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James F. Preston, Guang Nong, Virginia Chow, Changhao Bi and John D. Rice University of Florida Collaborators: L. O. Ingram, MCS K. T. Shanmugam, MCS F. Altpeter, PCMB G. Peter, PCMB Bacterial Conversion of Hemicellulosic Xylans to Biofuels and Chemicals

New Bacterial Conversion of Hemicellulosic Xylans to Biofuels and …floridaenergy.ufl.edu/wp-content/uploads/S3-Biomass... · 2011. 4. 19. · Quantification of MeGA substitution

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  • James F. Preston, Guang Nong, Virginia Chow, Changhao Bi and

    John D. Rice

    University of Florida

    Collaborators:

    L. O. Ingram, MCS

    K. T. Shanmugam, MCS

    F. Altpeter, PCMB

    G. Peter, PCMB

    Bacterial Conversion of Hemicellulosic

    Xylans to Biofuels and Chemicals

  • Objective

    Genetically engineer bacteria for digestion and fermentation of

    the hemicellulose fractions of agricultural residues (straw and

    sugar cane bagasse) and energy crops (poplar, eucalyptus and

    energy cane) to ethanol and lactic acid

    Expected Outcome

    Development of biocatalysts for the cost effective production

    of fuel alcohols and bioplastics from underutilized renewable

    resources

  • OBJECTIVE: Develop biocatalysts to provide maximal yields of alternative fuels and chemicals from lignocellulosics.

    Propanediol

    Cellulose

    Hemicellulose

    D-Glucose

    D-Xylose

    Butanediol

    Ethanol

    Lactic acid

    Glycerol

    Pyruvate

    P-Glyceraldehyde

    Hydrolysis/Saccharification Fermentation

    SPECIFIC AIM: Develop bacterial biocatalysts that efficiently converthemicellulose-derived glucuronoxylan to ethanol and chemical feedstocks.

  • Cellulose fiber

    32-48%

    Methylglucuronoxylan

    (MeGAXn) network

    18-35%

    Interaction of Major Polymeric Sugars in Lignocellulosic Biomass

    Cellulose and glucuronoxylan are

    tightly associated

    Cellulose fibers form through hydrogen

    bonding interactions between individual

    cellulose stands

    and cellulose fiber association by coating

    oGlucuronoxylan acts to limit microfibril

    r interacting with surface cellulose

    strands

    The noncarbohydrate polymer lignin

    embeds the interacting cellulose and

    glucuronoxylan through ester linkages to

    glucuronoxylan

  • FeedstockGlucan

    (cellulose)

    Xylan

    (hemicellulose)Lignin

    Corn stover 37.5 22.4 17.6

    Corn fiber 14.28 16.8 8.4

    Pine wood 46.4 8.8 29.4

    Popular 49.9 17.4 18.1

    Wheat straw 38.2 21.2 23.4

    Switch grass 31.0 20.4 17.6

    Office paper 68.6 12.4 11.3

    Composition of Selected Ligncellulosic Resouces, % dry weight

    Adapted from N. Mosier et al., 2005. Biores Technol. 96:673-686

  • 102030405060PPM708090100110

    Xyl nrb C1,

    int bC1

    MeGA C4

    MeGA C1

    Acetone CH3

    MeGA

    OCH3

    Xyl intC4

    60.898.5

    83.4

    103.3 77.2

    31.5

    Quantification of MeGA substitution 4-O-methylglucuronoxylan by 13C-NMR

    Sweetgum glucuronoxylan

    Xylose/MeGA

    Sweetgum 6-7

    Yellow Poplar 6-7

    Sugarcane bagasse >10

  • Dilute Acid Hydrolysis of Methylglucuronoxylan

    Hydrolysis H2SO4 0.5%, 121 oC

    (Xyl-Xyl-Xyl-Xyl-Xyl-Xyl-Xyl-Xyl-Xyl-Xyl-Xyl-Xyl-)n

    MeGA MeGA

    Xyl-Xyl

    MeGA

    Xyl+

    }MeGA(X)n

    20-31% Cfermxyl:MeGA=10-6

    Xyl

    MeGA

  • Fermentation products (mM)

    Succinate Lactate Formate Acetate Butanediol Ethanol Ethanol yield

    (% of theoretical)a

    E. a. JDR-1 12.7 5.6 15.0 25.2 13.4 42.6 19.2

    E. a. JDR-1

    (pLOI555)2.2 1.2 3.6 4.2 ND 217.4 98.0

    Xylose fermentation products from E.asburiae

    JDR-1 and E.asburiae JDR-1 E1 (pfl- , pLOI155)

    a: Yield of 100% theoretical defined as 5 mole ethanol formed/ 3 mole xylose

    consumed.

