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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

Biomass Conversion to Biofuel and Biobased Product

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Samir Khanal, Professor of Biological Engineering Molecular Biosciences and Bioengineering at UHM, describes an integrated approach in converting biomass into biofuel and biobased products. Slides from the REIS seminar series at the University of Hawaii at Manoa on 2009-10-22.

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Page 1: Biomass Conversion to Biofuel and Biobased Product

Samir K. Khanal, Ph.D., P.E.Assistant Professor of Bioengineering

Dept. of Molecular Biosciences and BioengineeringUniversity of Hawai’i at Mānoa

October 22, 2009

Page 2: Biomass Conversion to Biofuel and Biobased Product

Presentation Outline

Background

Cellulosic-ethanol with ultrasound pretreatment

Fungal fermentation of biomass to ethanol

Biofuel residues for fish feed production

Syngas fermentation to ethanol

Page 3: Biomass Conversion to Biofuel and Biobased Product

Why is “Biorenewables” so Important?

Provide biofuels and biobased chemicals

Improve environmental quality

Improve national security

Contribute to sustainable development

Page 4: Biomass Conversion to Biofuel and Biobased Product

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)

Page 5: Biomass Conversion to Biofuel and Biobased Product

Cellulosic Biomass to Ethanol

US Biomass Resource Potential

368

998

1366

0 500 1000 1500

Forestresources

Agriculturalresources

Total resources

Million dry ton per yearSource: USDA and USDOE, Apr 2005

Page 6: Biomass Conversion to Biofuel and Biobased Product

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 750Mton Land requirement @ 10 ton/acre 75 Macre 100 MGY biorefinery 600 each @ 160 mile2 (125 K acr)

gal/ton

Page 7: Biomass Conversion to Biofuel and Biobased Product

Lignocellulosic Biomass Structure

• Cellulose• Hemicellulose• Lignin

Page 8: Biomass Conversion to Biofuel and Biobased Product

How an Engineer can Visualize!

Reinforced concrete Plant cell wall material

Page 9: Biomass Conversion to Biofuel and Biobased Product

Distillation EthanolDrying

Stillage

Sugarcane-based ethanol

Cellulose Conversion

Hydrolysis

Starch-based ethanol

Cellulose-based ethanol

Cellulose PretreatmentCellulose

• Crop residues: corn stover, rice straw, wheat straw, bagasse etc.

• Forestry residues• Energy crops: switchgrass, poplar,

Miscanthus, many others

Ferment-ationSugarSugar

Cane

CornKernels

Starch Conversion(Cook or

Enzymatic Hydrolysis)

Biochemical Pathway for Biofuel Production

ThermochemicalConversion

• Heat and Power• Biofuels and Biochemicals

Animal Feed or Solid fuel Separator

Liquid Stream

Biogas(CH4)

Anaerobic Digester

Boiler

Steam

Product Dryer

VIDEO

Page 10: Biomass Conversion to Biofuel and Biobased Product

(Hybrid Saccharification & Fermentation)

Pretreatment Conditioning

Co-fermentationof C5 & C6

Sugars

ProductRecovery Products

By-products

EnzymeProduction

EnzymaticHydrolysis

Residue Processing

HSF

Ethanol YieldsEthanol Concentration

Xylose YieldXylose Degradation

Reactor CostsSolids Loading

Sugar Losses

Glucose YieldSolids Loading

Feedstock VariationFeedstock Quality

Enzyme Cost

RateHydrolyzate Toxicity

Feedstock Cost

NREL. 2007. Biochemical Ethanol Process and Barriers. 30by30

Biochemical Conversion

Page 11: Biomass Conversion to Biofuel and Biobased Product

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-lignininteraction.

Page 12: Biomass Conversion to Biofuel and Biobased Product

Enzyme hydrolysis of pretreated lignocellulosic biomass (animation)

Hydrolysis

G

G

G

Pretreatment

G: GlucoseEnzyme

LigninHemicellulose

Lignocellulosic biomass

G

G

GG G

G

G

CBH1 from T. reesei (from NREL)

SEM (corn stover)

Page 13: Biomass Conversion to Biofuel and Biobased Product
Page 14: Biomass Conversion to Biofuel and Biobased Product

Biomass Pretreatment

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

Alkaline or

Page 15: Biomass Conversion to Biofuel and Biobased Product

Ammonia Pretreatment of Switchgrass

Switchgrass(40 g)

Ammoniatreatment

1:1.5 (29.6%)Washing(with DI water)

Sonication(30 and 90 µm)

