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Elyntegration project overview Vanesa Gil

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Elyntegration project overview

Vanesa Gil

The Consortium • FHA (Coordinator, ES)

• IHT (CH)

• VITO (BE)

• Fraunhofer-IFAM (DE)

• Inycom (ES)

• IAEW-RWTH Aachen (DE)

19/06/2019 3 PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

ELYntegration – project overview

• Duration: September 2015 – May 2019

• The strategic goal of ELYntegration is the design and engineering of a:

– robust, flexible and cost competitive

– Multi Megawatt alkaline water electrolyser

– capable of producing - with a single stack - up to 4.5 ton

H2/day for energy applications.

19/06/2019 4 PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Overview

Objectives

AWE technical

developments

Testing

Communica

tion and

Awareness

Market and

business preparati

on

19/06/2019 5 PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Alkaline Water Electrolysis

• Cell design and improvements at stack level

high performance in a broad range of the electrolyser load

– Material development (electrodes , membranes)

– Topology and assembly of the final stack solutions

• Definition and design of an optimized balance of plant (BoP) for the dynamic operation

– Analysis of the BoP components and streams which could derive in lower costs of the system

– Participation of industrial and technological partners

• Advanced communication and control system

– Requirements of end-users

– Enhance the flexibility of the electrolyser providing grid services

19/06/2019 6 PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Testing

• Tested step by step and continuously during the project:

– from ex-situ characterization at laboratory level

– to in-situ testing at different scales (micro pilot to industrial size)

• The most promising results obtained in the project have been included in a final validation electrolyser working in an operational environment.

19/06/2019 7

Micropilot Pilot Industrial

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Highlights – Novel separator membranes

8

• Highly porous, compressible separator membrane

• low ionic resistance

• gas tightness thanks to compression in the electrochemical cell

Separator in un-compressed form Separator compressed in the cell

to 80% of its original thickness

Cross-section of a compressible separator

• Mixed matrix (organic-inorganic) composite membrane

• Textile reinforcement

• Pore template (60 nm/3000 nm primary grain size)

Advanced stack:

new separator membranes, 10 kW power PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Eight different membranes have been developed and tested at micropilot scale:

• 60 nm template particles; 750 μm, 1000 μm and 1250 μm.

• 3000 nm template particles; 750 μm (2 versions), 1000 μm 1250 μm (2 versions).

Two tested at pilot scale

One tested at industrial scale

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

In total:

Highlights – Novel electrodes • An innovative powder metallurgical (PM) route was used to coat a porous substrate (mesh and foam) with an

electrochemically active catalyst material (Mo, NiMo and Raney-Ni).

• The production was process was tested on industrial scale and a protocoll for safe handling was developed.

• The highest activity for the HER was obeserved for Raney-Ni electrodes (h300 (5 h) < 100 mV). The catalyst was very stabel attached to the substrate even after the AST tests.

PM route is suitable for the pproduction of hihgly efficient electrodes for GW electrolysis market.

Raney-Ni NiMo

Ni-substrate 1. Powder deposition 2. DT

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

In total: Three different kinds of electrodes have been developed at IFAM (Mo, NiMo and Raney-Ni) using a powder metallurgical route.

4 sets of electrode (Ni-, Mo-, NiMo- and Raney-Ni coated) tested at micropilot scale 2 sets of electrodes (NiMo and Raney-Ni)tested at pilot scale

Raney-Ni NiMo Mo

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

- pilot scale

Test benches commisioned at FHA

STACK

ELECTROLYSER

(10 kW)

Up to 60 bar and 95 ºC

Up to 25 KW and 3.5 Nm3/h

Remote control

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Testing at pilot scale

• Stack performance (characterization)

• Accelerated stress tests protocols

lifetime assessment under high dynamic loads

19/06/2019 PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252 13

Vref=VBOL@200A

1.00xVref

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Stack performance

Vref=VBOL@200A

Novel membranes

Novel electrodes

Vref=VBOL@200A

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

0.98

1.03

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0 500 1000 1500 2000 2500 3000 3500 4000 4500

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Vaverage_cycle 13 1.03xVref

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AST profile – stack membrane #1

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Accelerated load cycle

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PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

