PROMECA Overall presentation of the project Vincenzo Palma - - PowerPoint PPT Presentation

ENERGY ANALYSIS AND MODELING OF MEMBRANE REACTORS

PROMECA Workshop 2017

ENERGY ANALYSIS AND MODELING OF MEMBRANE REACTORS

PROMECA Workshop 2017

Consortium Partners

Associat e professor –Depart ment of Industrial Engineering –Universit y of S alerno Vincenzo Palma

PROMECA ‐ Overall presentation of the project

PROMECA PROcess intensification through the development of innovative MEmbranes and Catalysts Project number: 734561

Research and Innovation Staff Exchange (RISE) Call: H2020-MSCA-RISE- 2016 Start date: 01/01/2017 End date: 31/12/2020 Duration: 48 months 3 academia and 3 industrial partners in 4 European countries

Total EU financing € 688,500

3 academia and 3 industrial partners in 4 European countries

2 research centers/ academia, TEC and TUE, together with the industrial end user ICI, will provide competences on design, development and testing

• f

membranes in a prototype membrane reactor for hydrogen production 2 research centers/ academia, UNISA and TUE, together with the technology integrators and industrial end users KT and AL will contribute with highly qualified experiences

• n

design, development and testing of advanced catalysts to endothermic and exothermic processes intensification All academic and industrial partners will be involved in fostering the knowledge in energy analysis and process modelling in support

• f process design, integration, and

testing

Project Structure

WP n. Work Package Title Activity Type N.

• f

persons- months involved Start Month End Month 1 Project Management, Communication and Dissemination Management, Communication & Dissemination 13 1 48 2 Models and Energy Analysis Research & Training 55 3 36 3 Membrane design & development Research & Training 32 3 36 4 Catalyst design & development Research & Training 29 3 36 5 System integration and validation Research & Training 37 24 48

Participant Short name

UNISA TUE TECNALIA ICI KT AL

Work Package involved

1, 2, 4, 5 1, 2, 3, 4, 5 1, 2, 3, 5 1, 2, 3, 5 1, 2, 3, 4, 5 1, 2, 3, 4, 5

Person-months per participant

3 + 13 + 11 + 6 2 + 8 + 12 + 10 + 10 1 + 2 + 9 + 4 2 + 15 + 7 + 7 2 + 11 + 3 + 5 + 5 2 + 6 + 1 + 3 + 5

TOK team I (at KT, TUE, and AL premises): Energy Analysis and Modelling TOK team II (at UNISA and AL premises): Catalysts TOK team III (at TECNALIA and ICI premises): Membranes Group leader KT Group leader UNISA Group leader TECNALIA Supervisor TU E Supervisor AL Supervisor ICI Academic members TUE: TUE1, TUE2, F.Gallucci, Vincenzo Spallina, Niek De Noijer, Ivo Roghair TECNALIA: E. Fernandez, TECNALIA1, TECNALIA 2 UNISA: Vincenzo Palma, UNISA1, UNISA2, UNISA3 13 Academic member UNISA: Vincenzo Palma, UNISA1, UNISA2, UNISA3. TUE: F.Gallucci, Maria Nordio, TUE3, Marian san Pio, Martin van Sint Annaland 9 Academic members TUE: F. Gallucci, Maria Nordio, Niek de Noijer, Kai Coenen, Alba Arratibel, TUE4 TECNALIA: J. Zuniga, A. Pacheco,

• E. Fernandez, TECNALIA1,

TECNALIA 2, TECNALIA 3 12 Industrial members KT: G. Iaquaniello, E. Palo, L. Mosca, KT1, KT2, KT3 ICI: S.Argenton, G.Fares, C.Tregambe, ICI1, ICI2, ICI3, ICI4 AL: P. Pullumbi, M. Basin, S. Valentin,

• D. Tudorache, AL1

18 Industrial members KT: E. Palo, L. Mosca, KT1, KT2 ICI: C.Tregambe, ICI1, ICI2, ICI3, ICI4 AL: P. Pullumbi, F. Bellencontre, F. Brandani, AL1, AL2 14 Industrial members KT: G. Iaquaniello, E. Palo, KT1, KT3 ICI: G.Fares, C.Tregambe, ICI1, ICI2, ICI3, ICI4 AL: P. Pullumbi, M. Basin, AL2 13 TOT group I 31 TOT group II 23 TOT group III 25

• Necessary to define the TOK programme and the research set-up for

the project

Phase 1 - Competence analysis

• Compare the energy efficiency of the new system based on membrane reactors to benchmark
• technologies. The results of this analysis will define the operating conditions of the new catalysts

and membranes and reactors.

