Safety related issues of the unexpected Argon release into the tunnel Maciej Chorowski, Ziemowit Malecha, Jarosław Poliński.

Slides:



Advertisements
Similar presentations
These describe matter. Starts with a “p”
Advertisements

Liquid Nitrogen and Cryogenics Training Program
Chapter 4 Mass and Energy Analysis of Control Volumes (Open Systems)
WORKSHOP 2010 ON CONSTITUTIVE MODELING IN APPLICATIONS FOR INDUSTRIAL PROCESSES KRAKÓW, 1-3 September, 2010 Poznan University of Technology ASSESSMENT.
Introduction to SCREEN3 smokestacks image from Univ. of Waterloo Environmental Sciences Marti Blad NAU College of Engineering and Technology.
Chapter 15 Fluids. Pressure The same force applied over a smaller area results in greater pressure – think of poking a balloon with your finger and.
OpenFOAM for Air Quality Ernst Meijer and Ivo Kalkman First Dutch OpenFOAM Seminar Delft, 4 november 2010.
1 Validation of CFD Calculations Against Impinging Jet Experiments Prankul Middha and Olav R. Hansen, GexCon, Norway Joachim Grune, ProScience, Karlsruhe,
Some problems in an assessment of the consequences of a fire and an explosion during the multicomponent mixture unknown composition release. Melania Pofit-Szczepańska.
ICHS 2007, San Sebastian, Spain 1 SAFETY OF LABORATORIES FOR NEW HYDROGEN TECHNIQUES Heitsch, M., Baraldi, D., Moretto, P., Wilkening, H. Institute for.
Defining Hazardous Zones – Electrical Classification Distances Gary Howard,Andrei Tchouvelev, Vlad Agranat and Zhong Cheng Defining Hazardous Zones – Electrical.
CFD Modeling for Helium Releases in a Private Garage without Forced Ventilation Papanikolaou E. A. Venetsanos A. G. NCSR "DEMOKRITOS" Institute of Nuclear.
page 0 Prepared by Associate Prof. Dr. Mohamad Wijayanuddin Ali Chemical Engineering Department Universiti Teknologi Malaysia.
Thermal Analysis of Helium- Cooled T-tube Divertor S. Shin, S. I. Abdel-Khalik, and M. Yoda ARIES Meeting, Madison (June 14-15, 2005) G. W. Woodruff School.
Determination of Clearance Distances for Venting of Hydrogen Storage Andrei Tchouvelev, Pierre Benard, Vlad Agranat and Zhong Cheng.
Toxic Release and Dispersion Models
HYDRODYNAMIC EVOLUTION OF IFE CHAMBERS WITH DIFFERENT PROTECTIVE GASES AND PRE-IGNITION CONDITIONS Zoran Dragojlovic and Farrokh Najmabadi University of.
On numerical simulation of liquefied and gaseous hydrogen releases at large scales V. Molkov, D. Makarov, E. Prost 8-10 September 2005, Pisa, Italy First.
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,
Air Pocket 8th problem. A vertical air jet from a straw produces a cavity on a water surface. What parameters determine the volume and the depth of the.
ICHS4, San Francisco, September E. Papanikolaou, D. Baraldi Joint Research Centre - Institute for Energy and Transport
Viscous Stress Terms for the RELAP5-3D Momentum Equations Adam Kraus and George Mesina RELAP5 International Users Seminar 2010 September 20-23,
Physics Chapter 11 Energy.
Compressible Flow Introduction
Helium Spill Test in LHC tunnel to define length of restricted working areas  Actual situation  Evolution  How to continue  Set-up of the spilling.
128 May 2013 CENF Near Far Integration For the Safety Folder + Environmental impact Study Simple process: Identify Safety issues >> description >> risk.
Page 1 SIMULATIONS OF HYDROGEN RELEASES FROM STORAGE TANKS: DISPERSION AND CONSEQUENCES OF IGNITION By Benjamin Angers 1, Ahmed Hourri 1 and Pierre Bénard.
Physics and Astronomy Outreach Program at the University of British Columbia Physics and Astronomy Outreach Program at the University of British Columbia.
Explosion An explosion is a rapid expansion of gases resulting in a rapid moving pressure or shock wave. The expansion can be mechanical or it can be.
7.2 Fluids and Density 1)A fluid is any form of matter that can flow. a)Liquids and gases are fluids since they do not have a fixed shape. b)Solids are.
Fog Progression Presented by: Meshari Al-Hasan Supervised by: Prof. M. Fahim.
Safety Requirements and Regulations 10/3/20121Safety Requirements & Regulations James Sears.
Objective of the investigation: Determine the number and arrangement of jet fans to be installed in the Acapulco Tunnel that will ensure an air quality.
Wu. Y., International Conference on Hydrogen Safety, September Initial Assessment of the Impact of Jet Flame Hazard From Hydrogen Cars In.
Fluid Report Presentation Onur Erkal Korgun Koyunpınar Korhan Türker Hakan Uzuner.
Energy and Matter. In which state of matter does conduction of heat occur? Why?
Experimental and numerical studies on the bonfire test of high- pressure hydrogen storage vessels Prof. Jinyang Zheng Institute of Process Equipment, Zhejiang.
Task Force on Safety of Personnel in LHC underground areas following the sector 34 accident of 19-Sep-2008 Status report LPC 07/05/2009 B. Delille, S.
EHN1 Cryogenic Integration Requirements David Montanari / Johan Bremer Jun 18, 2015 Rev. 1.
Example 2 Chlorine is used in a particular chemical process. A source model study indicates that for a particular accident scenario 1.0 kg of chlorine.
© GexCon AS JIP Meeting, May 2011, Bergen, Norway 1 Ichard M. 1, Hansen O.R. 1, Middha P. 1 and Willoughby D. 2 1 GexCon AS 2 HSL.
Air filmcooling through laser drilled nozzles STW project CASA-dag
Evaluation of a rate form of the equation of state L.H. Fick, P.G. Rousseau, C.G. du Toit North-West University Energy Postgraduate Conference 2013.
Heating Curves and Energy. Which of the following measures the average kinetic energy of a sample? 1.Mass 2.Volume 3.Specific heat 4.Temperature 5.Heat.
Duy Phan, EN-STI-RBS. Description of the hazards  An Oxygen Deficiency Hazard (ODH) exists when the concentration of O2 ≤ 19.5 % (by volume)  Cold burns.
Flow of Compressible Fluids. Definition A compressible flow is a flow in which the fluid density ρ varies significantly within the flowfield. Therefore,
IB Physics 11 Mr. Jean November 3 rd, The plan: Video clips of the day Work Potential energy –Gravitational potential kinetic energy.
Shock waves and expansion waves Rayleigh flow Fanno flow Assignment
LAGUNA Design of a pan- European Infrastructure for Large Apparatus studying Grand Unification and Neutrino Astrophysics Guido Nuijten.
ESS Cryogenic Distribution System for the Elliptical Linac SV calculation approach Preliminary Design Review Meeting, 20 May 2015, ESS, Lund, Sweden J.
First Outcome of the Task Force on Safety of Personnel in LHC underground areas following the sector 34 accident of 19-Sep-2008 R. Trant on behalf of the.
Title: Prevention methods development against aerosol terrorism for ventilation of Tbilisi subway Grant N Report - Numerical modeling of aerosol.
S.G. Giannissi1,2, I.C.Tolias1,2, A.G. Venetsanos1
TOXIC RELEASE & DISPERSION MODELS (PART 3) Prepared by;
1) How is stopping distance calculated?
Cryogenic behavior of the cryogenic system
Experimental hall design in Japanese site
S.G. Giannissi1 and A.G. Venetsanos1
Review of ChE Fluid Mechanics
Vertical Motion Problems
Potential Energy.
Chapter 5: Energy Section 1 Part 2.
PURPOSE OF AIR QUALITY MODELING Policy Analysis
CFD MODELING OF LH2 DISPERSION USING THE ADREA-HF CODE
Unit 3 Functions.
Work and Energy Practice Problems
Two disks Two disks are initially at rest. The mass of disk B is two times larger than that of disk A. The two disks then experience equal net forces F.
CFD computations of liquid hydrogen releases
Physical Science: Chapter 13 Section 3: Energy
Cryogenic behavior of the magnet
Presentation transcript:

