pyne -- glasgow wp 2h biorefinery tony bridgwater and doug elliott september 20, 2006
TRANSCRIPT
PyNe -- Glasgow PyNe -- Glasgow PyNe -- Glasgow PyNe -- Glasgow
WP 2H Biorefinery
Tony Bridgwater and Doug ElliottSeptember 20, 2006
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Presentation OrganizationPresentation OrganizationPresentation OrganizationPresentation Organization
Biorefinery basics
Biorefinery concepts
TEA for Biorefineries
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An Example of a Current BiorefineryAn Example of a Current BiorefineryAn Example of a Current BiorefineryAn Example of a Current Biorefinery
Corn Wet Mill
starch corn oilcorn gluten
mealcorn gluten
feed
food & industrial starches
hydrolysis
glucose
fuelethanol
High fructosecorn syrup
sorbitol
• foodstuffs• pharma.
polyols isosorbide
hydrogenation
Othersweeteners
citric acid lysine
xanthan gumsitaconic acid
& other fermentation
products
industrial oils
lactic acid
PLApolymers
•resins & plasticsapplications
•polyesters•surfactants•pharmaceuticals
deicerssolventscoatings
glycerolfood oilsfeed oils
Corn Wet Mill
starch corn oilcorn gluten
mealcorn gluten
feed
food & industrial starches
hydrolysis
glucose
fuelethanol
fermentation
sorbitol
• foodstuffs• pharma.
polyols isosorbide
hydrogenation
citric acid lysine
xanthan gumsitaconic acid
& other fermentation
products
industrial oils
lactic acid
PLApolymers
•resins & plasticsapplications
•polyesters•surfactants•pharmaceuticals
deicerssolventscoatings
glycerolfood oilsfeed oils
T.A. Werpy, Biorefineries, ACS Mtg, Washington, DC August 31, 2005
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Current Ethanol ProcessCurrent Ethanol ProcessCurrent Ethanol ProcessCurrent Ethanol Process
Corn Dry Grind Liquefaction Scarification
FermentationPrimary
DistillationDistillationRectifier
MolecularSieves
Centrifuge
Triple EffectEvaporator
DDGDryer
DDGAnimal Feed Ethanol
Solids
50%EtOH
95%EtOH
100%EtOH
Liquids
Water Recycle
Solids
T.A. Werpy, Biorefineries, ACS Mtg, Washington, DC August 31, 2005
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Strategies for Creating Additional ValueStrategies for Creating Additional ValueStrategies for Creating Additional ValueStrategies for Creating Additional Value
Modify dry mills to include a quick steeping process that allows germ recoveryAdd an intermediate filtration process to recovery non-starch derived sugars (hemicellulose)Develop new fermentations for utilization of five carbon sugars (itaconic acid, succinic acid, etc)Develop new chemistry to produce value added products from hemi-cellulose (sugar alcohols, polyols)Include an energy component-pyrolyze “DDG or modified DDG” to produce bio-oil
T.A. Werpy, Biorefineries, ACS Mtg, Washington, DC August 31, 2005
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The Holistic Ethanol FacilityThe Holistic Ethanol FacilityThe Holistic Ethanol FacilityThe Holistic Ethanol Facility
Corn Quick Steep Scarification
Filtration Fermentation EthanolRecovery
MolecularSieves
“Fiber” HydrolysisNew DDG
Animal FeedEthanol
StarchEtOH 95%
EtOH100%EtOH
GermSeparation
Fermentation
CatalyticConversions
Pyrolysis
Fuel/PowerEG, PG
Glycerol, Etc
ItaconicSuccinic, Etc
Oil
T.A. Werpy, Biorefineries, ACS Mtg, Washington, DC August 31, 2005
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Possible Future BiorefineryPossible Future BiorefineryPossible Future BiorefineryPossible Future Biorefinery
Lignocellulosic Biomass
Hydrolysis Fermentation
UpgradingPyrolysis
Ethanol FuelDistillation
Products
Products
lignin
sugars
bio-oilAdditionalBiomass
Motor Fuel
D.J. Stevens, PyNe, 2005
Heat, electricity
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The Potential Role of PyrolysisThe Potential Role of PyrolysisThe Potential Role of PyrolysisThe Potential Role of Pyrolysis
