Federico Berruti
Transcription
Federico Berruti
ICFAR, Mobile Pyrolysis System (MPS200), LPS100, MFR & Feeding Technology, Pyrolyis Future Outlook Federico M. Berruti BESc, HBA, PhD Candidate Vanier CGS Scholar 2010-2013 Vice-President, Agri-Therm Inc. fberrut@uwo.ca www.agri-therm.com 1 SOUTHWESTERN ONTARIO 2 ~40,000 Undergraduate Students (U.G.S.) 1,300 Eng U.G.S ~5000 Graduate Students (G.S.) ~650 Eng G.S. $250 million in Research Revenue (University-Wide) $30 million Eng 95 Eng Faculty 3 4 Our People • 3 Full Members (Professors) • 12 Associate Members (Professors) • 4 Visiting Professors (in 2011-2013) • 40 Graduate Students (Master and PhD) • 5 Summer Students (Undergrad) • 4 International Visiting Students in 2011 • 3 Senior Research Scientists/Engineers • 7 Post-Doctoral Fellows • 3 Administrative Staff • 2 Technicians The Faculty Members Cedric Briens Director of Research and Development Franco Berruti Director (General) Charles Xu NSERC-FP Innovations Industrial Research Chair 6 Laboratory 8 Pilot Plants 9 Bench Top Equipment 75 mL 100 mL Flow-type supercritical reactors Fluidized sand-bath reactor system Stirred bath reactors (autoclave reactors) 500 mL 10 Analytical Equipment 30 L/min 40 L/min 50 L/min 60 L/min a) b) 0 rpm 500 rpm 1000 rpm 11 1500 rpm 2000 rpm 2500 rpm Analytical Equipment (cont’d) Agilent 3000 Micro-GC Shimadzu GC-FID 2010 500 mL Waters HPLC/GPC Brookfield Viscometer Mettler Toledo DSC 12 In-House Design 13 Industrial Partners Aduro Energy Inc. Agri-Therm Arclin Canada Chemtex Dynamotive Syncrude Total Agriculture and Agri-Food Canada FPInnovations Imperial Oil ExxonMobil Lignol Wood Ash Industries E-Plywood Gudgeon Thermofire Siliken Ellsin Environmental Iron Ore Company of Canada Del Monte Molson Breweries Tire King American Science and Technology Corporation Canmet Energy Sand Plains Community Ontario Bio-Lamp Sherritt Whitecrest Mushrooms Canadian Agra Corporation Altranex Char Technologies Airex Networks • ICFAR led the national $ 8.7 M Agricultural Biorefinery Innovation Network (ABIN) • ICFAR leads the $ 5.2 M NSERC LIGNOWORKS Strategic Research Network • ICFAR coordinates the “Central Platform” of BioFuelNet Canada, a National Network of Centres of Excellence (led by McGill University, Dr. Don Smith) • ICFAR is a partner in “Biochar for Carbon Capture” UKCanada Network (Leverhulme Trust) The depletion of fossil fuel reserves ( oil prices) Global demand for renewable fuels and green chemicals Demand for increasing utilization of agricultural and industrial by-products/wastes (process intensification) Reduce GHG Emissions Job creation 16 Selfsufficient in energy Converts crops, waste & other Biomass sources into Bio-Oil through a process called Fast Pyrolysis. No competition with food Compact, mobile, easy to operate: No need to transport biomass Reduces chemical fertilizers 17 The Problem: Converting Biomass into alternative fuel is limited by transportation costs/seasonality. Labour costs must be minimized. The Solution: Mobile Pyrolysis, the Agri-Therm MPS200 18 19 20 21 22 Mobile Pyrolysis System: SEE WEBSITE! ◦ Brings the “Plant” to the “Source” ◦ 5-10 tonnes dry biomass/day ◦ Converts Biomass to Bio-Gas, Bio-Oil and Bio-Char. ◦ Bio-Oil: ~30 MJ/kg ◦ Bio-Char: Carbon Sequestration and Soil Amendment ◦ 1 tonne Bio-Char sequesters 3 tonnes of CO2 23 Opportunities Wine Grape Wine Grape Skins and Seeds 12.2 million tonnes worldwide Corn Bio ethanol Dried Distiller’s Grains 35 million tonnes in North America Sugarcane Sugarcane Juice Sugarcane Bagasse 500 million tonnes worldwide Forest Resources Pulp and Paper Forestry Residue 280 million tonnes worldwide 24 Canada ◦ ◦ ◦ ◦ ◦ ◦ ◦ ◦ ◦ ◦ Forestry residues Tobacco Distillers’ grains & corn stover Chicken litter Apple pomace Grape residues Flax straw Food waste Coffee grounds Wastewater treatment plant sludge Rest of world ◦ Sugarcane plant and bagasse ◦ Rice straw ◦ Coffee husks 25 Globally 1.4B tpa 1% of Global market, 5400 MPS units Canada 42M tpa 1% of Canadian market, 200 MPS units 26 Cetane Energy 2 M gal/y New Generation Biofuels 5 M