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Samir K. Khanal, Ph.D., P.E.
             Assistant Professor of Bioengineering
Dept. of Molecular Biosciences and Bioengineering
                     University of Hawai’i at Mānoa

                                 October 22, 2009
Presentation Outline


 Background

 Cellulosic-ethanol with ultrasound pretreatment

 Fungal fermentation of biomass to ethanol

 Biofuel residues for fish feed production

 Syngas fermentation to ethanol
Why is “Biorenewables” so Important?


   Provide biofuels and biobased
    chemicals

   Improve environmental quality

   Improve national security

   Contribute to sustainable
    development
What is Biomass?
 Agricultural   crops and residues,
    forestry residues, energy crops,
    municipal wastes and other
    organic waste materials.


  Bana grass and guinea is a high
yield energy crop readily available
in Hawaii.
(Yield: 45 to 100 Mg/ha-yr)
Cellulosic Biomass to Ethanol


                       US Biomass Resource Potential

Total resources
                                                                     1366

    Agricultural
    resources                                     998

       Forest
     resources          368

                   0            500                  1000                   1500

                              Million dry ton per year
                                  Source: USDA and USDOE, Apr 2005
Cellulosic Biomass to Ethanol


                                 Gasoline (B gals)   Ethanol equivalent (B gals)
US consumption, 2004             139                 200
60% from imports                 83                  120
30% displacemnt                  42                  60
Biomass need at 80 ton/acre
                   gal/ton                           750Mton
Land requirement @ 10 ton/acre                       75 Macre
100 MGY biorefinery                                  600 each @ 160 mile2 (125 K acr)
Lignocellulosic Biomass Structure

• Cellulose
• Hemicellulose
• Lignin
How an Engineer can Visualize!




    Reinforced concrete   Plant cell wall
                          material
Biochemical Pathway for Biofuel Production
                                               Cellulose-based ethanol

                                                        Starch-based ethanol


      VIDEO
                                                                Sugarcane-based ethanol



                               Sugar                    Ferment-                                    Ethanol
                                           Sugar                     Distillation      Drying
                               Cane                       ation

                               Starch
             Corn            Conversion
            Kernels
                              (Cook or                                Stillage
                             Enzymatic                                                              Steam
                             Hydrolysis)


                              Cellulose            Animal Feed or                                    Boiler
                                                                      Separator
               Cellulose     Conversion               Solid fuel                          Biogas
Cellulose     Pretreatment
                                                                                    Liquid (CH4)
                              Hydrolysis                                                              Product
                                                                                    Stream
                                                                                                       Dryer
      • Crop residues: corn stover, rice
        straw, wheat straw, bagasse etc.                                                Anaerobic
                                                                                         Digester
      • Forestry residues                  •   Heat and Power
                    Thermochemical
      • Energy crops: switchgrass, poplar, •
                      Conversion               Biofuels and Biochemicals
        Miscanthus, many others
Biochemical Conversion

                         Feedstock Variation                               Enzyme Cost
                                                    Enzyme
                         Feedstock Quality
                         Feedstock Cost            Production



                                                                 HSF (Hybrid Saccharification & Fermentation)
                                                                          Co-
                                                  Enzymatic          fermentation        Product
      Pretreatment         Conditioning                                                                  Products
                                                  Hydrolysis          of C5 & C6         Recovery
                                                                        Sugars

                          Sugar Losses

                                               Glucose Yield
    Xylose Yield
    Xylose Degradation
                                               Solids Loading                             Residue
                                                                                         Processing
    Solids Loading
    Reactor Costs
                                                                Ethanol Yields
                                                                Ethanol Concentration
                                                                Rate
                                                                Hydrolyzate Toxicity
                                                                                         By-products



NREL. 2007. Biochemical Ethanol Process and Barriers. 30by30
Why Pretreatment is Needed?
Pretreatment is essential to facilitate easy access
of enzymes to cellulose/hemi-cellulose:

1. To solubilize lignin.

2. To dissolve hemi-
   cellulose.

3. To disrupt a cellulose-
   hemi-cellulose-lignin
   interaction.
Enzyme hydrolysis of pretreated lignocellulosic biomass
 (animation)

     Enzyme       Lignocellulosic
G:   Glucose
                  biomass
      Lignin
       Hemicell
       ulose


                                            SEM (corn stover)