Part of a Petroleum Refinery Biomass first would be converted to bio-oil, possibly at
distributed locations at small scale Bio-oil can be partially upgraded by catalytic
hydrotreatment at larger scale in proximity of a petroleum refinery
Upgraded bio-oil then would be co-fed with petroleum feedstocks through a catalytic process to produce conventional refinery product slate
The global petroleum industry is showing more interest From the Department of Energy perspective, this is a
medium-term approach
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Pyrolysis/Petroleum BiorefineryPyrolysis/Petroleum BiorefineryPyrolysis/Petroleum BiorefineryPyrolysis/Petroleum Biorefinery
Distributed Lignocellulosic
Biomass
Upgrading and Refining with Petroleum
Fast Pyrolysis
Products
Motor Fuel
bio-oil transport
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Overall Biorefining Concept
Primary fractionation
and liquefaction
Biomass residues
Co-processing in conventional
petroleum refineryDe-oxygenation
Hydrocarbon-rich fraction
Lignin-rich fraction
ConversionDerivatives of hemicelluloses and celluloses
Conventional fuels and chemicals
Oxygenated products
Energy production
Process residues
(blending)
Yrjö Solantausta, 14.3.2006, VTT
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The Potential Role of PyrolysisThe Potential Role of PyrolysisThe Potential Role of PyrolysisThe Potential Role of Pyrolysis
Stand-alone facilities Small size makes economics of fuel production difficult May be more appropriate for heat and power
applications High-value specialty chemicals may provide the
economic driver Unlikely to gain strong support from Department of
Energy in the U.S. because of current focus on petroleum displacement, but Department of Agriculture is interested
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Concept of a BiorefineryConcept of a BiorefineryConcept of a BiorefineryConcept of a Biorefinery
D. Radlein, Fast Pyrolysis Handbook, 1999
Pyrolyzer
Fuel Gas
Char Converter
Bio-oil
Ash Activatedcarbon
Biomass Anhydrosugars
Hydrolysis & Fermentation
Reaction
Reaction
Reaction
Separation
Separation
Catalytic Reforming
NH3
lime
alcohol
water
Ethanol
Slow Release Fertilizers(N, Ca, Zn, Fe ...)
Noxolene™(NOx reduction)
BioLime™(NOx/SOx reduction)
Fuel EnhancersFlavor ChemicalsChemicalsFlavors
Adhesives
Diesel/boiler FuelSpecialty
Synthesis GasHydrogen
Biomass Refinery ConceptD. Meier
Biomass
Fractionation
FibersCellulose
HemicelluloseLignin
direct use
•in situ treatment•post treatment
direct use
PHENOLS
alcoholswater (NCW, steam)
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Biomass Refinery ConceptBiomass Refinery ConceptD. MeierD. Meier
Biomass Refinery ConceptBiomass Refinery ConceptD. MeierD. Meier
Biomass
Fractionation
FibersCellulose
HemicelluloseLignin
direct use
•in situ treatment•post treatment
direct use
PHENOLS
alcoholswater (NCW, steam)
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BIOREFINERY CONCEPT
Fast pyrolysis
Wet fuelsMixed fuels
Woody biomass
waste wood, Acacia bark, agro-biomasses, constr. wood
ExtractivesSolvent
extraction Biodiesel
Aqueous phaseSteam
reformationH2 for fuel cells
Lignin phase Alcohol addition, solids removal
Fuel oils,Diesel fuels
Hydrolysis, fermentation
Bio-ethanol for fuel cells
Thermal cracking/Catalytic
hydrotreatment
Char Process energy
Steam activation
Activated carbon
Optional hydrolysis
Lignans
Anja Oasmaa, 2005, VTT
Forschungszentrum Karlsruhe in der Helmholtz-Gemeinschaft
ITC-CPV HEFW
FW
fast pyrolysis
biomass preparation
liquid fuel synthesis
rail transport from many pyrolysis plants
to large, central plant for syngas generation and use
entrained flow gasification
gas cleaning
electricity generation
Different biomass and carbon feedstocks
bio-oil/char -slurry
lignocellulosic biomass:wood, straw, hay ....fossil
fuel:
other biomass:
coal ...starch, oil ...
