dibanet concept networking day rio 2010 · wp3 –levulinic acid (and ethyl levulinate) reactor and...

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DIBANET Concept Development of Integrated Biomass Approaches Network The Production of Sustainable Diesel-Miscible-Biofuels from the Residues and Wastes of Europe and Latin America Prof. Michael H. B. Hayes University of Limerick, Ireland DIBANET Networking day, 13 December 2010

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Page 1: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

DIBANET Concept

Development of Integrated Biomass Approaches Network

The Production of Sustainable Diesel-Miscible-Biofuels from the Residues and Wastes of Europe and Latin America

Prof. Michael H. B. Hayes

University of Limerick, IrelandDIBANET Networking day, 13 December 2010

Page 2: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

SEVENTH FRAMEWORK PROGRAMME THEME: FP7-ENERGY.2008.3.2.1

“ Enhancing international cooperation between the EU and Latin America in the field of biofuels”

Grant Agreement For: CP-SICA Collaborative project

Page 3: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

EU & Latin America

� Share common needs and threats:�the increasing reliance on imported diesel fuels �annual increases in quantities of organic wastes.

� DIBANET is developing technologies to help towards eliminating the need for fossil diesel imports in either region,improving the security of energy supply.

� DIBANET is advancing the art in the production of ethyl-levulinate from organic wastes and residues.

� Ethyl levulinate (EL) is a novel diesel miscible biofuel (DMB) produced by esterifying ethanol with levulinic acid.

Page 4: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

Levulinic acid from lignocellulosic feedstocks

Page 5: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

DIBANET Partners

EUEU LALAUni. Of Limerick CTC

Aston Uni. UFRJ

Certh UBA

Ecosphere YPF

FOSS Embrapa

Geonardo Fundacion Chile

UNICAMP

There are 13 partners in the group, 6 from the EU & 7 f rom LatinAmerica. The total budget for the 42 project is €3.72 m. DIBANET is

co-ordinated by UL

Page 6: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

DIBANET members at recent project meeting in Buenos Aires, 2010

Page 7: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

5 Key Scientific Objectives

1. Optimise the yields of levulinic acid (and co-products), from the conversion of biomass, while minimising chemical/energy requirements. Levulinic acid is a platform chemical for the production of a Diesel Miscible Biofuel (DMB).

2. Improve the energy balance of the production of levulinic acid and the total biofuel yields possible from a feedstock by sustainably utilising the residues in pyrolysis processes to produce a bio-oil that will be upgraded to a (DMB).

Page 8: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

5 Key Scientific Objectives Cont’d

3. Reduce the energy and chemical costs involved in producing ethyl-levulinate from levulinic acid and ethanol.

4. Select key biomass feedstocks for conversion to levulinic acid, analyse these, and develop rapid analytical methods that can be used in an online process.

5. Analyse the DMBs produced for their compliance to EN590 requirements and, if non-compliant, suggest means to achieve compliance.

Page 9: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

Enhancing international cooperation

Four Co-Operation Objectives:1. Develop a tightly-integrated online network of key

players in the EU and LA2. Organise public meetings/forums between key

stakeholders from both regions3. Train PhD and post-doctoral researchers from the

opposite region 4. Develop an inter-regional Technology Transfer

Business Plan for the most effective exploitation of the DIBANET technologies. This will consider the combined needs of the EU & LA & the potential for trade.

Page 10: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

DIBANET Team

Page 11: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

Links created by DIBANET

Before After

Page 12: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

Advancement through co-operation

Page 13: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

DIBANET processes & products & their linkages

Page 14: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

WP1: Project Management

� to ensure the project keeps to the objectives.

Involves UL, Aston, Certh, Geonardo & UFRJ

Page 15: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

WP2: Feedstock for levulinic acid & DMB production

Objectives:� Selection of EU & LA biomass & waste feedstocks of

most value for the production of levulinic acid.

Miscanthus

Sugar cane bagasseRice husks

Involves UL, FOSS, CTC, Fundacion Chile & Unicamp

Page 16: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

Detailed chemicalanalysis Rapid NIR

Calibration & transferto online system

WP2: Feedstock for levulinic acid & DMB production

� detailed chemical analysis of these� development of rapid tools for analysis� transfer of these tools to an online facility

at a sugar mill in Piracicaba, Brazil for the rapid analysis of biomass.

Page 17: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development

Traditionally the yield of LevA is reduced by undesirable side reactions that form humins.

� DIBANET aims to increase the yield by

1. designing & engineering the reactor & conditions �reactor configurations�residence time,�temperature�pressure�acid concentration & type

Page 18: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

2. Development of kinetic models

4. Pre-treating the biomass

3. Using solid acid catalysts in acid hydrolysis& ethyl levulinate production

DIBANET aims to increase the yield by

Involves UL, UFRJ, UBA & ES

Page 19: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

WP4 – DMBs via the Pyrolysis and upgradingof Acid-Hydrolysis Residues (AHRs)

� Utilise solid resides effectively!

�Pyrolysis - produces bio-oil, biochar, gas.

Page 20: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

� Bio-oil highly oxygenated, high water content, acidity, non-miscible with diesel.�Improve bio-oil with catalytic

pyrolysis

�Upgrade bio-oil with hydrotreating & esterificationusing catalysts developed by DIBANET.

� Evaluate the biochar as a plant growth promoter.

Involves: UL, Aston, Certh, UFRJ, UBA & EMBRAPA

Page 21: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

WP5 – Assessment of DMBs and their Potential

� This involves the analysis of the DMBs produced in WPs3 and 4.

� YPF play a key role in determining how DIBANET DMBscomply with EN590 requirements & how fuel performance can be improved.

� 2020 without DIBANET sees a greater level of biodegradable waste going to landfill in both the EU & LA while the cost of large amounts of diesel imports drains both nations of cash.

� With the DIBANET process both nations are predicted to reduce the amount of biodegradable waste going to landfill by utilising it as a feedstock for the production of DMBs.

Involves all partners except FOSS

Page 22: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

2020 with & without DIBANET

Page 23: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

Optimised DIBANET process

� It combines this with the work from the WPs 2-4 to consider the design & implementation of a facility utilising all technologies and/or various combinations of these.

� It looks for the optimum configuration of the DIBANET Process Chain for various feedstock scenarios & policy/economic climates so that the most effective sustainable strategy for the EU and LA, & the DIBANET industrial partners, can be sought.

Page 24: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

WP6 Dissemination & Exploitation

� Engages stakeholders & increases cooperation.

� Website, newsletters, brochures, publications, contact data-base, e-learning course, workshops, summer school, EU-LA co-op day.

Involves all partners

Page 25: DIBANET concept networking day Rio 2010 · WP3 –Levulinic Acid (and Ethyl Levulinate) Reactor and Process Development Traditionally the yield of LevA is reduced by undesirable side

DIBANET

For more information on DIBANET please visit our website www.dibanet.org or email

[email protected]