biomasa a partir de catálisis enzimáticas_mercedes ballesteros
DESCRIPTION
Autora: Mercedes BallesterosTRANSCRIPT
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BIOFUELS FROM ENZYMATIC BIOFUELS FROM ENZYMATIC CATALYSTCATALYST
CATALYSIS FOR ENERGY: NEW CHALLENGES FOR A SUSTAINABLE CATALYSIS FOR ENERGY: NEW CHALLENGES FOR A SUSTAINABLE ENERGETIC DEVELOPMENTENERGETIC DEVELOPMENT
M. BallesterosHead of Biofuels Unit
CIEMAT
Santander, 19th august 2010
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They can be used pure or blending with fossil fuels
Bioethanol: sugars, starch, cellulose
Biodiesel: vegetable oils or animal fats
Biogas: Biomass
Biometanol: Biomass
Biodimetylether: Biomass
BioETBE and BioMTBE
Synthetic biofuels
Biohydrogen: a partir de biomasa
Pure Plant Oil
BIOFUELS
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BIODIESEL
- From vegetable oils - To be used in diesel engines
.
BIOETHANOL and its derivative (ETBE)
- From sugar-rich feedsotcks - To be used in Otto engines
MAIN BIOFUELS
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American Standard for Testing and Materials (ASTM):
a fuel comprised of mono-alkyl esters of long chain fatty acids derived from vegetable oils or animal fats, designated B100, and meeting the requirements of ASTM D 6751 to be use for transport or heating
BIODIESEL DEFINITION
European Directive 2003/30/CE
Biodiesel is a methyl-ester produced from vegetable or animal oil, of diesel quality to be used as biofuel in internal combustion engines
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Vegetable oils
Used vegetable oils
Animal fats
Microalgae
FEEDSTOCKS FOR BIODIESEL PRODUCTION
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*BIODIESEL: mono-alkyl esters from fatty acids
Shorter molecules, linear chain, less carbono content Lower viscosity and characteristics similar to fossil diesel
*PURE PLANT OILS (PPO):
Large and branches molecules, high carbon content High viscosity
PPO VERSUS BIODIESEL
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OIL/FAT
TRANSESTERIFICATION
MIXING
SEPARATION
PURIFICATION
BIODIESEL
RAW BIODIESEL
CATALYST
ALCOHOL
RAW GLYCERINE
FATTYACIDS
ALCOHOL (50%)
GLYCERINE
PURIFICATION
BIODIESEL PRODUCTION
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catalyst
TG + 3 ROH G + 3 FAAE
Catalyst: Alkaline, acid, enzymaticTG: triglyceride, ROH: alcohol, G: glycerineFAAE: fatty acid alkyl esters.
TRANSESTERIFICATION
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• It can transform free fatty acids and use ethanol
•High purity product
• Easier downstream process
• High enzyme cost
• Inactivation during the process (methanol y glycerol)
Mucor miehei
Rhizopus oryzae
Candida antarctica
Pseudomonas cepacia
Lipasa extracelular
Lipasa intracelular
Immobilization
BIODIESEL FROM ENZYMATIC CATALYSIS (Lipases)
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Transesterification proccess depends on:
• Temperature• Reaction time• Molar ratio alcohol:vegetable oil, • Alcohol type• Catalyst concentratio• Mixing intensity• Free fatty acids• Moisture
Lipases
• Solvent type (alcohol low solubility and effect of glycerol on enzyme) • pH• Microorganisms• Free or immobilized
OPERATIONAL VARIABLES
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R ecep c ió n d e l m ate ria l
C A Ñ A D E A Z Ú C A RR E M O L A C H A
H id ró lis is en z im á tica
Tritu rac ió n
R ecep c ió n d e l m ate ria l
C E R E A L
H id ró lis is en z im á tica H id ró lis is á c id a
Tritu rac ió n
R ecep c ió n d e l m ate ria l
L IG N O C E L U L O S A
Fermentación
Destilación
ETANOL
ETHANOL PRODUCTION PROCESSES
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STARCH CARBOHYDRATES COMPOSITION
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ETHANOL PRODUCTION PROCESS FROM GRAIN
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STARCH HYDROLYSIS
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Source: Medium Term Oil Market Report, OECD/IEA, Paris (2009)
BIOFUELS: An expanding industry
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Directive 2009/28:
