11ibbc - 8.1 - mani · 1 m 0.3 m 0.7 m 1 e ~0.2 e 0.9 e external heat supply temp: 180-280oc...

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Pilot Scale Testing of Biomass Torrefaction Technology Sudhagar Mani Assistant Professor, Biological & Agricultural Engineering Faculty of Engineering, University of Georgia, Athens, GA Faculty of Engineering, University of Georgia, Athens, GA Ph: (706) 542 Ph: (706) 542 - - 2358; Email: 2358; Email: [email protected] [email protected]

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Page 1: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Pilot Scale Testing of Biomass

Torrefaction Technology

Sudhagar ManiAssistant Professor, Biological & Agricultural Engineering

Faculty of Engineering, University of Georgia, Athens, GAFaculty of Engineering, University of Georgia, Athens, GA

Ph: (706) 542Ph: (706) 542--2358; Email: 2358; Email: [email protected]@engr.uga.edu

Page 2: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

IntroductionIntroductionIssues with biomass feedstock

• Wide range of moisture content (60-15% wb)

• Low bulk density (4 – 8 lbs/ft3)

• Low energy density (4,500-7,500 Btu/lb)

• Uneven particle sizes (no flow)

• Difficult to handle, store and transport

• High transport and storage cost

• Self heating and emission of off gases during storage

Page 3: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

IntroductionIntroductionIssues with thermoIssues with thermo--chemical conversion chemical conversion technologiestechnologies

•• Combustion/coCombustion/co--firing:firing:

Difficult to coDifficult to co--fire with coalfire with coal

Low energy densityLow energy density

High energy demand for grinding biomassHigh energy demand for grinding biomass

•• GasificationGasification

Tar formation

Low C/H ratio for liquid fuel production

•• Pyrolysis: Pyrolysis:

BioBio--oil instability & coke formationoil instability & coke formation

Page 4: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Biomass Gasification ProcessBiomass Gasification Process

Three step processThree step process1.1. Drying Drying -- evaporated moisture (<200evaporated moisture (<200ooC)C)

2.2. Pyrolysis Pyrolysis –– release of volatiles and char (~450release of volatiles and char (~450ooC)C)

3.3. Partial oxidation of volatiles and char (~800Partial oxidation of volatiles and char (~800ooC)C)

Complex, partial oxidation reactionComplex, partial oxidation reaction

ФФ –– Equivalence Ratio (ER) =Equivalence Ratio (ER) =

For gasification, For gasification, ΦΦ = 0.25 = 0.25 –– 0.50.5

[ ] tarashCHCOHCOOOCH 422heat

26.04.1 +++++⎯⎯→⎯φ+

( )( ) .Stoic

actual

F/AF/A

Page 5: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Biomass vs. CoalBiomass vs. Coal

Torrefied Biomass

Page 6: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

What is Torrefaction? What is Torrefaction? Solid-state thermal hydrolysis of biomass in an inert of biomass in an inert atmosphere (e.g.,Natmosphere (e.g.,N22))Temperature range Temperature range –– 180 to 300180 to 300ooCCHemicelluloseHemicellulose is hydrolyzed is hydrolyzed via release of acetic acid via release of acetic acid and subsequent hydrolysis reaction productsand subsequent hydrolysis reaction productsMoisture reduction, oxygen content reducedMoisture reduction, oxygen content reducedSome extractives volatilized, but 70Some extractives volatilized, but 70--80% solids 80% solids recoveredrecoveredMost familiar example Most familiar example –– roasting coffeeroasting coffee

Green chip Torrefied chip

Page 7: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Mass & Energy Balance

Torrefaction Process

Biomass

Volatile off gases

Torrefiedbiomass

1 m

0.3 m

0.7 m

1 E

~0.2 E

0.9 E

External heat supplyTemp: 180-280oCHeating rate: <50oC/minResidence time: > mins

Condensable:WaterOrganic acids, alcoholsFurans, ketonesTerpenes, phenolsWaxes, tannins, lipids

Non-condensable:H2, CO, CO2, CH4,Toluene, benzene

~0.1 E

Page 8: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Rotary drum reactor Rotary drum reactor –– UGAUGA(indirect heating)(indirect heating)

Capacity = 400 lbs/run

Page 9: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Torrefaction Torrefaction -- Pilot scale testingPilot scale testing