        Pretreatment
                                                                    CBH1 from T. reesei (from NREL)
                                                        G
                                    Hydrolysis                                 G       G




                                                                                             G
                                                                       G


                                                                                           G
                                                   G
                                                                G
                                                                           G          G
Biomass Pretreatment
                                  Alkaline or




 Ultrasound pretreatment  increase in pore volume  30 to 500oA
 Reduce crystalline structure of cellulose
 Reduce the enzyme loading and improve the rate of reaction
 Enhance sugar release  subsequent ethanol yield/ton of biomass
Ammonia Pretreatment of Switchgrass

               Ammonia                                            Cellulase
                              Washing           Sonication
Switchgrass    treatment                                           enzyme
                              (with DI water)   (30 and 90 µm)
   (40 g)     1:1.5 (29.6%)                                      24hr incub.     Reducing
                                                                                  sugar




                                                                               Cellulose: 45%
                                                                               Hemicellulose:
                                                                               31.4%
                                                                               Lignin: 12%


       Hydrolysate
  HYDROLYSATE AT DAY 4



                                    Weight Loss : 13.5%
Effect of Sonication on Microstructure




      Control




                       Ultrasound treatment: 40 sec
Change in Microstructure




  Control




                 Ultrasound treatment: 40 sec
Reducing Sugar Release
Fungal Fermentation of Biomass to Ethanol

                     Brown rot fungi                  Yeast
Lignocellulose

                                        Sugar-rich
                                                              Ethanol
                                         liquor


                 Cellulose & hemicellulose

                                         Sugar-rich

                                          liquor



                      White rot fungi
Experimental Steps
    Corn fiber (cellulose 16.5%, hemicellulose 45%,
     lignin ~ 1.5%, 37% others – protein, oil, ash etc.)


                 Addition of   Enzyme      Anaerobic
    Corn fiber     fungal      Induction   Incubation     Ethanol determination
     (25 g)       mycelia      (2 days)    (with yeast)
White rot                        Brown rot                       Soft rot

   (Phanerochaete                    (Gloeophyllum               (Trichoderma
   chrysosporium)                                                 reesei)
                                         trabeum)




                                         Trained cormorants
                                         with neckrings led
                                        to the submergence
                                          of the culture idea
Inside an incubator (37oC) during anaerobic incubation. Each bottle contained
 25 gram corn fiber, 650ml of respective fungal pellets, 150 ml of yeast media
              without glucose and 2ml of yeast cells (S. cerevisiae)
SSF with white and brown rot fungi converted ~ 9 % of fiber to ethanol on weight basis
SSF with T. reesei converted only ~ 5 % of fiber to ethanol on weight basis
Summary
• Ultrasound pretreatment resulted a significant
  disintegration of cellulosic micro-fibrils

• Following sonication of switchgrass, reducing
  sugar yield improved by 70% with respect to
  control

• Fungal process was able to hydrolyze cellulosic
  biomass

• Over 10% of the corn fiber was converted to
  ethanol through fungal fermentation alone
Fungal Fermentation
   Source of protein for animals, even for humans.

   Fungi prefer acidic condition (pH 4.0).

   High in lysine, 5.5% (DDGS 0.62%, soybean meal
    3.0%) → co-fed with DDG to non-ruminants.

   Source of valuable fungal byproducts such as
    enzymes, chitin/chitosan, and lactic acids.

   Easy recovery of fungal biomass with high
    quality water for reuse.
Fungal Species of Interest
Selection of Fungi

             Kingdom: Fungi
             Phylum: Zygomycota
             Order: Mucorales
             Family: Mucoraceae

            Genus: Rhizopus
            Species: microsporus




    50 µm
Vinasse Characteristics

Parameters                       Molasses          Sugarcane juice
                                 vinasse           vinasse
pH                               3.85 ± 0.00       3.88 ± 0.01

Chemical oxygen demand (g/l)     86.52 ± 5.32      86.79 ± 7.38

Soluble chemical oxygen demand   63.95 ± 4.84      68.35 ± 1.48
(g/l)
Total solids (%)                 5.12 ± 0.00       2.46 ± 0.04


Suspended solids (%)             1.25 ± 0.10       0.59 ± 0.02

Volatile solids (%)              3.55 ± 0.00       1.77 ± 0.02

Volatile suspended solids (%)    1.07 ± 0.06       0.53 ± 0.02

Total Kejdahl nitrogen (mg/l)    1088.36 ± 10.65   336.72 ± 4.61

Potassium (mg/l)                 5598.00 ± 48.65   1533.33 ±
                                                   152.75
Some Findings
Rhizopus oligosporus could directly utilize vinasses from
both molasses and sugarcane juice fermentations as
substrates for its growth without any treatment or nutrient
supplementation.

