WP1 – Management 3rd General Meeting€¦ · 5 PRESLHY 3rd General Meeting, 7- 8 March 2019, Bergen, Norway. WP1 – Management (KIT) WP2 - Technical Strategy & Evaluation (AL)

1 PRESLHY 3rd General Meeting, 7-8 March 2019, Bergen, Norway

Pre-normative REsearch for Safe use of Liquid HYdrogen

WP1 – Management3rd General MeetingHySafe/GexCon, Bergen, Norway, 7 March 2019


Objectiveso Report on the initial state-of-the-art and knowledge gaps with priorities

related to the envisaged use of LH2

o Execute adjusted experimental program addressing release, ignition andcombustion phenomena with highest priorities

o Document and publish detailed, aggregated and interpreted data in a FAIR way

o Develop suitable models and engineering correlations and integrate them in a suitable open risk assessment toolkits

o Provide enhanced recommendations for safe design and operations of LH2 technologies

o Support international SDOs in

• updating of existing standards or

• developing of new international performance based and risk informed standards

o Document and disseminate the enhanced state-of-the-art


Advisory Board

CoordinatorWP1 lead

KITJordan

WP2 leadAL

Jallais

WP3 leadNCSRD

Venetsanos

WP4 leadHSL

Hawksworth

WP5 leadKIT

Kuznetsov

WP6 leadUU

Molkov

KIT AL UU NCSRD UWAR HSL INERIS

HYSAFE

PS

DeputyKIT / Jedicke

General Assembly

Coordination Committee

FCH 2 JU

Governance


WP6 – Technical Implementation

WP1 –Management

WP2 - Technical Strategy & Evaluation

WP5 –Combustion

WP3 –Release &

Mixing

Advisory Board

WP4 –Ignition

General Approach


WP1 –Management

(KIT)

WP2 - Technical Strategy & Evaluation (AL)

WP5 –Combustion

(KIT)

WP3 –Release &

Mixing (NCSRD)

WP6 – Technical Implementation (UU)

Advisory Board –

(HySafe)

WP4 –Ignition(HSE)

T2.1 – Scenario & Phenomena

Ranking

T2.2 – Analysis ofStandards and

RegulationsT2.3 – Refinement

of Program

T3.2 –Simulations

T3.3 –Experiments

T6.1 –Update ofHandbook

T6.2 –Implementation of

Engineering Correlations

T6.3 –White papers

T1.1 –Contract

& Financials

T1.2 –Internal

Communication & Meetings

T1.3 –External

Communication & Dissemination

International Alignement

Technical Consultancy

SustainableExploitation

International Communication

T3.1 -Theory & Analysis

T4.2 –Simulations

T4.3 –Experiments


T5.2 –Simulations

T5.3 –Experiments


International Standardisation


PRESLHYExploitation & Dissemination

Activities

Management(WP1)

Implementation(WP6)

Task 1.3 Website

Data Manage

ment

Engineering tools Handbook Guidelines RCS Recom-

mendationsWhite Paper

Task 6.6 Dissemination

Conference

Outreach


HySafe (+ Hydrogen Safety Panel)

RCS SCGJRC

(HIAD)ISO TC

197IEA HIA Task 37

US DOE

WP1 –Manage-

ment(KIT)

WP2 - Strategy (AL)

WP5 –Combus-

tion(KIT)

WP3 –Release & Mixing(NCSRD)

WP6 – Implementation (UU)

WP4 –Ignition(HSL) PRESLHY –

Advisory Board

External Networking


WP1 - Update• Representation of consortium at Review Days 2018

in Brussels 16/17 November 2018; no poster, but listed in H2FC JU Success Stories Reportwww.fch.europa.eu/sites/default/files/FCHJU-successstories-brochure-WEB-fin.pdf

• Major revision of the website ISP and CMS Wordpress(currently running V5.1) providing better performance andnew safe email services

http://www.fch.europa.eu/sites/default/files/FCHJU-successstories-brochure-WEB-fin.pdf