Safety related issues of the unexpected Argon release into the tunnel Maciej Chorowski, Ziemowit Malecha, Jarosław Poliński

Motivation - LAGUNA-LBNO next-generation neutrino observatory a huge amount of liquid Argon (LAr) transported in cryogenic-tank trucks cistern capacity: 20 m3 (27.6 tons) the first Pilot installation:3800 tons of LAr GLACIER tons of LAr 10.5 km decline, irregular spiral shape, slope of 7.3  Work done: risk analysis of the LAr transportation identification of the worse case scenario effects of an uncontrolled LAr leak to the tunnel Acknowledgments: European Union's Seventh Framework Program grant agreement no [LAGUNA-LBNO] financial resources for science 2015, Polish Ministry of Science Large Apparatus studying Grand Unification and Neutrino Astrophysics and Long Baseline Neutrino Oscillations

Outline 1.Calculation of the LAr mass flow through the rupture hole 2.Calculations of the substitute gas Argon (GAr) area (needed for proposed numerical model) 3.Mathematical model and numerical implementation (GAr propagation in the tunnel) 4.Results of the numerical calculations: GAr cloud propagation for different ventilation regime

LAr, kg/s LAr mass flow through the rupture hole Time, min

Calculation of the substitute GAr area

Mathematical model and implementation Compressible flow of the gas mixture: air (79%N %O 2 ) and Argon The mixing process: the diffusion-advection equation for each gas, Momentum transportation: Navier-Stokes equations Mixture: additivity Energy transportation: enthalpy equation Numerical implementation: OpenFOAM CFD toolbox, FVM, PISO algorithm

Numerical model: the geometry Inclination = 7.3  Length = 200 m Width = 5 m Height = 5 m

Results of the numerical calculations Ventilation speeddirection 103.7down the tunnel down the tunnel 541.7up & down 650up the tunnel Table Average velocity and direction of GAr propagation for different ventilation regimes.

Limiting case: All the GAr goes up the tunnel

Conclusions Accident of the Argon spill inside the Pyhasalmi mine tunnel was investigated. GAr cloud tends to flow down the tunnel for low and moderate ventilation,1-3 m/s Low temperature and O 2 deficiency hazard only at the ground level of the tunnel. For air ventilation larger than 5 m/s, the GAr stays in the vicinity of the incident or go slowly up the tunnel. In this case, the temperature and the O 2 deficiency can drop in regions significantly above the ground of the tunnel. In case of Argon spill incident: ventilation should be reduced to the lowest possible speed ( max 2.5 m/s ), personnel should be evacuated upwards from the incident location Open Source OpenFOAM numerical toolbox is suitable for cryogenics flows analysis.