20% TOTAL ENERGY MUST BE RENEWABLE 10% OF TRNSPORT ENERGY
THE EUROPEAN OBJECTIVETHE EUROPEAN OBJECTIVE
No areas with high biodiversity
No areas with high carbon stocks
Primary forests and wooded land
Protected natural areas
Highly biodiversity land (grassland and non-grassland)
Cont. forested areas (trees higher 5m)
Peatland / wetlands
Minimum GHG savings
35% by 2009/201350% by 201760% after 2017
Only direct land use change consideredOnly if it affects carbon
stocks
Reference date: January 2008
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First generation
Second generation
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Advantages Better energy balance Reductions in:
• Greenhouse gas emissions• Land use requirements
No competition with food, fiber and water
Barriers High cost of production Logistics and supply Industry & consumer
acceptance Perceived risky investments
THE EUROPEAN OBJECTIVETHE EUROPEAN OBJECTIVE
10% replacement by 2020
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CONVERSION PATHWAYSCONVERSION PATHWAYS
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STATUS OF BIOFUELS TECHNOLOGIESSTATUS OF BIOFUELS TECHNOLOGIES
Source: DG-TREN
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21O-acetil - galactoglucomanano
THE REAL HEADACHE FOR DEVELOPING BIOFUELSTHE REAL HEADACHE FOR DEVELOPING BIOFUELS
The contrast between what we have (carbohydrates) and
what we want (oxygen-deficient fuels)
O-acethyl- 4- O- methylglucuronoxylan
arabin- 4- O- methylglucuronoxylan
glucomanan
Carbohydrates are large polymer chains containing C5 and C5 sugars and a similar number of oxygen atoms
Optimal fuel molecules for automobile engines must be small (5-15 carbons) and contain little oxygen
The challenge is finding a way of breaking down carbohydrates to form small molecules, while simultaneously removing the oxygen and minimizing the loss of energy value of original biomass
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COMPOSITION OF LIGNOCELLULOSIC BIOMASSCOMPOSITION OF LIGNOCELLULOSIC BIOMASS
Source: DOE Genomics: GTL, 2008
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COMPOSITION OF LIGNOCELLULOSIC BIOMASSCOMPOSITION OF LIGNOCELLULOSIC BIOMASS
Feedstock
Cellulose (%)
Hemicellulose
(%)
Lignin (%)
Extractives
(%)
Ash (%)
Corn stover
36.4 22.6Xylose 18Arabinose 3Galactose 1Mannose 0.6
16.6 7.3 9.7
Wheat straw
38.2 24.7Xylose 21.1Arabinose 2.5Galactose 0.7Mannose 0.3
23.4 13 10.3
Hardwood
43.3 31.8Xylose 27.8Mannose 1.4
24.4 ---- 0.5
Softwood 40.4 31.4Xylose 8.9Mannose 22.2
28.0 --- 0.5
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ETHANOL PRODUCTION BY ENZYMATIC HYDROLYSIS
Lignocellulosicbiomass
Pretreatment Product recovery
ETHANOL
Enzymatichydrolysis
Cellulase complex
Fermentation
Fermenting microorganism
Xylose Fermentation
Heat and electricity production
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BIOMASS PRETREATMENTBIOMASS PRETREATMENT
Pretreatment
Cellulose
HemicelluloseLignin
CHARACTERISTICS: • Versatile
• Avoid expensive biomass . comminuting
• Use low cost chemicals
• Have low energy and capital cost . . requirements
• High hexose and pentose sugars . . yield
• Low inhibitors production
• Facilitate the recovery of lignin
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Biological, Physical, Chemical, Combination
Pretreatment Advantages Disadvantages
Dilute acid Hemicelluloses solubilization Enhances cellulose accessibility
High capital costsSugar degradationNeutralization
Concentrated acid
Lower temperatureReduction of degradation compounds
ExpensiveRequires acid recovery
Steam explosion Well knownPartial hemicellulose solubilization
Low pentose recoveryRequires washing to remove inhibitors
AFEX Rupture of lignin-hemicellulose bondsLow degraded products
High capital costs due to need to recycle the ammonia
BIOMASS PRETREATMENT CLASIFICATIONBIOMASS PRETREATMENT CLASIFICATION
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Treatment of biomass with steam at high temperature (180-220ºC), followed by explosive decompression.