WP1 - Update• CA still do be signed by KIT legal officers

copies to be distributed in M15

• ISO/PWI 24077 „Safe Use of LH2 in Non-Industrial Settings“ established(after presentation at 27th plenary meeting in Vancouver, 6th December 2018)

Email of the ISO TC 197 chairperson Andrei V. Tchouvelev dated 15 January 2019:

“I am happy to inform you that ISO Central Secretariat, per the resolution of ISO/TC 197, has assigned a number to the PWI on the safe use of LH2 in non-industrial settings – ISO/PWI 24077 with Dr. Thomas Jordan (HySafe) as the Project leader. Please use this number for reference in regards to this PWI. Congratulations! (Delivered as promised :))

I must say this is the first such PWI that is directly related to a PNR international project. We have broken a new ground that gives the project direct and formal entrance to the leading international SDO. I hope this unique opportunity will be realized to its full potential.

Regarding the use of the PRESLHY project results for the purpose of this PWI, certainly a contribution to the revision of ISO/TR 15916 is an option. However, a development of a standalone TR could be another attractive option – this is too early to predict and it will be determined by TC197 once and if a new work item proposal (NWIP) with a Working Draft or at least a TOC has been developed and submitted.”


WP1 - Update

• Proposal of a safety distance benchmark „LH2 based HFS“by Air Liquide

• Proposal for next site visit:Air Products Liquifier Site in Rotterdam

• CC Meetings 8 to 12 organised via POWWOWNOW, later via GotoMeeting


Next Meetings

Special session(s) on LH2 safety expected.

9 abstracts (KIT, PS, UU, NCSRD, KIMM, SNL, UniTokio)Full paper due by end of M15


Advisory BoardName Company

InstitutionNation Expertise

Derek Miller Air Products US IndustryAndrei Tchouvelev AVT CAN General Expert, SDO (ISO), SMEKlaus Schäfer DLR D Large Scale User, General ExpertFranz Grafwallner ET D Aerospace ExpertTrygve Skjold GexCon N Modelling Expert, SMEKarl Verfondern Jülich D General Expert, ResearchShoji Kamiya KHI JP Industry, Naval applicationSalvador Aceves LLNL US Research, Cryo-compressedLee Philips Shell UK IndustryEthan Hecht SNL US ResearchChristoph Haberstroh Uni Dresden D CryoOlav Hansen Loyds N General Expert, Naval, InsuranceEtienne Studer CEA F Research, General ExpertJulien Salvat TME BE Industry, AutomotiveJens Franzen Daimler D Industry, AutomotiveMike Johnson DNVGL N Industry, InsuranceGerd-Michael Würsig DNV GL D Insurance, Naval applicationPietro Moretto JRC NL EC, ResearchVolker Schröder BAM D SDO, Regulation (national)Steve Woods NASA US Research, Aerospace Expert

New, byelectronic

voting

Suggested


todayGantt Chart with Deliverables


todayGantt Chart with Milestones

Delays in WP3,4 and 5 experiments because of

delayed delivery, manufacturing of components

and several requests forchanges for the experiments


Table of Deliverables at M15

today


Deliverable 1.3 – Data Management Plan – Version 1.5


Experimentalsub-program

Localrepository

INERIS


Localrepository

KIT


Localrepository

HSL

WP3

,4,5

DMP - Internal Data Management


Select, edit

transfer


Localrepository

INERIS


Localrepository

KIT


Localrepository

HSL

WP2

,6

WP3

,4,5

DOI

DMP - Preparing


Long termrepository

Select, edit

transfer


Localrepository

INERIS


Localrepository

KIT


Localrepository

HSL

WP1

,2,6

WP3

,4,5

DOI

RADAR Services(alternatively

KITopen)