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2 months

providing

grid

services

(Finish

aFRR)

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

17

1.30xVref

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2 months providing

grid services (Finish

aFRR)

Novel electrodes

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

- industrial scale: up to 250 KW, 30 bar, 95 ºC

Test benches upgraded at FHA

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Highlights – Demo testing at industrial size

• Stack 4. New topology

(high dynamic power profile and grid services provision)

• Stack 3. State-of-the-art stack stak (grid services provision)

• Stack 2. Novel membranes

(high dynamic power profile and grid services provision)

• Stack 1. Commercial stack (C&CS validation)

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Stack performance – high dynamic power profile

19/06/2019 PUBLIC – ELYNTEGRATION G.A. 671458 20

CONFIDEN

TIAL

19/06/2019 21

30 bar

stand-by

53,125%

CONFIDEN

TIAL

CONFIDEN

TIAL

stand-by

I_up

25%(I_up-I_low) 50%(I_up-I_low)

75%(I_up-I_low)

I_low

CONFIDEN

TIAL

CONFIDEN

TIAL

Grid services provision

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Modelling and BOP cost optimization

• Once validated and demonstrated at prototype level, the advanced constructive features have been integrated in the design of a multi-MW single stack alkaline electrolyser.

• BOP cost and manufacturing optimization has been assessed

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Highlights – Cost optimization

6/10th upscaling method

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

KOH pumps 20%

Glycol pump

2%

Positive displaceme

nt pump 2%

Heat exchangers

20% Air-liquid cooler

1%

Heater 10%

Vessels 35%

Filters 10%

Cost in range [~80,000…~300.000€]

20% error considered

•“Duplicated” sizing strategy (based on simulations) 1 additional Heat exchanger

1 additional KOH pump

Validation: Grid services & Qualygrids protocols

· Carbon steel + epoxy resin coating in vessels

· Better efficiencies with nanostructured electrodes and

electrochemical compressors

· FHA experience to reduce instrumentation

· Containerization and transport

· External processes: Waste heat (2MWh) Oxygen gas (36 tpd)

High valorisation potential

Market and business preparation • Feasibility study and market potential assessment

– determine the best possible markets, sectors and countries for the final product

• The market study has been focus on the national policies towards renewable energy and energy storage, with special attention to electricity prices in the power market and the provision of grid services to minimize the cost of the hydrogen production.

• Exploitation strategy and business plan: After the results of the demonstration activities, the conclusions of the market study and the analysis of different business cases have been studied

19/06/2019 24 PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

• identified business models in power systems – spot market participation and provision of positive control reserve most

promising

– provision of grid services with potential, however subjected to significant short and medium term uncertainty

• main drivers for profitable electrolyser operation – hydrogen demand sectors with high hydrogen prices (e.g. mobility)

– high shares of renewable energies within power system

– high prices for CO2 emission certificates

– potential exemptions from specific end-user price component (network charges, taxes, levies)

19/06/2019 25

Highlights – Business models

PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Communication and Awareness

• Activities complementary to the exploitation strategy and business plan.

• Targets: policy makers, local authorities, technology providers, general public.

• The final goal is to develop awareness of the services and technology to be demonstrated in the project at each level, including energy transition problematic, grid flexibility and environmental aspects.

• Channels: website, leaflets, participation in specialized conferences and fairs.

• Public deliverables are also published and available in the project’s webpage.

19/06/2019 26 PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

Highlights - Communication

• World Hydrogen Technologies Convention, WHTC:

2 oral contributions (June 2019, Tokyo)

• World Hydrogen Energy Conference, WHEC:

Keynote lecture (June 2018, Rio Janeiro) and oral contribution (June 2016, Zaragoza)

• European Hydrogen Energy Conference, EHEC:

1 oral contribution (March 2018, Málaga)

• International Conference on Electrolysis (ICE2017), Iberconnapice (2016, 2017) Hannover Fair (2016,2017, 2018, 2019)

• Publications: 3 scientific open access papers published + 4 on-going

19/06/2019 27 PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252

19/06/2019 28

Acknowledgement

Thank you for your attention Vanesa Gil [email protected]

19/06/2019 29 PUBLIC – ELYNTEGRATION G.A. 671458. SERI 15.0252