catalytic conversion of carbohydrates to hydrocarbons

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  • 7/31/2019 Catalytic Conversion of Carbohydrates to Hydrocarbons

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    Catalytic Conversion of Carbohydrates to HydrocarbonsDOE Biomass R&D TAC Meeting

    May 19, 2011

    Paul Blommel, PhD

    Director of Process Chemistry, Virent Energy Systems, Inc.

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    BioFuel Pathways from Biomass

    Biomass

    Fermentation

    Fermentation

    AqueousPhase

    Reforming

    Refining

    Fischer-Tropsch

    Catalysis

    Gasification

    Pyrolysis

    Hydrolysis

    Syngas

    Bio-oils

    Sugars

    DieselJet Fuel

    Ethanol

    MethanolEthanol

    Liquid Fuels

    EthanolButanolHydrocarbons

    Gasoline,Jet, Diesel,Chemicals,Alcohols,

    Hydrogen

    CH1.4O0.6

    CH1.6O0.4

    CH2O

    CO + H2

    CH2

    CH2

    CH3O0.5

    CH3O0.5

    CH3O0.5

    CH2

    CH2

    CH3O

    0.5

    Conversion ofCarbohydrates

    toHydrocarbons

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    O

    OHOH

    HO

    HOCH2OH

    H2OH2

    CO2

    n-Paraf f ins

    iso-Paraffins

    Aromatics

    + H2O

    3.58 C6H12O6 C14H30 + 7.5 CO2 + 6.5 H2O

    Overall Theoretical Stoichiometrywith in situhydrogen generation

    Hydrocarbon contains 65 % of Sugar CarbonHydrocarbon contains 94% of LHV of Sugar

    Generation of Hydrocarbons from Carbohydrateswith In-situHydrogen Generation

    Slide 3

    Potential

    CarbonYield

    Potential

    EnergyRecovery*

    Ethanol

    Fermentation67% 96%

    Catalytic

    Conversion in

    situ hydrogen

    65% 94%

    Catalytic

    Conversion ex

    situ hydrogen

    100% 144%(90% including H2)

    *Potential LHV of liquid fuel product/LHV ofcarbohydrate feed

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    Catalytic Carbohydrate ConversionTechnology

    Feedstock Flexible Conventional Sugars

    Non-Food Sugars

    Drop-in Products

    Liquid Fuels and Chemicals

    Tunable Platform

    Infrastructure Compatible

    Fast and Robust Inorganic Catalysts

    Moderate Conditions

    Low Residence Times

    Energy Efficient Exothermic

    Low Energy Separation

    Slide 4

    A catalytic route to renewable hydrocarbon fuels and chemicals.

    Virent Demonstration Plant

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    Aromatics and Paraffins

    BioForming Platforms

    APR

    Modified

    ZSM-5

    Condensation Hydrotreating

    Biomass

    SugarCane

    Corn

    Starch

    Kerosene

    Jet Fuel

    Diesel

    Slide 5

    Gasoline +

    AromaticsReactive

    Intermediates

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    Generation of Reactive Intermediates

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    Production of Hydrocarbons fromReactive Intermediates

    Slide 7

    APR FractionationCatalytic

    Conversion

    GasolineProduct

    C5 & C6Sugars

    Hydrolysates

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    BioGasoline ProductPremium product with the same components as petroleum derived gasoline

    BioForming BioGasoline+120,000 BTUs/Gal

    Ethanol

    76,000 BTUs/Gal

    Unleaded Gasoline

    115,000 BTUs/Gal

    Unleaded Gasoline

    BioForming

    Green Gasoline

    ~ 20 liters of sugar derived gasoline

    from Virents BioForming process.Slide 8

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    Catalytic Processing Offers Flexibility toReplace More than Fuels

    0.0E+00

    2.0E+06

    4.0E+06

    6.0E+06

    8.0E+06

    1.0E+07

    1.2E+07

    1.4E+07

    1.6E+07

    1.8E+07

    2.0E+07

    0 5 10 15 20 25 30 35 40 45

    FIDR

    esponse

    (ArbitraryUnits)

    Retention Time (Minutes)

    11 % Benzene

    1.2% Benzene

    38 % Toluene

    12 % Toluene

    Optimized Product for Gasoline

    Blending

    Composition Shifted for

    Aromatics Production

    Product CompositionFlexibility

    Bio-reformate can replace typical reformate which is dominantfeedstock for many chemicals, fibers, and plastics in use today.