DMP - Preparing


PRE302KIT001DEVISE181001.EXT1 integer forwork package, 3=WP3 for

release andmixing

4=WP4 forignition

5=WP5 forcombustion

2 integers =number ofexp. serieswithinworkpackage

Partner„KIT“, „HSL“or „INR“ (for INERIS)

3 integers =numberof experimentwithin series(0=metafile, seriesdescription)

6 charactersindicatingmeasuredquantity andlocation or device(„P#0008“, or„T#0001“, „PHOTRN“ „NIKON_“,..)details in metafile

6 integersfor date(YYMMDD) ortimestamp(in particular forphotographs)

Standardfile extension(e.g. „txt“, „jpg“, „avi“,…)

DMP – File Name Convention

Length 24.3


DMP –Metafile Templatep.1/2


DMP –Metafile Templatep.2/2


Repositories

RADAR services for 25 years and the estimated 2 TB storage:https://www.radar-projekt.org/display/RE/2016/05/09/Updated+price+information

25 x 500 Euro = 12500 Euro net+ per 1 Gigabyte published data2000 GB x 6,37 = 12740 Euro net______________________________

Total: 25240 Euro net

KITopen services are free (initially limited to 10 years)https://www.bibliothek.kit.edu/cms/english/kitopen.php


Data Input Interface for KITopen


Nomination of Data Management Team

− KIT: T. Jordan− Pro-Science: A. Friedrich− HSL: ?− INERIS: ?− WP2: E. Vyazmina− WP3: A. Venetsanos− WP6: D. Cirrone


WP5 –Combustion

WP3 –Release &

Mixing

WP4 –Ignition

Original extended experimental program for…


WP/Exp. Nr.

Phenomena/Name

Issue addressed/Objective

To be investigated Variation of Range ofvariables

n ofvariations

Partner/Test facility

WP3 Release andMixing

E3.1 Small ScaleMulti-phaseRelease

Discharge Coefficientsof Pressurized or LH2Releases

pressure changes in bulk vesseltemperature changes in a jetmass flow rateinertia (thrust), weight

Initial pressure 0-200 bar(sub-critical &supercritical)

4 KIT/HYKA-H8(He)

DISCHA-facility in Testchamber

V = 2.867 dm³BOS images, laser diagnostics of jetprinciple structure, potential wallattachment/ impingement

Initial temperature 25-200K 4

Nozzle shape and cross-sectional area

4

Extraction point(high/gaseous-low/liquid &middle)

3

E3.2 Multi-phaseHigh PressureRelease

Charcterisation ofPressurised LH2releases usingcharacteristic pipediameters

Pressure, temperature,release type (length anddiameter, orientation,thrust, discharge coefficient

0-1000 bar?(or highestpressurepossible)

t.b.d. HSL/Suitable vesselrequired/system required

Scale up of E3.1 wrtinventory, releaserates & p

E3.3 Mid-ScaleMulti-phaseRelease

LH2 jets/near fieldcloud dispersion

flash rate, momentum, velocity(Temperature pressure andconcentration measurements in thenear field from 0 to 1m),Cloud dispersion : temperature etconcentration measurements (fieldinstrumentation ~10 m)

orifice size , pressure 5/15 mm ; 0-10bar

3 x 3 INERIS/2 m3 vessel + 20 m line(1"ID)+dischargevalve+calibrated orifice

E3.4 Pool of LH2 Evaporation a spill ofLH2

evaporation rate, cold gas mixing,O2 entrainment

Material of the ground solid-liquid-porous

3 KIT/HYKA-H110(N2)

1 m2 BOS imaging Initial temperature 77-300K 3temperature profile in a gasconcentr. profile in a gas

E3.5 Rainout Tests LH2 Sprayevaporation/ Poolformation

evaporation rate, pool formation release height 3 HSL/Pool facility

releaseup/down/horizont.

3

WP3 Release (experiments set italic are in reserve because of budgetary constraints)


WP/Exp.Nr.