  • • Gram-negative Enterobacter asburiae E1 (pLOI555) produced ethanol from glucuronoxylan hydrolysate in a theoretical yield of 98% compared to 63% for Gram-negative Escherichia coli KO11.

    • The genetic basis for this metabolic potential may be transferred to E. coli and Klebsiella biocatalysts for more efficient bioconversion of hemicellulose hydrolysates to biofuels and chemicals.

    Summary 1

  • Technologies for Saccharification of Hemicellulose

    Treatment Xylose Aldouronate Inhibitors

    Steam Explosion X,X2,X3 MeGAX1,2,3 < 0.1% Furfural

    Dilute Acid, 140oC X MeGAX < 0.25% Furfural

    AFEX, 160oC Xn MeGAXn

    0.1 M Ca(OH)2GH10 xylanase

    X2, X3 MeGAX3

  • Pretreatment of O-acetyl-arabinoglucuronoxylan and

    enzymatic depolymerization of 4-O-methylglucuronoxylan

  • Properties of xylanolytic Paenibacillus sp.

    JDR-2 selected for growth on MeGX

    0

    0.1

    0.2

    0.3

    0.4

    0.5

    0.6

    0.7

    0.8

    0.9

    1

    0 5 10 15 20 25 30 35 40

    Hours of Growth

    OD

    600 n

    m

    0.2% GAXn

    0.2% GAX1

    0.27% GlucoseMeGAXn

    MeGAX

    Glucose

  • Paenibacillus sp. strain JDR-2 (27227837)

    Triplicate CBM 22 GH 10 CD CBM 9 SLH

    Catalytic

    Nucleophile

    E262

    Catalytic

    Acid

    E138

    A

    B DC

    Modular architecture of XynA1 secreted by

    Paenibacillus sp. JDR-2

  • yesN yesM ytcQ lplB ytcP xynA2aguA xynB

    Predicted

    polycistronic

    mRNAs

    = rho-independent terminator

    = transcriptional promotor

    0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 kb

    G GG

    G = cre, catabolite repression motif

    Aldouronate-

    utilization operon

    xynA1

    G

    Endoxylanase A1

    G

    Regulation of expression of aldouronate-utilization genes in Paenibacillus JDR-2

  • MeGAX

    MeGA

    Ethanol

    MeGAX

    MeGAX3

    MeGAX3

    ABC

    ABC

    X3

    Xylose

    AguA

    XyloseXynA2

    XynB

    Fermentation

    Lactate

    MeGAXn

    XynA1

    H2SO4

    Acetate

    Succinate

    Processing of Aldouronic Acids by Paenibacillus sp. JDR

  • Depolymerization of MeGXn with Xyl10B and AguA

    from thermophilic Thermotoga maritima

    Lane 1 and 7: standards

    of MeGX1-4Lane 2 and 6: standards

    of X1-4Lane 3: sweetgum with

    the Xyl10B

    Lane 4: sweetgum xylan

    with Xyl10B and AguA

    Lane 5. sweetgum xylan

    1 2 3 4 5 6

    7

    Xyl10B + + -

    AguA - + -

  • Summary 2

    Cell-surface anchored GH10 xylanases catalyze depolymerization

    of glucuronoxylan and vectoral processing of products.

    Bacteria endowed with this capability may be developed for

    direct conversion of hemicellulosic resources to biobased products

    Thermophilic α-glucuronidases and endoxylanases produced in

    planta may enhance xylan bioconversion by bacterial biocatalysts.

    These systems may allow the application of alkaline pretreatment

    protocols to reduce costs and increase yields of fuels and chemicals

    from agicultural residues and energy crops.

  • Pretreatment

    Agricultural

    Residues

    Energy

    Crops

    Lignin

    Cellulose

    Hemicellulose

    Solid

    Waste

    Thermal

    Conversion

    Hydrogen

    (Fuel)

    Chemical

    Feedstocks

    Bioconversion

    Fuels

    (ethanol, butanol)

    Chemical

    Feedstocks

    Options for Biomass and Solid Waste Conversion to Energy

  • Acknowledgements

    Virginia Chow, Adnon Hasona, Guang Nong, John Rice, Franz St. John,

    Lorraine Yomano, and Kheir Zuobi-Hasona

    Dr. Sheilachu P. Gomez, Florida Center for Renewable Chemicals and Fuels,

    University of Florida.

    US Department of Energy Grants DE FC36-99GO10476 and DE FC36-

    00GO10594.

    The Consortium for Plant Biotechnology Research Project OR22072-94.

    Current funding from the Florida Energy Systems Consortium

    Institute of Food and Agricultural Sciences, University of Florida Experiment

    Station, as CRIS Project MCS 3763.