The optimal pH for fungal biomass production is 5.

Fungal biomass yields of 0.61 and 0.60 (g fungal biomass
increase/g fungal biomass initial) were obtained from
growing fungus on molasses vinasse and sugarcane juice
vinasse, respectively.

SCOD removal of about 20 and 50% were obtained from
effluents after harvesting fungal biomass from molasses
vinasse and sugarcane juice vinasse, respectively.
Fungal Pellets
Draft-tube Batch Experiments




  Aeration on        Aeration off →   Floating mycelial pellets
Dried Fungal Biomass




                  Sugarcane juice vinasse




      YM medium



                      Molasses vinasse
Cellulose -Ethanol: Syngas Fermentation
  Lignocellulosic biomass
  - 40–50% cellulose, 20–40% hemicellulose and 10–20% lignin
  - can yield 60 billion gallons of fuel-grade ethanol per year in the US




• Acid/enzyme hydrolysis of
                                               • Convert all the biomass to
  cellulose/hemicellulose to
                                                 syngas (H2+CO)
  hexose/pentose
                                               • Ethanol fermentation from
• Ethanol fermentation from
                                                 syngas
  hexose/pentose

                                              • Gas/liquid mass transfer
• High cost of pretreatment                     limitation due to poor
  and enzyme                                    solubility of CO and H2
• Leaving lignin for disposal                 • Inhibitory acetic acid as by-
                                                product
33


   Mesoporous Silica (MPS) functionalized by amine group
      •Parallel structure of silica having homogenous mesoporous (2-50 nm)
       pores
      → high area-to-mass ratio and accessibility
      •Permanent bonding of amine on the silica structure
      → Selective adsorption of acetic acid (-NH3+…Ac-)
      → Regenerable by pH control




R=-(CH2)3NH2 or –(CH2)3NH(CH2)2NH(CH2)2NH2
Some Issues with Biofuels
• Potential impact on food/feed supplies due to
land use.
• Possible increase in agricultural products prices
(due to biofuel feedstocks production).
• Likely to impact biodiversity.
• Degradation of soil quality/soil erosion.
• Increased use of fertilizer and pesticides.
• May impact water quality and quantity.
Acknowledgements

 Graduate students: Prachand Shrestha, Mary
Rasmussen
ConocoPhillips
 USDA and UDDOE
ADM
 P&G
Books
 Biofuel and Bioenergy from Biowastes
 and Biomass




 Samir K. khanal (lead editor)

 American Society of Civil Engineers
THANK YOU

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Biomass Conversion to Biofuel and Biobased Product