pulverised coalcoal/water slurry
organic waste:paper, plastics, dung ...
synthesis products:synfuel, chemicals, H2
electricity
low Theat
O2
CO2
specialchemicals
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SummarySummarySummarySummary
Numerous opportunities involving: incorporation into sugar biorefinery incorporation into a petroleum refinery stand-alone with chemical, fuel, and power production incorporation into a gasification and synthesis plant
Pyrolysis demonstration will lead to biorefineryProduct separation and recovery is a major hurdleFinding the right niche is key
PyNe -- Glasgow PyNe -- Glasgow PyNe -- Glasgow PyNe -- Glasgow
Progress in BiorefineryCase studies
Max Lauer and Doug ElliottSeptember 20, 2006
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The Potential Role of PyrolysisThe Potential Role of PyrolysisThe Potential Role of PyrolysisThe Potential Role of Pyrolysis
Part of a sugars-based biorefinery based on residue pyrolysis for fuel and, perhaps, products
Part of a Petroleum Refinery with distributed production and centralized processing
Stand-alone facilities with distributed production and centralized processing and refining or true stand-alone with or without fractionation and product processing
Incorporation into a gasification and chemical/fuel synthesis plant
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TEA of Pyrolysis BiorefineryTEA of Pyrolysis BiorefineryTEA of Pyrolysis BiorefineryTEA of Pyrolysis Biorefinery
What process concept (or concepts?) Single concept in depth, or Comparison of several concepts
Technical or Technoeconomic Detailed mass and energy balance only, or M&E balance to allow capital & operating cost estimate
What methods?
What level of detail?
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Biorefinery Concepts to be EvaluatedBiorefinery Concepts to be EvaluatedBiorefinery Concepts to be EvaluatedBiorefinery Concepts to be Evaluated
The following institutions agreed to provide the relevant information for the concepts listed below, and these would form the basis of an evaluation exercise. USDA - compare pyrolysis to combustion in ethanol plants IWC – pre-separation concept and pyrolyse products (lignin), maximise by-products and chemicals from the process, particularly phenolsFZK – bio-slurry gasification + synthesis PNNL - Distributed pyrolysis to central refinery for upgrading and integrationBTG – direct gasification of bio-oil in existing gasifier + synthesisAston – Speciality chemicals and fuelsRodim – Chemicals and animal pharmaceuticals and fertiliserJR - Pyrolysis + CHP stand-aloneECN – comparison with biomass gasification routes
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Biorefinery Concepts to be EvaluatedBiorefinery Concepts to be EvaluatedBiorefinery Concepts to be EvaluatedBiorefinery Concepts to be EvaluatedChemicals as primary product
IWC – pre-separation concept and pyrolyse products (lignin), maximise by-products and chemicals from the process, particularly phenolsAston – Speciality chemicals and fuelsRodim – Chemicals and animal pharmaceuticals and fertiliser
Fuels as primary productFZK – bio-slurry gasification + synthesis BTG – direct gasification of bio-oil in existing gasifier + synthesisECN – comparison with biomass gasification routesPNNL - Distributed pyrolysis to central refinery for upgrading and integrationUSDA - compare pyrolysis to combustion in ethanol plants JR - Pyrolysis + CHP stand-alone
TemplateBlock flowsheet starting with biomass input – maybe as bio-oil, using all
products in some way and minimising waste productionOutline mass balance through „blocks“Capital costsProduct costs
