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Logo PROGETTO UE COMETHY

COMETHY

Compact Multifuel-Energy To Hydrogen converter

Informazioni Generali

Coordinatore:
ENEA (Italia)
Responsabile:
GIACONIA ALBERTO - TERIN-DEC-H2V (CASACCIA)
Ruolo ENEA:
COORD
Sito WEB:
Sito WEB non disponibile

Programmi Europei

Programma:
Settimo Programma Quadro R&ST (2007-2013) -> JTI - Hydrogen (CP - Progetto di collaborazione)

Descrizione e Attività

Descrizione Generale

Sustainable decentralized hydrogen production requires development of efficient fuel-flexible units adaptable to renewable sources. CoMETHy aims at developing a compact steam reformer to convert reformable fuels (methane, bioethanol, glycerol, etc.) to pure hydrogen, adaptable to several heat sources (solar, biomass, fossil, refuse derived fuels, etc.) depending on the locally available energy mix. The following systems and components will be developed: • a structured open-celled catalyst for the low-temperature (< 550°C) steam reforming processes • a membrane reactor to separate hydrogen from the gas mixture • the use of an intermediate low-cost and environmentally friendly liquid heat transfer fluid (molten nitrates) to supply process heat from a multi fuel system. Reducing reforming temperatures below 550°C by itself will significantly reduce material costs. The process involves heat collection from several energy sources and its storage as sensible heat of a molten salts mixture at 550°C. This molten salt stream provides the process heat to the steam reformer, steam generator, and other units. The choice of molten salts as heat transfer fluid allows: • improved compactness of the reformer; • rapid and frequent start-up operations with minor material ageing concerns; • improved heat recovery capability from different external sources; • coupling with intermittent renewable sources like solar in the medium-long term, using efficient heat storage to provide the renewable heat when required. Methane, either from desulfurized natural gas or biogas, will be considered as a reference feed material to be converted to hydrogen. The same system is flexible also in terms of the reformable feedstock: bioethanol and/or glycerol can be converted to hydrogen following the same reforming route. The project involves RTD activities ion the single components, followed by proof-of-concept of the integrated system at the pilot scale (2 Nm2/h of hydrogen) and cost-benefit analysis.

Attività svolta da ENEA

L'ENEA coordina il progetto ed è coinvolta in tutte le attività di ricerca, sviluppo sperimentale e dimostrazione previste nel workpackage 6 che costituiscono il piano di lavoro.

Dati Finanziari (in euro)

Costo Eleggibile

Progetto:
4.318.737,80
ENEA:
676.127,00

Contributo

Progetto:
2.484.095,00
ENEA:
436.773,00

Durata del Progetto

Anno di stipula e Durata:
2011 - 36 mesi
Periodo:
01-12-2011 -> 30-11-2014

Partner (12)

Ruolo Nome Nazione
GKN SINTER METALS ENGINEERING GMBH Germania
IKTS FRAUNHOFER INSTITUTE FOR CERAMIC TECHNOLOGIES AND SYSTEMS Germania
CERTH - CENTRE FOR RESEARCH AND TECHNOLOGY HELLAS Grecia
UNIV. ARISTOTLE OF THESSALONIKI (AUTH) Grecia
ACKTAR LTD Israele
TECHNION ISRAEL INSTITUTE OF TECHNOLOGY Israele
PROCESSI INNOVATIVI SRL Italia
UNIV. CAMPUS BIOMEDICO DI ROMA Italia
UNIV. ROMA LA SAPIENZA (UNIROMA1) Italia
UNIV. SALERNO Italia
ECN ENERGY RESEARCH CENTRE OF THE NETHERLANDS Paesi Bassi
COORD ENEA Italia

Keyword CORDIS (2)

Keyword Argomento
Hydrogen production Energy
RENEWABLE SOURCES OF ENERGY Energy

Altre Keyword (0)

Nessuna altra keyword disponibile

Disp.comm. 255/2013: aumento del contributo finanziario a ENEA di 85.305,08 per un totale di 436.773 euro