  • 1. Samir K. Khanal, Ph.D., P.E. Assistant Professor of Bioengineering Dept. of Molecular Biosciences and Bioengineering University of Hawai’i at Mānoa October 22, 2009
  • 2. Presentation Outline  Background  Cellulosic-ethanol with ultrasound pretreatment  Fungal fermentation of biomass to ethanol  Biofuel residues for fish feed production  Syngas fermentation to ethanol
  • 3. Why is “Biorenewables” so Important?  Provide biofuels and biobased chemicals  Improve environmental quality  Improve national security  Contribute to sustainable development
  • 4. What is Biomass?  Agricultural crops and residues, forestry residues, energy crops, municipal wastes and other organic waste materials.  Bana grass and guinea is a high yield energy crop readily available in Hawaii. (Yield: 45 to 100 Mg/ha-yr)
  • 5. Cellulosic Biomass to Ethanol US Biomass Resource Potential Total resources 1366 Agricultural resources 998 Forest resources 368 0 500 1000 1500 Million dry ton per year Source: USDA and USDOE, Apr 2005
  • 6. Cellulosic Biomass to Ethanol Gasoline (B gals) Ethanol equivalent (B gals) US consumption, 2004 139 200 60% from imports 83 120 30% displacemnt 42 60 Biomass need at 80 ton/acre gal/ton 750Mton Land requirement @ 10 ton/acre 75 Macre 100 MGY biorefinery 600 each @ 160 mile2 (125 K acr)
  • 7. Lignocellulosic Biomass Structure • Cellulose • Hemicellulose • Lignin
  • 8. How an Engineer can Visualize! Reinforced concrete Plant cell wall material
  • 9. Biochemical Pathway for Biofuel Production Cellulose-based ethanol Starch-based ethanol VIDEO Sugarcane-based ethanol Sugar Ferment- Ethanol Sugar Distillation Drying Cane ation Starch Corn Conversion Kernels (Cook or Stillage Enzymatic Steam Hydrolysis) Cellulose Animal Feed or Boiler Separator Cellulose Conversion Solid fuel Biogas Cellulose Pretreatment Liquid (CH4) Hydrolysis Product Stream Dryer • Crop residues: corn stover, rice straw, wheat straw, bagasse etc. Anaerobic Digester • Forestry residues • Heat and Power Thermochemical • Energy crops: switchgrass, poplar, • Conversion Biofuels and Biochemicals Miscanthus, many others
  • 10. Biochemical Conversion Feedstock Variation Enzyme Cost Enzyme Feedstock Quality Feedstock Cost Production HSF (Hybrid Saccharification & Fermentation) Co- Enzymatic fermentation Product Pretreatment Conditioning Products Hydrolysis of C5 & C6 Recovery Sugars Sugar Losses Glucose Yield Xylose Yield Xylose Degradation Solids Loading Residue Processing Solids Loading Reactor Costs Ethanol Yields Ethanol Concentration Rate Hydrolyzate Toxicity By-products NREL. 2007. Biochemical Ethanol Process and Barriers. 30by30
  • 11. Why Pretreatment is Needed? Pretreatment is essential to facilitate easy access of enzymes to cellulose/hemi-cellulose: 1. To solubilize lignin. 2. To dissolve hemi- cellulose. 3. To disrupt a cellulose- hemi-cellulose-lignin interaction.
  • 12. Enzyme hydrolysis of pretreated lignocellulosic biomass (animation) Enzyme Lignocellulosic G: Glucose biomass Lignin Hemicell ulose SEM (corn stover) Pretreatment CBH1 from T. reesei (from NREL) G Hydrolysis G G G G G G G G G
  • 13.
  • 14. Biomass Pretreatment Alkaline or  Ultrasound pretreatment  increase in pore volume  30 to 500oA  Reduce crystalline structure of cellulose  Reduce the enzyme loading and improve the rate of reaction  Enhance sugar release  subsequent ethanol yield/ton of biomass
  • 15. Ammonia Pretreatment of Switchgrass Ammonia Cellulase Washing Sonication Switchgrass treatment enzyme (with DI water) (30 and 90 µm) (40 g) 1:1.5 (29.6%) 24hr incub. Reducing sugar Cellulose: 45% Hemicellulose: 31.4% Lignin: 12% Hydrolysate HYDROLYSATE AT DAY 4 Weight Loss : 13.5%
  • 16. Effect of Sonication on Microstructure Control Ultrasound treatment: 40 sec
  • 17. Change in Microstructure Control Ultrasound treatment: 40 sec
  • 19. Fungal Fermentation of Biomass to Ethanol Brown rot fungi Yeast Lignocellulose Sugar-rich Ethanol liquor Cellulose & hemicellulose Sugar-rich liquor White rot fungi
  • 20. Experimental Steps  Corn fiber (cellulose 16.5%, hemicellulose 45%, lignin ~ 1.5%, 37% others – protein, oil, ash etc.) Addition of Enzyme Anaerobic Corn fiber fungal Induction Incubation Ethanol determination (25 g) mycelia (2 days) (with yeast)
