steele repreve 1 13-11
DESCRIPTION
Dr. Phil Steele, MSU, gives a talk on pyrolysis research, using Freedom Giant Miscanthus. They turned the feedstock miscanthus x giganteus in to gasoline, diesel and aviation fuel. Originally presented at the Freedom Field Day.TRANSCRIPT
The Potential for Production of Fuels from Giant Miscanthus via Pyrolysis
Philip Steele
Professor and SERC
Bio-oil Thrust Leader
Sustainable Energy Research Center
Mississippi State University
Acknowledgements
• This research is based upon work funded through the
Sustainable Energy Research Center at Mississippi State
University and is supported by the Department of Energy
under Award Number DE-FG3606GO86025.
MSU bio-oil objectives:
• Develop more effective pyrolysis reactors to produce high-quality bio-oils at optimum yield
• Upgrade bio-oils to commercial liquid fuels
• Commercialize technologies by demonstration projects and industrial relationships
• Oxygen in bio-oil: 45-50% by weight– Incorporated in oxygenated compounds
• Causes most of the negative properties:– Variable viscosity– High acidity– Pungent odor– Low energy density
Bio-oil challenges:
Development effective auger pyrolysis reactors:
• Auger reactors can be built with reduced capital investment
• Auger reactors are more readily produced at small scale
Giant miscanthus pyrolysis products:
• Giant miscanthus yield is 60% vs 65% for pine wood
• Hydrocarbons can be produced from giant miscanthus bio-oil
The MSU auger reactor design is under MOU to an industrial partner:
• Prototype 10 ton/day reactor built to MSU design is producing bio-oil at 67% yield
• All benchmarks have been met and licensing should be completed during September 2010
• Construction of a 50-ton per day pyrolysis facility planned for 2012
Our proprietary HDO catalyst produces a high-quality hydrocarbon mix:
Hydrogen
Removal of oxygenated compounds
Water + HDO bio-oil
Water
Hydrocarbons
Bio-oil
• Yield is 1.1 bbl of hydrocarbons per dry ton of biomass; this represents 40% (goal = 50%) of the original energy contained in the bio-oil.
Property HDO bio-oil Diesel
Water content (wt%) 0 0
Acid value (mg KOH/g) <0.1 0
Viscosity (cSt @ 40C) 2.8 2.6
HHV (MJ/kg) 45.2 45.8
Carbon (%) 88.6 85.1
Hydrogen (%) 11.4 12.2
Oxygen (%) 0 0
Properties of HDO bio-oil vs diesel:
GC simulated distillation showing fuel components of HDO bio-oil hydrocarbon mixture:
Upgrading bio-oil :
• Lignocellulosic Boiler Fuel (LBF)
LBF combustion flame produced with a drop-in injector replacement module:
Physical and chemical properties of LBF bio-oil:
PropertyRaw
bio-oilLBF
Water Content (%) 24.2 7
Acid value ( mg KOH/g) 89 46
Viscosity (cSt @ 40 oC) 14.53 5.6
HHV (MJ/kg) 17.5 31.9
Upgraded bio-oil :
Anhydrosugars to ethanol or hydrogen
Anhydrosugar production via fast pyrolysis:
• Biomass pretreatments allow anhydrosugars to be generated in significant quantities in the aqueous fraction (MSU = 51% vs previous high of 36%; 30% increase)
• Anhydrosugars can be catalytically reformed to produce hydrogen
Levoglucosan
• Alternatively, the sugar-rich aqueous fraction can be hydrolyzed and fermented to ethanol.
Anhydrosugar production via fast pyrolysis, cont’d:
Raw
bio-oil
Raw bio-oil and fractionation products:
71%
Aqueous phase fraction
29%
Pyroligneous fraction
High percentage of anhydrosugars in bio-oil aqueous fraction (51%); GC/MS spectra:
Scan EI+ TIC
5.43e8
11112008-1
0
%
100
5.00 10.00 15.00 20.00 25.00 30.00 35.00 40.00Time
1.08
1.28
2.55
2.63 2.64
2.66
4.05
4.13
5.00 6.17
7.63
8.48 9.
9710
.40
11.2
412
.09
13.3
6
14.8
315
.33
16.9
717
.81
19.0
519
.47
20.8
022
.06 22
.29
23.7
3
24.9
725
.82
27.1
727
.74 29
.07
30.2
130
.26
30.5
130
.69
31.6
632
.62
33.5
834
.44
35.2
8
36.8
638
.17
39.0
939
.93
40.7
7
Anhydrosugars
Final patent to be filed in October 2010
Raw aqueous fraction before and after filtration of inhibitors; after hydrolysis to glucose:
• We have producedethanol without problem with the hydrolyzed glucose
Future activities:
• Catalytic pyrolysis reactor design is completed and will be built by the end of the year
• A 4-ton per day auger reactor and 100-gal per day hydrotreater and esterified bio-oil production capabilities will be housed in an SERC pilot plant on MSU campus
• MSU auger reactor licensee will commercialize and scale up production based on their success with a 10-ton per day MSU design
Future activities, cont’d:
• Aqueous fraction sugars will be produced from giant miscanthus bio-oil
Philip Steele
Professor and SERC
Bio-oil Thrust Leader
Sustainable Energy Research Center
Mississippi State University
The Potential for Production of Fuels from Giant Miscanthus via Pyrolysis