• It will be led by KT (company leader in technology integration, plant design, simulation, analysis

and realization) and supervised by TUE (European excellence in research on integrated membrane reactors), to ensure a proper mix of scientific and industrial approach, and mainly developed by Group 3

Phase 2 – Energy analysis and Modelling

• will include the work in parallel of i) Group II on membranes, led by TECNALI A (leader in

membrane development for industrial reactors) and supervised by AL, bringing its long standing knowledge on membranes in several industrial applications (gas, water, etc.); and ii) Group III on catalysts, led by UNISA (experts in heterogeneous catalysis, development and testing of advanced catalysts for industrial processes), and ICI, company bringing expertise on medium and small-scale industrial reactors for hydrogen production

Phase 3 – Development of reactor components

• The final Phase of the project, in which all the models, materials and components

will be integrated in the final PROMECA reactor prototype (capacity 1Nm 3/ h of pure hydrogen), which will be designed, constructed and tested

Phase 4 - Integration, test and validation

• Development of structured catalyst with high heat conductivity and low pressure drop,

through the use of ceramic or metallic supports in shape of monoliths or foams, and active species, properly deposited on them, able to perform the desired process

• Partners involved: UNISA, TUE, KT and AL

Advanced catalysts – WP4

• Development
• f highly permeable and selective ultra-thin (4µm)

Pd-based supported membranes, stable under reactive conditions

• Partners involved: TUE, ICI, Tecnalia, KT and AL

Innovative membrane – WP3

• Development of new processes based on the novel catalysts, novel membranes and the

combination of the two

• Partners involved: UNISA, TUE, ICI, Tecnalia, KT and AL

Catalyst and membrane integration – WP5

• Energy analysis and Modelling of the different novel processes
• Partners involved: UNISA, TUE, ICI, Tecnalia, KT and AL

Energy analysis and modelling – WP2

• Proof of concept of the integrated PROMECA system, validated with modelling based on the

experimental results

• Partners involved: UNISA, TUE, ICI, Tecnalia, KT and AL

System validation – WP5

• Cost analysis and comparison with benchmark technologies
• Partners involved: UNISA, TUE, ICI, Tecnalia, KT and AL

Cost analysis – WP5 Main Objectives

The financial support is composed of a staff member unit cost of 2,000 EUR per month, plus an institutional unit cost of 2,500 EUR per person-month.

Financial support

The institutional unit cost is split into research, training and networking costs of 1,800 EUR per month of secondment, and management and indirect costs of 700 EUR per month.

Marie Skłodowska- Curie Action Staff member unit cost [per person-month

• f secondment]

[EUR] Institutional unit cost [per person-month of secondment] Research, training and networking costs [ EUR] Management and indirect costs [ EUR] RISE 2,000 1,800 700

Financial support

Participant Short name

UNISA TUE TECNALIA ICI KT AL

Person-months per participant

30 40 15 29 25 15

Budget per participant

Financial support

BENEFICIARY PARTNER COST (€) BENEFICIARY PRE PAYMENT (JANUARY 2017) (€) DIFFERENCE (€) UNISA € 135,000.00 € 81,000.00 € 54,000.00 TU/ E € 180,000.00 € 109,200.00 € 72,000.00 KT € 108,000.00 € 64,800.00 € 43,200.00 ICI CALDAIE € 130,500.00 € 78,300.00 € 52,200.00 TECNALIA € 67,500.00 € 40,500.00 € 27,000.00 AIR LIQUIDE € 67,500.00 € 40,500.00 € 27,000.00 total € 688 500 00 € 413 100 00 € 275 400 00

EU Prepaym ent ( January 2 0 1 7 ) : € 4 1 3 ,1 0 0 .0 0

Scientific Deliverables Deliverable No Deliverable Title WP No Lead Beneficiary Short Name Type Dissemination Level Due Date D 2.1 Report on the influence of integration level membrane/ reactor on process development 2 KT Research CO M10 D 2.2 Report on preliminary economic analysis and overall technology assessment 2 KT Research CO M24 D 2.3 Process design package 2 KT Research CO M36 D 3.1 First and second generation membranes 3 TECNALIA Research CO M28 D 3.2 Final membranes for lab-scale prototype 3 TECNALIA Research CO M36 D 4.1 First and second generation catalysts 4 UNISA Research CO M28 D 4.2 Catalytic activity tests with the final catalysts 4 UNISA Research CO M36 D 5.1 Report on design and 3Ddrawing of the PROMECA reactor 5 ICI Research CO M30 D 5.2 Report on tests 5 ICI Research CO M48 D 5.3 Report on industrialisation aspects, including techno-economic analysis 5 ICI Research CO M48 D 5.5 Report on available models for membrane reactors (including heat management). 5 ICI Research CO M48

Management, Training, and Dissemination Deliverables

Deliverable No Deliverable Title WP No Lead Beneficiary Short Name Type Dissemination Level Due Date D 1.1 PROMECA project web site, communication and dissemination plan 1 UNISA Management CO M3 D 1.2 Progress report at M12 1 UNISA Communication & Dissemination PU M12 D 1.3 Progress report at M36 1 UNISA Management & Training CO M36 D 1.4 Mid term meeting 1 UNISA OTHER CO M18 D 1.5 Preliminary roadmap for collaboration and R&D and durable knowledge network (preliminary collaboration plan, IPR agreement) 1 UNISA Communication & Dissemination CO M12 D 1.6 Competence Analysis and preliminary research plan, TOK, staff exchange and Training plans 1 UNISA Management PU M6

Consortium Partners

Thank you for your attention

FOR MORE INFORMATION: Vincenzo Palma - vpalma@unisa.it