STEAM EXPLOSION PRETREATMENT STEAM EXPLOSION PRETREATMENT
Extractives(%)
Cellulose(%)
Hemicellulose(%)
Lignin
(%)
Ash(%)
Straw 12 37 26 17 8
Pretreated
WIS --- 60 6 31 3
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ENZYMATIC HYDROLYSISENZYMATIC HYDROLYSIS
EnzymaticHydrolysis
RATE LIMITING FACTORS
SUBSTRATE STRUCTURE
Crystallinity of cellulose Low substrate surface area Lignin blocking reactive sites
ENZYMES
End-product inhibition Enzyme inactivation Non-specific binding
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• Endoglucanases• Cellobiohydrola
ses• β- glucosidases
Bacterial cellulosome
Cellulases secreted by fungi
CELLULASE COMPLEXCELLULASE COMPLEX
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30Fuente: Novozymes, 2005
Enzimas accesorias:- xylanasas- pectinasas- beta-glucosidasa- extensinas
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AMORPHOGENESISAMORPHOGENESIS
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TECHNOLOGY CHALLENGES FOR BIOCHEMICAL ROUTETECHNOLOGY CHALLENGES FOR BIOCHEMICAL ROUTE
NEW AND/OR IMPROVED ENZYMESNEW AND/OR IMPROVED ENZYMES
• To reduce the costs of enzyme production by improving cellulase production and enzymatic cocktail efficiency
• To find the way for reducing enzyme loading without loss of performance
• To develop enzymes with improved thermo-stability and less susceptibility to sugars inhibition
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TECHNOLOGY CHALLENGES FOR BIOCHEMICAL ROUTETECHNOLOGY CHALLENGES FOR BIOCHEMICAL ROUTE
NEW AND/OR IMPROVED ENZYMESNEW AND/OR IMPROVED ENZYMES
• To reduce the costs of enzyme production by improving cellulase production and enzymatic cocktail efficiency
• To find the way for reducing enzyme loading without loss of performance
• To develop enzymes with improved thermo-stability and less susceptibility to sugars inhibition
TO MAXIMIZE THE CONVERSION OF CELLULOSE TO SUGAR
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Saccharomyces cerevisiae EthanolGlucose
Mannose
Galactose
Xylose
Arabinose
ETHANOL PRODUCTIONETHANOL PRODUCTION
THEORETICAL YIELD• 0. 51 g ethanol / g sugar
1 ton wheat straw• 400 kg hexoses → 200 kg
etanol• 200 kg pentoses → 100 kg
etanol
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Acid hydrolysis
Enzyme production
1950
1970
Enzyme production
Enzymeproduction
Enzyme productionEnzymatic hydrolysisGlucose to ethanolHemicellulosic sugars to ethanoll
Glucose to ethanol No hemicelulose utilization
Enzymatic hydrolysis
Glucose to ethanol
Enzymatic hydrolysisGlucose to ethanolHemicellulosic sugars to ethanol
No hemicellulose utilization
Enzymatic hydrolysisGlucose to ethanol
Today
No hemicellulose utilization 1980
Tomorrow
ADVANCES IN RESEARCH
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• More efficient pretreatment technologies• Increase the efficiency of enzymatic
hydrolysis• Low enzyme and inoculum concentration • Fermentation of pentoses on real
substrates• Reduce energy demand in the
production process• Low concentration of product (ethanol)
IMPROVEMENTS IN THE PRESENT TECHNOLOLOGY
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OPERATOR LOCATION ETHANOL CAPACITY
SCALE STATUS
Abengoa Bioenergy
Salamanca, Spain 4000 t/yr DemoOperational, start-up 2009
BioGasol Bornholm, Denmark 4000 t/yr Demo Planned
DTU, BioGasol Copenhagen, Denmark 10 t/yr Pilot Operational, start-up 2006
SEKAB Örnsköldsvik, Sweden
100 t/yr4500 t/yr50,000 t/yr120,000 t/yr
PilotDemoDemoComm.
