fermentable sugars for biofuels
DESCRIPTION
Fermentable sugars for Biofuels. Donal F. Day Audubon Sugar Institute UNO Sept. 2014. Target: regionally appropriate biomass feedstocks. Questions to be Answered Agricultural Are these crops suitable for production in underutilized agricultural areas (Cold tolerance)? Industrial - PowerPoint PPT PresentationTRANSCRIPT
FERMENTABLE SUGARS FOR BIOFUELS
Donal F. Day
Audubon Sugar Institute
UNO Sept. 2014
The deep south states can to produce 50% of the biofuels in the future because they have the most available land with adequate water and sun.
Questions to be Answered
Agricultural
Are these crops suitable for production in underutilized agricultural areas (Cold tolerance)?
Industrial
Are the products (syrups) suitable for use by industrial partners?
Financial-Environmental
What is the financial baseline for producing biofuels from these crops and what are the environmental costs associated with the production?
Target: regionally appropriate biomass feedstocks
CROP CHOICES (POTENTIAL YIELDS)
Wet ton/acre
40.5
lbs simpleSugar/acre
123.6
lbs complexSugar/acre
362.3
Total lbsSugar/acre
19,679
Wet ton/acre
24.3
lbs simpleSugar/acre
184.1
lbs complexSugar/acre
186.4
Total lbsSugar/acre
9,003
Energycane Sweet Sorghum
TASKS
Feedstock Development
Sustainable Production
Logistics and processing
Conversion and Refining
Economics, Markets and Distribution
Education
Extension
Crops with staggered harvests that will grow across desired range (and not compete with food crops)
Low input, sustainable production
Harvest, transport, effective range
Conversion to sugars (syrups) suitable for jet fuel production
Establishment, market, selling costs
Training of potential workers for new industry
Bringing stakeholders on-board
Approaches
APR
ZSM-5
Gasoline
Diesel
KeroseneJet Fuel
Condensation Hydrotreating
Biomass
SugarCane
CornStarch
Sustainable Production Harvest Deliver
ProcessIntermediate ProductConversion to Fuel
Biomass
ProcessIndeterminate
analyzeFeedstock developmentSustainability
Technology development
Technology development
Economic feasibilityValue to Consumer
Developing Process
Primary processing plants supplying centralized biorefineries
Storable syrups as feedstocksPrimary plants drawing on local acreage
*Industrial Model
Sweet Sorghum July - September
Energycane October -March
Bagasse, syrup,woodchips,molasses, etc.
April - June
Staggered Harvest, Complementary Crops, producing both fermentable sugars and biomass.
*Agricultural Model
SUSTAINABLE PRODUCTIONEXPERIMENTAL SITES
Sites were established in Louisiana in different soil types and climatic zones for growing energycane and sweet sorghum.
FEEDSTOCK DEVELOPMENT
Energy cane- seven molecular markers have been found, four for leaf greenness and three for regrowth damage. Genetic variability was created by cross hybridization between a set of distinct species
Cross pollination between sugarcane and miscanthus, F1 in field tests across Louisiana
Cold tolerance testing of Energy cane in North Louisiana location
Low input testing in North Louisiana
One semi-commercial variety released
Breeding for Cold Tolerance
Molecular markers developed for cold
tolerance
St. Gabriel (early June 2013)
Energycane grows fasterThan commercial varieties
Energycane
sugarcane
ENERGYCANE – YEAR 3 (N. LOUISIANA
June 2014
SWEET SORGHUM
Annual crop
Contains, a sugar containing juice, starch containing seed heads and fiber
90-120 day crop cycle, can be grown across target region
Gross structure similar to sugarcane
Can be widely grown across Southern US
SWEET SORGHUM PRODUCTION FOLLOWING LEGUME INCORPORATION IN THE SOIL (LOW INPUT TESTING)
HARVESTINGSweet Sorghum Energy cane
Weight loss- 6-7% over 72 hr. period on harvesting3 trials, one acre lots (about 18 rows) 8 inch billets, 3 different fan speeds evaluated
7-9% weight loss over a 72 hr. period. Same design.Harvesting in October
TOTAL FOSSIL ENERGY USE (LCA)
Brazilian sugar cane
4 (50% - 74%)
3 (25% - 49%)
2 (1% - 24%)
Biofuel FeedstockProduction Feasibility
Index
5 (75% - 100%)
1 (no change)
Energy Cane ProductionFeasibility Scale
Crop Market Price Crop Yield Variable Cost
Energy cane
CornCottonSorghumRiceSoybeansSugarcane
$75/ton
$5.00/bu.$0.80/lb.