  • 21. White rot Brown rot Soft rot (Phanerochaete (Gloeophyllum (Trichoderma chrysosporium) reesei) trabeum) Trained cormorants with neckrings led to the submergence of the culture idea Inside an incubator (37oC) during anaerobic incubation. Each bottle contained 25 gram corn fiber, 650ml of respective fungal pellets, 150 ml of yeast media without glucose and 2ml of yeast cells (S. cerevisiae)
  • 22. SSF with white and brown rot fungi converted ~ 9 % of fiber to ethanol on weight basis SSF with T. reesei converted only ~ 5 % of fiber to ethanol on weight basis
  • 23. Summary • Ultrasound pretreatment resulted a significant disintegration of cellulosic micro-fibrils • Following sonication of switchgrass, reducing sugar yield improved by 70% with respect to control • Fungal process was able to hydrolyze cellulosic biomass • Over 10% of the corn fiber was converted to ethanol through fungal fermentation alone
  • 24. Fungal Fermentation  Source of protein for animals, even for humans.  Fungi prefer acidic condition (pH 4.0).  High in lysine, 5.5% (DDGS 0.62%, soybean meal 3.0%) → co-fed with DDG to non-ruminants.  Source of valuable fungal byproducts such as enzymes, chitin/chitosan, and lactic acids.  Easy recovery of fungal biomass with high quality water for reuse.
  • 25. Fungal Species of Interest
  • 26. Selection of Fungi Kingdom: Fungi Phylum: Zygomycota Order: Mucorales Family: Mucoraceae Genus: Rhizopus Species: microsporus 50 µm
  • 27. Vinasse Characteristics Parameters Molasses Sugarcane juice vinasse vinasse pH 3.85 ± 0.00 3.88 ± 0.01 Chemical oxygen demand (g/l) 86.52 ± 5.32 86.79 ± 7.38 Soluble chemical oxygen demand 63.95 ± 4.84 68.35 ± 1.48 (g/l) Total solids (%) 5.12 ± 0.00 2.46 ± 0.04 Suspended solids (%) 1.25 ± 0.10 0.59 ± 0.02 Volatile solids (%) 3.55 ± 0.00 1.77 ± 0.02 Volatile suspended solids (%) 1.07 ± 0.06 0.53 ± 0.02 Total Kejdahl nitrogen (mg/l) 1088.36 ± 10.65 336.72 ± 4.61 Potassium (mg/l) 5598.00 ± 48.65 1533.33 ± 152.75
  • 28. Some Findings Rhizopus oligosporus could directly utilize vinasses from both molasses and sugarcane juice fermentations as substrates for its growth without any treatment or nutrient supplementation. The optimal pH for fungal biomass production is 5. Fungal biomass yields of 0.61 and 0.60 (g fungal biomass increase/g fungal biomass initial) were obtained from growing fungus on molasses vinasse and sugarcane juice vinasse, respectively. SCOD removal of about 20 and 50% were obtained from effluents after harvesting fungal biomass from molasses vinasse and sugarcane juice vinasse, respectively.
  • 30. Draft-tube Batch Experiments Aeration on Aeration off → Floating mycelial pellets
  • 31. Dried Fungal Biomass Sugarcane juice vinasse YM medium Molasses vinasse
  • 32. Cellulose -Ethanol: Syngas Fermentation Lignocellulosic biomass - 40–50% cellulose, 20–40% hemicellulose and 10–20% lignin - can yield 60 billion gallons of fuel-grade ethanol per year in the US • Acid/enzyme hydrolysis of • Convert all the biomass to cellulose/hemicellulose to syngas (H2+CO) hexose/pentose • Ethanol fermentation from • Ethanol fermentation from syngas hexose/pentose • Gas/liquid mass transfer • High cost of pretreatment limitation due to poor and enzyme solubility of CO and H2 • Leaving lignin for disposal • Inhibitory acetic acid as by- product
  • 33. 33 Mesoporous Silica (MPS) functionalized by amine group •Parallel structure of silica having homogenous mesoporous (2-50 nm) pores → high area-to-mass ratio and accessibility •Permanent bonding of amine on the silica structure → Selective adsorption of acetic acid (-NH3+…Ac-) → Regenerable by pH control R=-(CH2)3NH2 or –(CH2)3NH(CH2)2NH(CH2)2NH2
  • 34. Some Issues with Biofuels • Potential impact on food/feed supplies due to land use. • Possible increase in agricultural products prices (due to biofuel feedstocks production). • Likely to impact biodiversity. • Degradation of soil quality/soil erosion. • Increased use of fertilizer and pesticides. • May impact water quality and quantity.
  • 35. Acknowledgements  Graduate students: Prachand Shrestha, Mary Rasmussen ConocoPhillips  USDA and UDDOE ADM  P&G
  • 36. Books Biofuel and Bioenergy from Biowastes and Biomass Samir K. khanal (lead editor) American Society of Civil Engineers