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Biorefinery Concepts to be EvaluatedBiorefinery Concepts to be EvaluatedBiorefinery Concepts to be EvaluatedBiorefinery Concepts to be EvaluatedChemicals as primary product1. Speciality chemicals and/or separation of biomass
componentsTransport fuels as primary product2. Bio-oil for transport fuels via gasification and FT and/or
methanol 3. Bio-oil (hydro) de-oxygenation for transport fuels Reference case4. Power and heatProcessa. Template for specifications and bio-oil costsb. Block flowsheet starting with biomass (industrial sawmill
waste ISW) input, using all products in some way and minimising waste production, to give end products
c. Outline mass balance through „blocks“. Size d. Capital costse. Product costsHow and when?Small working groups, Email, Draft (a) & (b) & (c) by end 2006 to
DCESmall meetings if needed(d) & (e) TBD but NOT after next TNet meetingGroup meeting 2007FT 20,000bbl/d=3000t/dBiomass 2,000t/d = 660,000t/y
AU, IWC, UN, USDA
ECN, FZK, BTG, VUT,
PNNL, VTT, UT, AU, CF
JR, NTNU, UF, USDA
@ JRDefine ISW @ JR
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Biorefinery Concepts to be EvaluatedBiorefinery Concepts to be EvaluatedBiorefinery Concepts to be EvaluatedBiorefinery Concepts to be Evaluated
FACTSFT single train 20,000bbl/d = 3000t/d diesel = ca 12,000t/d biomassUSA Biomass 2,000t/d = 660,000t/yEU Biomass 300 t/d = 100,000 t/yChoren planning 1,000,000 t/y for gasification + FT
SIZE OF BIOMASS PROCESSING PLANTS for considerationSmall = 200 t/d input dry biomassLarge = 2000 t/d input dry biomass = 400 MWth input = 160 MWe
SIZE OF intermediate fuel products dependent of biomass input, e.g. partially refined product to refinery
SIZE OF FT12,000 bbl/d output diesel productionUpgraded bio-oil hydrotreater = 6000 bbl/d diesel = 800 t/d diesel
PyNe -- Glasgow PyNe -- Glasgow PyNe -- Glasgow PyNe -- Glasgow
Round Robin on Lignin Pyrolysis
Dietrich Meier and Doug ElliottSeptember 20, 2006
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Round RobinRound RobinRound RobinRound Robin
Participants Which laboratories? list of potential participants at Lille
Feedstock requirements What kind? many potential sources How much? depends on the laboratory method
Time line Acquire feedstock Distribute feedstock Perform tests Collect data Submit report
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Potential Round Robin ParticipantsPotential Round Robin ParticipantsPotential Round Robin ParticipantsPotential Round Robin Participants
Laboratory ProcessAston University Fluid bed, TGA, Py-GCMSForschungszentrum Karlsruhe (FZK) Fluid bed, screw feedECN Fluid bedUniversity of Napoli BatchUniversity of Twente Fluid bedUSDA-Eastern Regional Research Center Fluid bed, TGABFH-Institute for Wood Chemistry Fluid bed, EFNational Renewable Energy Lab (NREL) Fluid bed
Pacific Northwest National Lab (PNNL) Analytical, TGA, Fluid bedVTT-Technical Research Centre of Finland Py-GC-AEDCIRAD-Forêt AnalyticalInstitut Français du Pétrole (IFP) TGA, Analytical,
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Potential Round Robin ParticipantsPotential Round Robin ParticipantsPotential Round Robin ParticipantsPotential Round Robin Participants
Lab Process
Aston Fluid bed (150, 300, 1000g/h), TGA (10mg), Py-GCMS (0.1mg)FZK Fluid bed, screw feed (10000g/h)ECN Fluid bed (Napoli Batch, fluid bed (10g?)Twente Fluid bed (1000g/h)USDA Fluid bed (1000g/h), TGA
BFH Fluid bed (150, 5000g/h), PyGC (0.1mg), microbatch (20mg)NREL Fluid bed (10000g/h)PNNL Analytical, TGA (10mg), Fluid bed (100g/h)VTT Py-GC-AED (0.1mg)CIRAD Analytical, fluid bed (1000g/h)IFP TGA (10mg), Analytical,
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Potential Lignin Sources for Potential Lignin Sources for Round Robin Round Robin