Operational, start-up 2004Planned, start-up 2011Planned, start-up 2014Planned, start-up 2016
Inbicon, DONG
Energy
Fredericia, DenmarkFredericia, DenmarkKalundborg, Denmark
110 t/yr1100 t/yr4,500 t/yr
PilotPilotDemo
Operational, start-up 2003Operational, start-up 2004Inauguration 2009
Procethol 2G,
FuturolPomacle, France
140 t/yr
2840 t/yr
Pilot
Demo
Under construction, start up 2010Planned
Süd-Chemie Münich, Germany 2 t/yr Pilot Operational, start-up 2009
Second generation bioethanol, pilot, demonstration and projectedcommercial plants in Europe.
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OPERATOR LOCATION ETHANOL CAPACITY
SCALE STATUS
Abengoa Bioenergy
Salamanca, Spain 4000 t/yr DemoOperational, start-up 2009
BioGasol Bornholm, Denmark 4000 t/yr Demo Planned
DTU, BioGasol Copenhagen, Denmark 10 t/yr Pilot Operational, start-up 2006
SEKAB Örnsköldsvik, Sweden
100 t/yr4500 t/yr50,000 t/yr120,000 t/yr
PilotDemoDemoComm.
Operational, start-up 2004Planned, start-up 2011Planned, start-up 2014Planned, start-up 2016
Inbicon, DONG
Energy
Fredericia, DenmarkFredericia, DenmarkKalundborg, Denmark
110 t/yr1100 t/yr4,500 t/yr
PilotPilotDemo
Operational, start-up 2003Operational, start-up 2004Inauguration 2009
Procethol 2G,
FuturolPomacle, France
140 t/yr
2840 t/yr
Pilot
Demo
Under construction, start up 2010Planned
Süd-Chemie Münich, Germany 2 t/yr Pilot Operational, start-up 2009
Second generation bioethanol, pilot, demonstration and projectedcommercial plants in Europe.
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OPERATOR LOCATION ETHANOL CAPACITY
SCALE STATUS
Abengoa Bioenergy
Salamanca, Spain 4000 t/yr DemoOperational, start-up 2009
BioGasol Bornholm, Denmark 4000 t/yr Demo Planned
DTU, BioGasol Copenhagen, Denmark 10 t/yr Pilot Operational, start-up 2006
SEKAB Örnsköldsvik, Sweden
100 t/yr4500 t/yr50,000 t/yr120,000 t/yr
PilotDemoDemoComm.
Operational, start-up 2004Planned, start-up 2011Planned, start-up 2014Planned, start-up 2016
Inbicon, DONG
Energy
Fredericia, DenmarkFredericia, DenmarkKalundborg, Denmark
110 t/yr1100 t/yr4,500 t/yr
PilotPilotDemo
Operational, start-up 2003Operational, start-up 2004Inauguration 2009
Procethol 2G,
FuturolPomacle, France
140 t/yr
2840 t/yr
Pilot
Demo
Under construction, start up 2010Planned
Süd-Chemie Münich, Germany 2 t/yr Pilot Operational, start-up 2009
Second generation bioethanol, pilot, demonstration and projectedcommercial plants in Europe.
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REDUCCIÓN DEL COSTE DEL ETANOL CELULÓSICO
Source: NREL
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• Ethanol from lignocellulose is close to commercialization
• Technological advances to reduce the costs of ethanol production of the bioetanol are still needed.
• Basic and applied research, technological development and demonstration projects must carried in a coordinated way
CONCLUDING REMARKS