01/04/2014 / page 1 (disclosure or reproduction without prior permission of ferret is prohibited). a...

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01/04/2014 / Page 1 (Disclosure or reproduction without prior permission of FERRET is prohibited). A Flexible natural gas membrane Reformer for m-CHP applications FERRET This project is supported by the European Union’s Seventh Framework Programme (FP7/2007-2013) for the Fuel Cells and Hydrogen Joint Technology Initiative under grant agreement nº 621181 Duration: 3 years. Starting date: 01-Apr-2014 Contact: [email protected] The present publication reflects only the author’s views and the FCH JU and the Union are not liable for any use that may be made of the information contained therein.

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Page 1: 01/04/2014 / Page 1 (Disclosure or reproduction without prior permission of FERRET is prohibited). A Flexible natural gas membrane Reformer for m- CHP

01/04/2014 / Page 1 (Disclosure or reproduction without prior permission of FERRET is prohibited).

A Flexible natural gas membrane Reformer for

m-CHP applications

FERRET

This project is supported by the European Union’s Seventh Framework Programme (FP7/2007-2013) for the Fuel Cells and Hydrogen Joint

Technology Initiative under grant agreement nº 621181

Duration: 3 years. Starting date: 01-Apr-2014Contact: [email protected]

The present publication reflects only the author’s views and the FCH JU and the Union are not liable for any use that may be made

of the information contained therein.

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Summary

FERRET aims at developing a high efficient heat and power cogeneration system based on:

i) design, construction and testing of a flexible advanced reformer for pure hydrogen production from a broad range of natural gas with optimization of all the components of the reformer (catalyst, membranes, heat management etc) and

ii) the design and optimization of all the BoP for the integration of the novel reforming technology in a CHP system.

The main idea of FERRET is to develop a novel more efficient and cheaper multi-fuel membrane reformer for pure hydrogen production in order to intensify the process of hydrogen production through the integration of reforming and purification in one single unit

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Partnership

Multidisciplinary and complementary team: 6 top level European organisations from 4 countries: 3 Research Institutes and Universities and 3 top industries in different sectors (from hydrogen production to catalyst developments to boilers etc.).

TU/e, Netherlands TECNALIA, Spain POLIMI, Italy ICI, Italy HyGear,

Netherlands Johnson Matthey

(UK)

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Scale-up of membranes and development of new pore-filled membranes more resistant to fluidized bed membrane reactor configuration and using less amount of Pd per m3/h of hydrogen production

Reduction of fuel processor costs Development of methods for recycling and repairing of Pd-

based membranes Improvement of catalyst for reforming of different natural gas

compositions Scale up the catalyst production for fluidized bed applications Improvement of a novel fluidized bed membrane reforming

reactor of different natural gas compositions Improvement of a novel fluidized bed membrane reforming

reactor for long-term performance. Protection of Fuel cell stack (e.g. Cr release), CO poisoning Integration of the novel reforming in a CHP system Optimization of the BoP for the novel reforming CHP system Simulation and optimization of the reformer integration with

the entire system

Project objectives

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Work structure

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Partnership synergies

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Catalyst development

Develop an autothermal reforming catalyst to convert a mixture of natural gas, steam and air into syngas (hydrogen, carbon monoxide, carbon dioxide, nitrogen).

The catalyst needs to be mechanically durable and operate as a fluidized bed inside a membrane reactor.

The catalyst needs to maintain activity under membrane reactor operating conditions.

Scale up of catalyst production

Objectives:

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Membranes development

Development of Pd based tubular membranes, for application in natural gas autothermal reforming catalytic membrane reactors

Improved flux and selectivity

Temperature 600ºC

Improved sulphur resistance

Resistant to fluidization regime

Process scaling up

Objectives:

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Pd

Al

AlThin Pd film membrane

Pore-fill type Pd membrane

Thin Pd film membrane

Pore-fill type Pd membrane

Advantages of pore filled over conventional membranes

- Less Pd is used ( a fraction of conventional)- Protection under fluidization regime

Membranes development

Composite nano porous membranes Packed with Palladium panoparticles (pore filled membranes)

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Selection of ATR-CMR components: catalysts, membranes and supports, and sealing based.

Integration of these elements in lab scale reactors specifically designed for ATR.

Validation of the lab scale reactors performances and identification of the best design for prototype pilot.

Lab scale reformer

Objectives:

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Objectives:

Design the pilot scale catalytic membrane reactor (CMR)

Construct and assemble the pilot scale catalytic membrane reactor including controls

Perform functionality tests before integration into Fuel Cell CHP-system

Pilot scale catalytic membrane reformer

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Challenges

• Fluidization regime• Hotspots• Adequate back-mixing• Slugging• Kinetic limitations• Membrane area• Manifolding• Sealing

Pilot scale catalytic membrane reformer

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Integration & Validation in CHP-

System definition of fuel cell CHP-model based on existing fuel cell CHP-system and validate system model with test results

Integrating the FERRET reformer into existing CHP-system Evaluation of the FERRET CHP-system feeding different natural

gas compositions Compare performance of the FERRET CHP-system with existing

CHP-system Perform techno-economic analysis of the FERRET CHP-system

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A Flexible natural gas membrane Reformer for

m-CHP applications

FERRET

Thank you for your attention

Contact: [email protected]