Cellulaseenzyme

24hr incub. Reducing sugar

Weight Loss : 13.5%

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

HYDROLYSATE AT DAY 4Hydrolysate

Page 16: Biomass Conversion to Biofuel and Biobased Product

Effect of Sonication on Microstructure

Control

Ultrasound treatment: 40 sec

Page 17: Biomass Conversion to Biofuel and Biobased Product

Change in Microstructure

Control

Ultrasound treatment: 40 sec

Page 18: Biomass Conversion to Biofuel and Biobased Product

Reducing Sugar Release

Page 19: Biomass Conversion to Biofuel and Biobased Product

Fungal Fermentation of Biomass to Ethanol

Ethanol

Lignocellulose

White rot fungi

Brown rot fungi Yeast

Cellulose & hemicellulose

liquor

Sugar-rich

liquor

Sugar-rich

Page 20: Biomass Conversion to Biofuel and Biobased Product

Corn fiber (cellulose 16.5%, hemicellulose 45%, lignin ~ 1.5%, 37% others – protein, oil, ash etc.)

Corn fiber(25 g)

Addition offungal mycelia

Enzyme Induction(2 days)

AnaerobicIncubation(with yeast)

Ethanol determination

Experimental Steps

Page 21: Biomass Conversion to Biofuel and Biobased Product

Brown rot

(Gloeophyllum

trabeum)

White rot

(Phanerochaete chrysosporium)

Soft rot(Trichoderma reesei)

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)

Trained cormorantswith neckrings led

to the submergenceof the culture idea

Page 22: Biomass Conversion to Biofuel and Biobased Product

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

Page 23: Biomass Conversion to Biofuel and Biobased Product

• 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

Summary

Page 24: Biomass Conversion to Biofuel and Biobased Product

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.

Page 26: Biomass Conversion to Biofuel and Biobased Product

Selection of Fungi

Genus: RhizopusSpecies: microsporus

Kingdom: FungiPhylum: ZygomycotaOrder: MucoralesFamily: Mucoraceae

50 µm

Page 27: Biomass Conversion to Biofuel and Biobased Product

Parameters Molasses vinasse

Sugarcane juice 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 (g/l)

63.95 ± 4.84 68.35 ± 1.48

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

Vinasse Characteristics

Page 28: Biomass Conversion to Biofuel and Biobased Product

Rhizopus oligosporus could directly utilize vinasses fromboth molasses and sugarcane juice fermentations assubstrates for its growth without any treatment or nutrientsupplementation.

The optimal pH for fungal biomass production is 5.

Fungal biomass yields of 0.61 and 0.60 (g fungal biomassincrease/g fungal biomass initial) were obtained fromgrowing fungus on molasses vinasse and sugarcane juicevinasse, respectively.

SCOD removal of about 20 and 50% were obtained fromeffluents after harvesting fungal biomass from molassesvinasse and sugarcane juice vinasse, respectively.

Some Findings

Page 29: Biomass Conversion to Biofuel and Biobased Product

Fungal Pellets

Page 30: Biomass Conversion to Biofuel and Biobased Product

Draft-tube Batch Experiments

Aeration off → Floating mycelial pelletsAeration on

Page 31: Biomass Conversion to Biofuel and Biobased Product

YM medium

Sugarcane juice vinasse

Molasses vinasse

Dried Fungal Biomass

Page 32: Biomass Conversion to Biofuel and Biobased Product

Cellulose -Ethanol: Syngas Fermentation

•Acid/enzyme hydrolysis of cellulose/hemicellulose to hexose/pentose

•Ethanol fermentation from hexose/pentose

•Convert all the biomass to syngas (H2+CO)

•Ethanol fermentation from syngas

•High cost of pretreatment and enzyme

•Leaving lignin for disposal

•Gas/liquid mass transfer limitation due to poor solubility of CO and H2

• Inhibitory acetic acid as by-product

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

Page 33: Biomass Conversion to Biofuel and Biobased 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

Page 34: Biomass Conversion to Biofuel and Biobased Product

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.

Page 35: Biomass Conversion to Biofuel and Biobased Product

Acknowledgements

Graduate students: Prachand Shrestha, Mary Rasmussen ConocoPhillips USDA and UDDOEADM P&G

Page 36: Biomass Conversion to Biofuel and Biobased Product

Books

Biofuel and Bioenergy from Biowastes and Biomass

Samir K. khanal (lead editor)

American Society of Civil Engineers

Page 37: Biomass Conversion to Biofuel and Biobased Product

THANK YOU