Clean pine chips with less than 1% fines (< ¼inch)

Uniform initial moisture content of 10% (wb)

Temperature conditions – T200, T225, T250, T275 & T300oC

Residence time – 20 & 40 min

Inert gas flow rate was kept constant

Steady state operation

Page 10: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Pilot Unit Pilot Unit –– Torrefied Biomass YieldTorrefied Biomass Yield

Page 11: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Torrefied biomass Torrefied biomass –– Moisture ContentMoisture Content

Page 12: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Torrefied Biomass Torrefied Biomass -- Compositional changesCompositional changes

Biomass  Ash (%) C H N S O/C Ratio

HHV

(MJ/kg)

CT‐PC 0.27 47.9 7.4 0.3 0.14 0.91 18.46

TPC‐200 0.27 50.8 7.3 0.3 0.1 0.82 20.22

TPC‐225 0.27 51.7 7.2 0.3 0.08 0.78 20.83

TPC‐250 0.25 57.8 6.8 0.26 0.08 0.61 23.71

TPC‐275 0.35 67.9 6.5 0.3 0.07 0.38 27.0

TPC­300 0.43 74.3 5.78 0.33 0.05 0.25 30.61

Coal 6.3 77.9 6.7 1.95 2.02 0.16 33.11

Page 13: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,
Page 14: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Torrefaction of Pine ChipsTorrefaction of Pine Chips

Torrefaction Process

Page 15: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Torrefied Biomass Characteristics

Coal like brown biomass

Higher energy density –

(20 to 23 GJ/tonne)

Hydrophobic in nature due to removal of hydroxyl groups – easy storage

Brittle biomass – Less energy required for grinding

Page 16: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Torrefied biomass Torrefied biomass –– Bulk densityBulk density

Page 17: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Improved Improved PelletingPelleting ProcessProcess

Raw material Drying process Drying

Torrefaction Pelletization Products

Raw material Torrefaction

Grinding PelletizationHigh quality Pellets

Page 18: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Results Results –– Grinding EnergyGrinding Energy

Page 19: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Results: Bulk Flow PropertiesResults: Bulk Flow Properties

Biomass grindsa

SPHT(Dimensionless)

Bulk density (kg m-3)

Particle density

(Mg m-3)

Specific grinding energy

consumption (kW h t-1)

Untreated-PC 0.48 381.0 1.40 239.7TPC-225 oC 0.52 342.4 1.41 107.9TPC-250 oC 0.51 331.8 1.40 70.0TPC-275 oC 0.60 376.1 1.37 54.7TPC-300 oC 0.62 400.2 1.34 35.0

Page 20: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Results Results –– Particle Size DistributionParticle Size Distribution

Page 21: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Results Results –– Torrefied Powder Particle SizeTorrefied Powder Particle Size

Page 22: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Effect of Torrefaction on Pellet Density

225

275275

225

Page 23: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

ConclusionsConclusionsTorrefaction is a promising (platform) pretreatment technology for conversion of biomass into fuels & chemicals

During torrefaction, hemi-cellulose was almost hydrolyzed and resulted in higher energy density product with a heating value of more than 23 MJ/kg or 10,000 Btu/lb.

Torrefaction process significantly reduced the specific grinding energy of biomass with up to 10 fold reduction.

Particle size and size distributions were skewed down or narrowed down as torrefaction temp. increases.

Pelleting of torrefied biomass pose some challenges in maintaining the pellet quality

Page 24: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

AcknowledgementResearch Team• Dr. Sudhagar Mani, Team Leader • Dr. KC Das, Director, Biorefinery Program• Dr. J. Kastner, Catalyst Expert• Mr. Ryan Adolphson, Engg. Outreach Director• Brian Bibens, M.Sc. Student • Manunya Phanphanich, M.S. Student• Eric Gobert, Research Technician

Financial Support

Traditional Industries Program of Georgia

The Southern Company Services

Biorefinery grant by Department of Energy

Page 25: 11IBBC - 8.1 - Mani · 1 m 0.3 m 0.7 m 1 E ~0.2 E 0.9 E External heat supply Temp: 180-280oC Heating rate:  mins Condensable: Water Organic acids,

Thank you

Biomass Torrefaction Technology

Direct Combustion or co-firing

Gasification & Fast Pyrolysis

Biochemical conversion

Densification

Value added products –Nano-fibers