Phenomena/Name

Issue addressed/Objective


n ofvariations


WP4 Ignition

E4.1 Generalignition

fundamental ignitionparameters (MIE,AIT)

influence of the adiabatic mixing temperature on the standard ignition parameters

Concentration/temp 4 to 75% H2,-100°C toambient(adiabaticmixing)

10concentrations/temp

INERIS/Available mixing nozzle

E4.2 Electrostaticignition in coldjet

Pressurized LH2 jet Electrostatic measurements Initial pressure 0-200 bar KIT/HYKA-A1

"Paul Coupe"-Facility

Auto-ignition mechanism Initial temperature 33-200K

BOS images of the jet Nozzle diameter

H2 concentration profileE4.3 Electrostatic

ignition in coldplume

Large scale cold cloud(combination withE3.5)

Electrostatic measurements 6 HSL/same as 3.5

Auto-ignition mechanism

BOS images of the plumes

H2 concentration profileE4.4 Ignition above

poola spill of LH2 ignition position Material of the ground solid-liquid-

porousKIT/

HYKA-H110

1 m2 BOS imaging Initial temperature 77-300K same as E3.4

temperature profile in a gasE4.5 Condensed

phase ignitionIgnition ofLH2/LOX/solidoxygen mixtures

Composition, energy and types of ignition source

Produce under idealised conditions to understand sensitivity and conditions for ignition.

HSL/Blast test facility

E4.6 Diffusionignition ofCcH2

Pressure limits forspontaneous ignition

Influence of temperature pipe diameter, length, orifice shape

Initial p, T; pipe diameter, length, orifice shape, position of rupture membrane

KIT or HSL

WP4 Ignition (experiments set italic are in reserve because of budgetary constraints)


WP/Exp. Nr.

Phenomena/Name

Issueaddressed/

Objective


n ofvariations


WP5 Combustion

E5.1 Jet Fire Pressure andheat radiationeffects

Effects of variations onheat flux and dosis, temperature, maxpressure and rise rate

Mass LH2 /initial pressure

0-200 g/0-200 bar

3 KIT/DISCHA in HYKA-V220

Measured with Nozzle diameter 1-4 mm 3 Q160 or H110High speed video, BOS, pressure andradiation probes (bolometers)

Ignition location 0-2m 5 (similar E3.1)

Ignition delay times 0-1s 4

E5.2 Flame accelerationand

H2-air mixturein

Critical conditions for FA H2 concentration H2concentration

KIT/HYKA-H110

DDT at cryogenictemperatures

obstructed tube50 mm id

Critical conditions for DDT Initial temperature 50-200K or HYKA-Q160

Flame dynamics Initial pressure 1-5 barSchlieren imagesPressure measurements

H2-air mixturein congestedtube 0.7m id

Initial temperature H2concentration

E5.3 Flame propagationover a spill of LH2

3x9 m2 floor Flame dynamics (video), Pressuremeasurements, Temperaturemeasurements, BOS images

Initial temperature,Evaporation rate (derived inE3.4)

33-300 KIT/HYKA-H110(same as E3.4 and E4.4)

E5.4 BLEVE LH2 Max radius of fireball Mass LH2 0-100 g KIT/HYKA-V220

Max. time of fireball ignition delay 0-2 s or HYKA-V3Dynamics of fireball Initial pressure 1-10 barPressure outside

E5.5 Flame propagationin obstructed/confined coldcloud

FA and DDTwith realgeometricalconstraints

Flame dynamics (video), Pressuremeasurements, Temperaturemeasurements, BOS images

Congestion,confinement,

inventory,ambient conditions

tbd tbd HSL

WP5 Combustion (experiments set italic are in reserve because of budgetary constraints)


Documents

WP1 – Management 3rd General Meeting€¦ · 5 PRESLHY 3rd General Meeting, 7- 8 March 2019, Bergen, Norway. WP1 – Management (KIT) WP2 - Technical Strategy & Evaluation (AL)