluating Control Room Location through Quantitative Risk Assessment

Machine Gun Suppression Lessons Learned

Large Scale Tests for Explosion Pressure Resistant Design in Combination with Explosion Venting. Folie 1

RESIDENTIAL REGULATORS

SUBPART C - STRUCTURE

SF SERIES CNG COMPRESSOR MODEL HF-4MH. 4 Nm3/Hour Displacement OPERATION MANUAL

Wind Plant Simulation and Validation Jonathan Naughton Department of Mechanical Engineering University of Wyoming

THE EXTERNAL EXPLOSION CHARACTERISTICS OF VENTED DUST EXPLOSIONS.

Process Safety Management Of Highly Hazardous Chemicals OSHA 29 CFR

1 PIPESYS Application

Transcription:

Full Scale Experimental Testing of Aerosol Filling Facilities Experiments and Validation FLUG User Group Meeting 29 th November 2017 Tim Jones Principal Consultant Email: tjones@mmiengineering.com

Introduction Background Project Overview Initial Analysis Experimental Program Validation

Background Almost all domestic aerosols are propelled by a liquefied compressed gas. Since CFCs were banned in the 70 s these are mainly flammable LPG propellants (propane/ butane/ Pentane blends) Aerosols are filled with propellants in dedicated unmanned buildings external to normal product. Up to 500cans per minute (each with up to 200ml of LPG) are filled. Many layers of protection for the flammable gas operation: Zoning /Ventilation /Unmanned operation/ gas detection /automatic shutdown /etc.

Background Pressure relief is last line of defense

Background Typical building design Factory Lifting Top Hat Roof Gas House Conveyor for cans

Background Inside the gas house Gasser

Project Overview Historically building have been design based on NFPA standards Calculations using these standards indicated that the withstand of the walls were close to the expected overpressures FLACS analysis conducted by Gexcon To validate FLACS analysis experimental program was conducted over 2 phases FLACS analysis was repeated as a validation exercise

Design Specification Circular building with top down ventilation out through subfloor vent Wall strength to NFPA 30B (100lb/ft 2-48mbar) Relief design to NFPA 68 Relief pressure (Pstat) <20mbar Light weight roof (should be <12.2kg/m 2 ) with restraint chains (1.4 to 2m length) Challenge existing circular roof design comes in closer to 30kg/m 2

NFPA 68 Correlations Reduced pressure a function of: Gas type Vent area Relief pressure Internal surface areas These correlations suggested overpressures are borderline compared to the capacity of the walls. Some uncertainty with respect to what areas should be considered.

Initial FLACS Analysis FLACS analysis was carried out by Gexcon. Calculated overpressures of 1 barg. These pressure would lead to catastrophic failure of the gas houses. Gas houses would have to rebuilt around the world cost of > 10m

Initial FLACS Analysis

Initial FLACS Analysis Some simplifications had to be made in the FLACS analysis. FLACS is unable to resolve curved surfaces directly therefore they are represented by the porous sub model. The roof itself is a top hat arrangement with slanted side. Again these cannot be resolved by the grid. Although pressure relief panels can be modelled there is no account for a moving mesh. Based on engineering judgement it was felt that the overpressure were overpredicted. Due to the costs associated with rebuilding the gas houses it was decided to embark on an experimental program.

Experimental Program Started with a blank piece of paper and was when MMI got involved. Experiments were defined, test rig was designed, fabricated and assembled onsite at Spadeadam. Rig was a full scale representation. FEA analysis conducted to ensure test rig would remain elastic

Experimental Program

Experimental Program All experiments considered 100% fill of the gas house Phase 1: 1A: Polythene sheet roof, ignition at bottom of gas house 2A: Same as 1A, ignition at bottom of gas house 3A: Repeat of 1A due to insufficient fuel, ignition at bottom of gas house 4A: Same as 1A with actual roof, ignition at bottom of gas house 5A: Same as 4A, ignition at bottom of gas house

Test 1A

Test 1A

Test 4A

Test 4A

Test 4A

Phase 1 Summary Tests 1A and 3A define a lower limit for the design pressure for the walls for an idealised roof. Average pressure on the walls was 0.08 barg with a peak of 0.09 barg. With the roof overpressures increased to 0.1 barg average and 0.18 barg max. Client was happy! Might not have to knock down all the gas houses and rebuild them. Repeatability was also good between tests (1A and 3A and 4A and 5A). Therefore decision was made to not conduct multiple test for Phase 2.

Experimental Program Second phase looked at sensitivities Phase 2: 6A: Polythene sheet roof, ignition inside the gasser

Test 6A Second phase looked at sensitivities Gasser

Experimental Program Second phase looked at sensitivities Phase 2: 6A: Polythene sheet roof, ignition inside the gasser 7A: Polythene sheet roof, ignition at bottom of gas house, preignition turbulence

Experimental Program Second phase looked at sensitivities Phase 2: 6A: Polythene sheet roof, ignition inside the gasser 7A: Polythene sheet roof, ignition at bottom of gas house, preignition turbulence 8A: Frangible roof, ignition at bottom of gas house

Test 8A Foam Panels

Test 8A

Experimental Program Second phase looked at sensitivities Phase 2: 6A: Polythene sheet roof, ignition inside the gasser 7A: Polythene sheet roof, ignition at bottom of gas house, preignition turbulence 8A: Frangible roof, ignition at bottom of gas house 9A: Polythene sheet, ignition at bottom of gas house, grated floor removed

Test 9A

Test 8A

Test 8A

Phase 2 Summary Ignition in the gasser led to overpressures increasing from 0.08 to 0.25 barg. 220% increase. Addition of pre-ignition turbulence increased overpressures from 0.08 to 0.15 barg. 88% increase. The removal of the grating led to a reduced overpressures from 0.08 to 0.07 barg. 15% reduction. The frangible roof increases overpressures from 0.08 to 0.28 barg compared to the polythene roof test. Compared to the steel roof overpressures were increased from 0.14 to 0.28 barg. Increases were due to three factors: Residual blockage of the fixed roof structure Sections of the panels remaining in-place following the explosion. Limited by design wind speeds

Phase 2 Summary Could reduce overpressures by using tapered panels.

FLACS Validation Experimental results are lower than initial FLACS analysis. Approximately a factor of 3. Further work was carried out for Test 1A by Gexcon.

FLACS Validation Maximum pressure distribution With gasser walls

FLACS Validation Maximum pressure distribution With gasser walls No gasser walls

FLACS Validation Pressure evolution within gas house

FLACS Validation Pressure evolution within gas house with no gasser walls

FLACS Validation Sensitivity conducted on the ignition location with no gasser walls. Differences of up to 40% observed for changes in ignition location by only 0.5 m.

FLACS Validation Summary For Test 1A the overpressures were 0.08barg and FLACS calculated overpressures of ~0.25barg. Reduced overpressures seen when the gasser was removed and for sensitivities with respect to ignition location but still higher than experimental results. Sensitivities with the commercial version of FLACS have been exhausted and currently investigating if modifications to the solver could be made to better match experimental data.

Current Status of the Project There was a fear from the project that the overpressures based on the frangible roof were too high and there was a reluctance to re-engineer the roofs. The steel roof tests showed positive results with respect to pressure therefore shock absorbing springs have been retrofitted to chains to reduce shock load and keep the roof attached to the structure. Client would like to have an analytical solution to design of gas houses in the future therefore still interested in the work being done by FLACS. MMI have also started a project with Cambridge University, in conjunction with the client, to trial their CFD codes to simulate the experiments.

Engineering a Safer World Engineering a Safer World mmiengineering.com mmiengineering.com