$8.00/bu.$16.00/cwt.$14.00/bu.
$0.23/lb.
10 dry ton/A
160 bu./A1,200 lb./A
90 bu./A70 cwt./A45 bu./A
7,500 lbs./A
$500/A
$530/A$600/A$310/A$660/A$340/A$530/A
Feedstock Breakeven Economic Analysis
PROCESSING- DEMONSTRATE SCALABILITYPRODUCE PRODUCTS FOR INDUSTRIAL TESTING
Plant operational- initial process run July 2013
Flexible Pilot Plant: Education, Extension and Training Facility
PILOT PLANT
MILLING
Sweet Sorghum Energy Cane
Three runs of 5 ton lots. For two runs the whole plant was harvested, for one the seed heads and leaves were removed.
Feed rate low. It was not possible to mill the clean billets because of choking (not enough fiber).
Feed rate dependent on variety.
Leaf removal necessary to improve efficiency.
Increased power requirement due to high fiber content.
Sweet sorghum and energycane fall at different ends for fiber.
POWER REQUIREMENTS- MILLING (CROP DEPENDENT)
Eiland and Clarke, 2008 ASSCT, Panama City, Florida
Sweet Sorghum
Energy Cane
Sugarcane
COMPOSITION SORGHUM SYRUP
27.1 % Water
72.9 % Dissolved Solids
8.4 % Ash
13.2 % Glucose
11.2 % Fructose
46 % Sucrose
0.1 % S0.1 % P0.25 % N
3.5 % Potassium
1.1 % Chloride
0.4 % Calcium0.3 % Sulfate0.2 % Sodium0.2 % Magnesium
0.7 % Nitrate
0.1 % Ammonium0.1 % Phosphate
FUELS PRODUCTION -VIRENT ENERGY SYSTEMS
APR
ZSM-5
Gasoline
Diesel
KeroseneJet Fuel
Condensation Hydrotreating
Biomass
SugarCane
CornStarch
COMPOSITION SORGHUM SYRUP
27.1 % Water
72.9 % Dissolved Solids
8.4 % Ash
13.2 % Glucose
11.2 % Fructose
46 % Sucrose
0.1 % S0.1 % P0.25 % N
3.5 % Potassium
1.1 % Chloride
0.4 % Calcium0.3 % Sulfate0.2 % Sodium0.2 % Magnesium
0.7 % Nitrate
0.1 % Ammonium0.1 % Phosphate
Removal of potassium and chloride requires advanced separation techniques such as
• Ion exchange• Electrodialysis• Nanofiltration
LIGNOCELLULOSIC UTILIZATION
CO-GENERATION
Scenario 1Excess bagasse used for electric power
generation
Scenario 2Excess bagasse used for lignocellulosic
sugars production
FeedstockPrimary sugars,
million kg
Excess bagasse, million t
Power export, million kWh
Syrup, K-m3
Primary sugars,
million kg
Excess bagasse, million t
Lignocellulosic sugars,
million kg
Syrup, K-
m3
Energy cane
99.8 600.8 268 50.5 99.8 330.2 85.8 94.1
Sweet Sorghum
49.6 164.2 119.9 24.9 49.6 147.4 38.9 44.5
Facility total
149.4 765.0 387.9 75.4 149.4 477.6 124.7 138.6
Annual production of fermentable sugars, excess bagasse, electric power and syrup
Model developed in SUGARSTM
Extraction by diffusion Diluted acid pretreatment for lignocellulosic
conversion
LIGNOCELLULOSIC LOGISTICS AND PRE-PROCESSING
Storage Pile storage best for short-term biomass storage
Fragmentation patterns on milling
(the lower the fiber the less fragmentation)
Particle size effects pretreatment rates
SURPLUS SUGARS PER DAY (10,000 T/D)
Fiber Composition: 40% Cellulose (C6-Glucose) & 25% Hemicellulose (C5-Xylose)Grinding Rate : 10,000 tons/day , Bagasse Production : 3000 tons/day
Power Bagasse can be fluidized for steam drying, increasing energy value.
