1. GreenSyngas Workshop ”GREENSYNGAS” Güssing February 23, 2011 General Presentation of GREENSYNGAS Advanced Cleaning Devices for Production of Green Syngas Mehri Sanati Lund University Faculty of Engineering Mehri.Sanati@design.lth.se http://www.eat.lth.se/greensyngas/

2. Role of each contractor in the project 1-ULUND: Coordinator & Management; research of downstream processing, particle phase characterisation for performance measurement of cleaning, catalytic system, demonstration 2-TUM: Development of sophisticated techniques (Laser diagnostics, Optical) for characterisation of tar & alkali in gasifier 3-TUD: On-line tar measurements and gasification with different biomass supply by Lantmännen, the gasifier was also used for field test of reforming catalyst (gas supply to the reactor system), and calibrating of the developed methodology for high temperature fine particle in produced gas (gas supply) 4-PA: Filter system that responds to the requirement of clean gas for downstream processing in GREENSYNGAS, multi-cyclone and sintered metal

3. 3 5-FZJ: Chemical hot gas cleaning and thermodynamic modelling, small gasification system, Biomass characterisation supply by Lantmännen 6-UNIBO: Downstream catalytic system; steam reforming, WGS reaction, catalytic tar cracking 7-JM: Scientific aspect of the catalytic system, catalysts supply, process flow- sheeting 8-NTNU: Downstream catalytic system; steam reforming, WGS reaction 9-BKG: Gasification, demo of cleaning device, experimental concerning catalyst exposure, supply of product gas from the gasifier to the partners laboratory 10-LANTM: biomass quality, accessibility and supply to different laboratories 11. Science in Society: Bil Sweden, Karin Kvist Continue

4. Total budget and duration 4 Total EC support, in €: 2,718,461.00 Total Contract cost, in €: 4,089,167.00 38 months project Contract start date:2008-01-01 Contract end date: 2011-02-28

5. WPs name and WPs leader and involved partners 5 WP N° Title of WPWP Leader Short name 1Coordination and Management ULUND 2Development of characterisation techniques for emissions measurement from Biomass Gasification TUM 3Gas purification of particulates PA 4Tar, alkali, HCl, NH 3 and sulphur removal including water treatment at high- low temperature TUD 5Non –catalytic and Catalytic steam reforming, catalytic poisoning and process flow sheeting tasks ULUND 6Water Gas Shift reaction and scale-up NTNU 7Large scale-Plant testingBKG 8Dissemination and Exploitation UNIBO WP Participant Short name Type of WP°°Start Date End Date All partnersManagement1 38 ULUND, TUM. LANTMResearch1 38 ULUND, PAResearch and demo 12 38 ULUND, TUD, FZJ, UNIBO, JM Research and demo 2 38 ULUND, UNIBO, JM, NTNU Research and demo 4 38 ULUND, UNIBO, JM, NTNU Research and demo 10 38 ULUND, TUD, PA, FZJ, UNIBO, JM, NTNU, BKG, LANTM Demo32 38 All partnersDissemination1 38

6. 6 Optimisation of units in Biofuel production route? Schematic energy conversion in a biomass to added value products (Thermochemical Conversion) Fuel ForestProcessing Harvesting Transport Palletizing Heat losses Thermo- Chemical Conversion Gas cleaning Heat losses Upgrading step to added value products Heat losses reforming and shift Product gas from gasification process consists of CO, CO 2, H 2, H 2 O, unburned hydrocarbons, tar, sot, char, inorganic, and generally org The aim will be increasing utilization of LHV of feedstock to added value products

7. collaboration between applied oriented technical discipline and basic research concentrated on new field of scientific knowledge Technological research targets Basic Research and Applied Investigation towards an innovative improved particle cleanup system and preventing catalytic deactivation Catalytic and nion- catalytic reaction system Improved particle removal system Combustion Thermo-chemical conversion & synthesis of product gas to heat & power, chemical and vehicle fuels Gasification High temperature Aerosol Physics Fluid Dynamics Transport Phenomena Thermodynamics Multiphase reaction system

8. 8

9. Baserad på gas produktsammansättning olika ”down stream” process kan vara aktuella.

10. 10 Partners contribution in relation to this Figure

11. 11 High temperature Cleaning device, in market High temperature Gas phase characterization High temperature particle characterization Ammonia removal Tar cracking Capture of sulfur and alkali Flow sheeting

12. 12 Reforming Step A) Steam reforming B)Auto-thermal reforming steam: carbon ratio about 2-4

13. Upgrading Steps-production routes of Syngas; Steam reforming

14. 14 Regenerative System for endothermic process, no heat waste (Energy Saving)

15. High temperature sampling probe for particulate (submicrone) High temperature Particle emission from wood Gasification To develop and evaluate methods for characterization of particles - Physically; Size, Mass, Number concentration -Chemical composition - Deposition on heat surface (corrosion issue)

17. 17 ACKNOWLEDGMENTS The work was supported by European Commission (EC) 7th Framework Programme (GREENSYNGAS Project Contract number 213628) and the Swedish Energy Agency

18. 18 Thanks for your attention mehri.sanati@design.lth.se