Potential Lignin Sources for Potential Lignin Sources for Round Robin Round Robin
MeadWestvaco Indulin AT – precipitated Kraft lignin (softwood)
Lignol (Alcell) Organosolve lignin Variable biomass source potential
IOGEN EtOH residue (straw lignocellulosic)
International Lignin InstituteOthers Sigma Aldrich (sulfur-free) Borregard (kraft lignin or lignosulfonates, both with sulfur) STFI (Swedish pulp & paper institute), kraft lignin
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Lignin SourceLignin SourceLignin SourceLignin Source
MeadWestvaco www.meadwestvaco.com pulping lignin products several grades
sulfonated Kraft lignins – REAX and KRAFTSPERSE sulfonated sulfite lignin – POLYFON unsulfonated Kraft lignin – Indulin
- AT: 5% moisture, 6.5 pH (15% aq) 3% ash, 97% lignin - C: 5% moisture, 10.2 pH (15% aq)
commercial products, readily available in most quantities
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Lignin SourceLignin SourceLignin SourceLignin Source
Lignol (Alcell process) – Bridgwater/Elliott organosolve hardwood lignin Michael Rushton, Vancouver, BC, Canada kilogram quantities available signed agreement by each researcher
no third party distribution no publication without permission – source attributed no chemical analysis without permission – data shared inform Lignol of patenting efforts involving Lignol lignin joint ownership of jointly developed IP mutual confidentiality recipient pays cost of shipping, duties, etc.
many potential biomass types in the future
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Lignin SourceLignin SourceLignin SourceLignin Source
Iogen – Elliott ligno-cellulosic EtOH residue Ron R. Paradis, VP EtOH and Byproduct Marketing not responsive
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Lignin SourceLignin SourceLignin SourceLignin Source
ENEA-Trisaia -- Chiaramonti steam explosion, alkali extracted, acid precipitated Dr. Braccio and Dr. Zimbardi 1 kg lignin available for round robin tests
they would ship the lignin they would like to know some details like what kind of
tests and who would carry them out
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Lignin SourceLignin SourceLignin SourceLignin Source
Abengoa – Prins biorefinery residue Viorel Duma, Chesterfield, MO, USA a few hundred kilos available at a time start up this winter 30% dry solids (could be treated (?) to reduce moisture
for pyrolysis) lignin content of 60%, balance fiber and ash less interesting alternative -- dry purified lignin product
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Lignin SourceLignin SourceLignin SourceLignin Source
Aldrich Chemical www.sigma-aldrich.com Several grades, commercially available
low sulfonate, alkali $0.30-0.40/g hydrolytic $1.20-1.60/g organosolve $0.60-1.00/g
100s of gram quantities
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Lignin SourceLignin SourceLignin SourceLignin Source
Lignoboost -- Meier/Elliott pulping residue lignin Per Tomani, STFI-Packforsk AB, Stockholm sulfur content depends on method, but typically 1-3% several hundred kilos of product available
they need to know more of purpose of testing
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Lignin SourceLignin SourceLignin SourceLignin Source
Swedish Energy Agency – Bridgwater organosolve enzyme acid
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Other Potential Lignin Sources Other Potential Lignin Sources for Round Robin for Round Robin
Other Potential Lignin Sources Other Potential Lignin Sources for Round Robin for Round Robin
Lignin without sulfur Baltic hydrolysis ILI Genencor enzyme hydrolysis lignin Mondi
Sulfur containing lignin Kraft lignin (Borregard?)