SUGARS FROM LIGNOCELLULOSE
Unlike starch (corn), lignocellulose is made of tightly bonded sugars (cellulose, hemicellulose) and lignin
The primary technical problem
is economic access to the carbohydrates in this matrix.
IDEALIZED PROCESS
Pretreatment
APR
ZSM-5
Gasoline
Diesel
KeroseneJet Fuel
Condensation Hydrotreating
Biomass
SugarCane
CornStarch
Syrup
PRETREATMENT TECHNOLOGIES
Treatment
Temperature
oC
Pressure(atm)
Time(min)
acid 190-200 3-15 2-30
water 160-190 6-14 10-30
ammonia 150-170 9-17 30-60
lime 70-130 1-6 60-360
oxidizers 20-100 1 3-60
As yet there is no low cost ideal pretreatment
Pretreated
Post -hydrolysis
PretreatmentDilute Ammonia (DA) Pretreatment
SEM Images of Untreated and Treated Sugarcane, Energy Cane and Sorghum Bagasse
Aita, G., Salvi, D., Walker, M. 2011. "Enzyme hydrolysis and ethanol fermentation of dilute ammonia pretreated energy cane." Bioresource Technology, 102 (6): 4444-4448.
Salvi, D., Aita, G., et al. 2010. "Dilute ammonia pretreatment of sorghum and its effectiveness on enzyme hydrolysis and ethanol fermentation." Applied Biochemistry and Biotechnology, 161 (1-8): 67-74.
Sugarcane bagasse
Energy cane bagasse
Sorghum bagasse
Untreated
Treated
A
B
C
D
E
F
ENZYMATIC SUGAR PRODUCTION
Start
3 hours
6 hours
40 hrs
sugar yield - 70-90% of cellulose in biomass converted to fermentable
sugars
OTHER P
RODUCTS
BU
T AN
OL ;
AC
ON
I TI C
AC
I D B
I OP
L AS
TI C
S
IMMOBILIZED CELL COLUMNS
Laboratory Small Scale-up
BUTANOL PRODUCTION COMPARISON
Batch Fermentation with 4% glucose
Continuous Culture (0.6 ml/min) with 4% glucose
0.42% butanol 0.61% butanol
0.60% solvents 0.99% solvents
Anoxic conditions needed Anoxic conditions maintained
1.5 L media used (5 days) 4.32 L media used (5 days)
3 L reaction vessel 400 ml reaction vessel
0.6 g solvents/L/day 21.384 g solvents/L/day
Research financed by Optinol LLC
Simplified Plant Designtentative
(GLUCOSE TO BUTANOL)
Product ConcentrationScale-up
36
ACONITIC ACID IS AN ABUNDANT ORGANIC ACID IN SUGARCANE, ENERGYCANE AND SWEET SORGHUM.
Aconitic acid ~1% on Brix solids
Found in molasses at 3-5%
Used as flavor ingredient and adjuvant (up to 300 ppm)
Similar to citric acid
O
OH
O
O
O
O OH
OO
Aconitic acid“Green Plastic”
BIO-PLASTICS MATRICES FROM ACONITIC ACID
Biodegradablephotolithotrophicplastics from sugarcane materials
POLYESTER FROM ORGANIC ACID.
Trans-Aconitic Acid Formulation
Citric Acid
Formulation
The trans-aconitic acid is darker in color and contributes to the polymer color.
The citric acid is a white crystalline powder forming a clear polymer with some bubbles.
Cis-Aconitic Acid
Formulation
The cis-aconitic acid is darker in color and contributes to the polymer color.
THANK YOU
Always thinking outside the box
This work supported by a USDA AFRI-Cap grant (Award No. 2011-69005-30515)