gal/y Biojet 200 M gal/y 10 units 25 units 1000 units 27 28 ◦ ◦ ◦ ◦ Phase I Demonstration Unit MPS200 cold testing underway Currently seeking partners/financing for pilot project MPS200 & Company Growth Opportunities Phase II Partnerships & Growth Manufacturing/Distribution, Service Providers, Oil Co’s, Upstream/Downstream Processing Improvements Phase III Expansion Expanded product lines, expanded uses (e.g. tires, waste) 29 Our Approach Project-1 Polyols (NSERC/FPInnovations) Bio-oil Platform Forest Biorefinery Catalytic hydrolysis Polyurethane Project-2 Project-4 Project-3 30 Opportunities 31 Opportunities 32 Opportunities 33 Opportunities Vapours from the reactor Gas-Sampling Filter ESP Cyclonic Condensers 34 Opportunities Bio-oil Vapours and permanent gases enter the condenser Persistent aerosols and permanent gases exit The “Cyclonic Effect” enhances heat transfer and facilitates droplet collection Collected liquid 35 Opportunities 1-10 kg/hr fluidized bed fast pyrolysis pilot plant. Highly instrumented to control all critical reaction parameters (such as T & P) Safe & Easy to Operate (1 operator required). Ideal for Research Facilities Optional Inconel reactor can be purchased for higher temperature gasification reactions. Product bio-gas can be recycled for fluidization. More Technical Specifications on Web-site! 36 Small Scale Batch (0.5 kg) Mechanically Fluidized Reactor (MFR) Pilot Plant 37 Mid-Scale (0.7 t/day) Mechanically Fluidized Reactor (MFR) Pilot Plant 38 Demo-Scale (2.5 t/day) Mechanically Fluidized Reactor (MFR) Mobile Plant Biomass Feed Gas Bio-Carbon Bio-Oil Fraction 1 Bio-Oil Fraction 2 Currently under design and construction (expected completion: Dec. 2013) Conclusions N2 Pulse N2 continuous 40 Conclusions Bio-oil vapours and permanent gases leave the reactor toward condensers. 4) An hot filter traps the small fraction of fine particles elutriated from the bed, avoiding contamination of the bio-oil. 3) The char stays in the bed. 1) The biomass is injected into the bed. 2) It mixes with the hot sand and reacts. N2 or Recycled pyrolysis permanent gases for Fluidization Conclusions 42 Conclusions FUNDAMENTALS BEING STUDIED: • Design criteria & scale-up • Effect of particle size & properties (avalanching machine & Hausner Ratio) • Slug Chamber Geometries • Slug characterization (length, mass, speed, spreading) – using lasers • Straggler detection (mass of stragglers) • Modeling • Effect on Fluid Bed Mixing & Stability LASERS 43 Opportunities 44 Opportunities Product yields: Kraft lignin 0.4 s vapor residence time 60 bio-oil yield, wt% 50 40 char 30 20 gas 10 0 440 460 480 500 520 540 560 o Reactor temperature, C 580 600 620 45 Opportunities 46 Opportunities Energy Balance and Sustainability vs. Temperature OPTIMAL RANGE Energy (MJ) Contained per kg MBM Feed 20 15 Product Gas Bio-Oil Bio-Char Total Reaction Energy Raw MBM Feedstock Energy Total Energy Input 10 91% Total Practical Energy Yield Obtained at 550°C 5 0 450 500 550 600 SUSTAINABLE! Temperature (°C) 47 Conclusions This is a CHALLENGE! Oil Industry > 100 years to Standardize Bio-Oil Upgrading Challenges/Economics Possible Steps: Demonstrate: Heat + Power Generation + Bio-Oil + Char Develop upgrading capabilities/create conventional products STABILIZE & STANDARDIZE PRODUCTS & FUELS Develop successful business operating models (scale, labour, raw materials, etc.) AND… 48 Conclusions TEAM UP! Biomass residue prep, drying, transportation Pyrolysis Technology & Research: Reactor Design, Feeders, Condensation, Upgrading, Scale-Up Bio-Char Characterization: Handling, Pelletization, Transportation, and Safe Utilization Bio-Oil Characterization: Stabilization, Upgrading, Handling, Transportation, and Safe Utilization Business: management, financing, securing resources and contracts, partnerships, designing business models, connecting the dots… 49 Conclusions Federico M. Berruti BESc, HBA, PhD Candidate Vanier Canada Scholar 2010-2013 Vice-President, Agri-Therm Inc. fberrut@uwo.ca www.agri-therm.com 50
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