    Benzene

    Toluene

    Para-Xylene

    Meta-Xylene

    Ortho-Xylene

    Slide 9

    http://www.google.com/imgres?imgurl=http://www.tela.it/immagini/imballi.jpg&imgrefurl=http://www.tela.it/products.html&usg=__8Hsv5gqBuazdASPuFe7SN1SuC_o=&h=544&w=621&sz=37&hl=en&start=6&sig2=QleLu1LgNSTWWMyg7arNSw&itbs=1&tbnid=FDKjLpy1xYDvKM:&tbnh=119&tbnw=136&prev=/images?q=polyurethane+foam&hl=en&gbv=2&tbs=isch:1&ei=m7zxS76nIp3sMMOpxeoL
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    Process Scale Up Gasoline/Aromatics

    Carbohydrates-to-Aromatics process

    Scale-up of x100 from pilot plant

    10,000 gallons per year

    Full Length Reactor andCommercial Scale Catalyst

    Product volumes for registrationand fleet testing

    Feedstock handling and purification

    system flexibility Operations started in November 2009

    Overall success: On time, underbudget, high quality product

    Slide 10

    http://vnet/Pictures/Eagle/Eagle%20040.JPG
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    Paraffins and Naphthenes

    BioForming Platform - RPN

    APR

    Gasoline

    Condensation Hydrotreating

    Biomass

    SugarCane

    Corn

    Starch

    Gasoline +

    Aromatics

    Kerosene

    Jet Fuel

    Diesel

    Slide 11

    Modified

    ZSM-5

    ReactiveIntermediates

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    Virent RPN Characteristics

    Boiling Point

    Polarity

    Commercial Jet A-1

    Virent Jet

    Slide 12

    Max Jet Max Diesel

    Gasoline 20% 20%

    Jet 50% 0%

    Diesel 10% 60%

    Process Oil 20% 20%

    Flexible product slate

    Product is uniquely advantaged

    due to both component classes

    and ability to meet broad boiling

    point specifications

    Jet certification challenging and

    requires large volumes

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    Feedstock flexibility for catalytic conversion

    Biomass

    Cellulose(35-50%)

    Hemicellulose(15-35%)

    Lignin(15-35%)

    Others: 5-15%(Ash, Extractives)

    Pentose(Xylose, Arabinose)

    Hexose(Glucose, Mannose, Galactose)

    Monosaccharides

    Oligosaccharides

    Soluble Cyclics &Phenolics

    Ash & SolubleInorganics

    Lignin

    Sugar Degradation(Furfurals, HMF, Organic

    Acids)

    MicrobialConversion

    CatalyticRoutes

    vs.

    Slide 13

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    NABC Overview

    Slide 14

    Consortium LeadsNational Renewable Energy Laboratory

    Pacific Northwest National Laboratory

    Consortium PartnersAlbemarle Corporation

    Amyris Biotechnologies

    Argonne National Laboratory

    BP Products North America Inc.

    Catchlight Energy, LLC

    Colorado School of Mines

    Iowa State University

    Los Alamos National Laboratory

    Pall Corporation

    RTI International

    Tesoro Companies Inc.

    University of California, Davis

    UOP, LLCVirent Energy Systems

    Washington State University

    Virent leads the Catalytic Conversion of Lignocellulosic Sugars (CLS) strategy. The underlined parties above are

    currently collaborating within the CLS strategy.

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    Virent Deconstruction Partners

    Slide 15

    Dilute acid pretreatment and

    enzyme hydrolysis

    Wet oxidation and enzymehydrolysis

    Strong acid pretreatment

    Virent catalytic deconstruction

    Enzyme

    Hydrolysis

    Dilute Acid

    Deconstruction

    Enzyme

    Hydrolysis

    Wet Oxidation

    Deconstruction

    Catalytic

    Deconstruction

    Concentrated

    HCl

    Deconstruction

    Polyoxygenates

    Furans

    Carboxylic Acids

    Separator

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    Catalytic Lignin Conversion

    Slide 16

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