Introduction to portfolio of Hydrogen Production, Distribution and Storage projects. Nikolaos Lymperopoulos, Project Manager

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Transcription:

Introduction to portfolio of Hydrogen Production, Distribution and Storage projects Nikolaos Lymperopoulos, Project Manager

AGENDA Day 2 Afternoon

2008-2013 MAIP Energy RTD H 2 Production & Distribution Public Awareness, Education Market Support (SME Promotion, Demand Side Measures, etc.) Vehicles & Infrastructure Low Carbon Supply Chain Demonstrations System Readiness Manufacturability Backup/UPS Off-road H2 Vehicles Micro/Portable FC Technology, Sustainability & Socio-Economic Assessment Framework Stack & Subsystems Specific PNR & Harmonised RCS Research and Technological Development Processes & Modules Periphery & Components Systems & Integration & Testing Components New Technologies Material & Design & Degradation & Durability Long-term and Breakthrough Orientated Research Transport & Refuelling Infrastructure Hydrogen Production & Distribution Stationary Power Generation & CHP Early Markets

2008-2013 MAIP Targets Energy H 2 Production & Distribution Actual 43 9.6 52.6 12.1%

2008-2013 MAIP Targets Energy RTD H 2 Production & Distribution RTD H 2 43 M 10% CROSS- CUTTING 28 M 6.4% TRANSPORT 194 M 45.1% ENERGY 209 M 48.5% 432 M FCH JU Contribution/M RTD H 2 24 projects 15.5% ENERGY 90 58,1% CROSS- CUTTING 26 16,8% TRANSPORT 39 25,2% 155 projects No. FCH JU projects per pillar

Overview of Panel 5 Projects Topic 2010 2011 2012 2013 2014 2015 2016 2017 Alkaline electrolysis PEM electrolysis High temp electrolysis Concentrated solar Photo-electrochemical Reformers Biomass gasification Biological H2 storage (boron+mh) H2 tanks & distribution H2 bulk storage Studies ADEL RESΕLYSER ELECTROHYPEM NOVEL HELMETH SOPHIA ELECTRA SOL2HY2 ARTIPHYCTION PECDEMO COMETHY NEMESIS2+ BioRobur UNIfHY HYTIME BOR4STORE EDEN DeliverHy HyTransfer HyUnder ELY ES GH

Electrolysers - 1 Alkaline (RESELYSER) Novel cells for variable operation minimizing gas crossover at low current density to 25% Aiming for >80% η retention >90% over 1,000 on/off High temperature (ADEL, HELMETH, SOPHIA, ELECTRA) Completed: 6-17/kg H 2, 1.33 A/cm2, 1-5% degradation / 1,000 hours Recent: 0.5-1% degradation / 1,000 hours, total η >85% electricity -> syngas, coupling to concentrated solar source

Electrolysers - 2 Study: Development of water electrolysis in the EU Energy system R&D interaction of el. with grid, benchmarks, test cycles Electrolyser system R&D part-load & dynamic operation for H2 customers and provision of energy services Electrolyser technology - reduce capex while maintaining reliability, increase performance (catalysts, membranes, systems) http://www.fch-ju.eu/page/publications

Concentrated Solar (SOL2HY2) Modelling, multi-objective design and optimisation and testing of improved critical materials solutions and processes, leading to a virtual plant model Sulphur depolarised electrolyser (selected), solarpowered H 2 SO 4 cracker (sun-tested) and heat storage (molten salts) 3 concepts chosen, critical BoP units selected, main blocks built using Aspen Plus S/W.

Photoelectrochemical (ARTIPHYCTION, PECDEMO) 2.5% - 5.2% sun-to-h 2 conversion η, 5-8% aim, 5% target 1,000h is aim, 10,000h target 100W 3g/h aim, 100W-100kW target

Reformers -1 Membrane reformer, 550 o C, integrating RE heat sources (COMETHY) Centralised SMR η > 70% aim, 72% target >2Nm 3 /h aim, 2-750 Nm 3 /h target <3vol% CO, <10vol% CO target Diesel, biodiesel reforming (NEMESIS2+) 70% η aim, 80% target, >1,000 h durability, 50Nm 3 /h prototype

Reformers -2 Biogas reformer (BIOROBUR) 100 kg/day aim, 50-250 kg/day target CO < 10 vol% aim and target Materials costs for 50 Nm 3 /h 150 k, target 250 k >65% η aim and target

Biomass gasification (UNIFHY) Continous process for pure H 2 production from biomass (gasifier+wgs+psa+thermal int) H 2 cost < 5/kg for 6,000h/year operation on plant, as per target 70% η aim, > 66% target

Biological routes (HYTIME) Dark fermentation of 2 nd gen biomass, continuous process 5L (6gr H 2 /day) reactor in operation, 50L ready for tests, 300L just purchased 1-10 kg H 2 /d aim and target 71% η from straw, 36% from grass, <10% kitchen waste, > 75% aim

H 2 storage : MH Boron hydride-based materials (BOR4STORE) 9-10 wt.% on material basis, >6 wt.%, 4% on system basis target Release temp 350-450 o C, 450 o C target Mg-based materials (EDEN) 7 wt.% on material basis, >6 wt.% target SOFC compatible, > 1.5 lt/min release

H 2 distribution Composite material trailers (DELIVERHY) Applicable safety factors from SF=3.0 -> SF=2.25 52.5 MPa most suitable, >40MPa target Delivery freq. x3, CO 2 x4, cost = LH 2 Faster filling (HYTRANSFER) CFD and lab testing Reduction of HRS OPEX and CAPEX

H 2 bulk storage Underground storage in salt caverns (HYUNDER) Technically feasible, suitable geology, public acceptance Cavern contributes 0.5/kg to cost of H 2 Short term: Transport sector only market for commercial operation of H 2 plant (electrolyser and storage)

Studies Energy Storage Green Hydrogen (just launched, 1/12/2014 deadline) http://www.fch-ju.eu/page/vacancies-procurement

Thank you for your attention!