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Presentation Overview• Company Overview• Why Fractionate?• The FWS System • Process Flow • Equipmentq p• Mass Balance Chart• Summary of Fractions• Summary of Enhanced DDGSSummary of Enhanced DDGS• Performance Expectations• Economic Model• PricingPricing• Conclusions• Contact Us
Company Overview• FWS has over 50 years of experience & expertise inthe grain handling and processing industry in NorthAmericaAmerica
• We specialize in the design-build of inland terminals,feed mills, malt plants and water and waste-watert t t l ttreatment plants
• FWS is considered a leader and innovator in theindustrial design-build market place industrial design build market place
• Offices in Canada (Winnipeg & Calgary) and theUnited States (San Diego)
• Active international involvement
About FWS Technologies• FWS began working on its Corn Fractionation System
in December 2003
• Patent Application filed in February 2005
• Our system is currently in the Patent Pending StatusOur system is currently in the Patent Pending Status(File No. 60/649,970)
• A favorable patent opinion was received in May 2006 with thefinalization of the patent expected in the Fall of 2007 finalization of the patent expected in the Fall of 2007
• FWS Technologies is a newly created division within the FWSGroup of Companies and leads the commercialization of thep pFWS Corn Fractionation System
• Key Team Members Include: Glen Foster, Mel Harnett, Rick Chale and Scott MacKenzieChale and Scott MacKenzie
Why Fractionate?
Fractionation removes the non-fermentables from the ethanol production process, helping to:
• Increase Profits
• Maximizing ethanol plant throughput• Maximizing ethanol plant throughput• Creating new and high value co-products• Reducing energy consumption / lowering operating costs
• Lower ethanol plant emissions
The FWS System
The FWS Fractionation System produces three separatefractions:s
• Endosperm Fraction* (high in starch)• Germ Fraction (high in fat/oil)• Germ Fraction (high in fat/oil)• Bran Fraction (high in neutral-detergent fiber (NDF))
*O d f ti iti t i th ti l t i t*Our endosperm fraction composition contains the essential nutrientsto facilitate total fermentation
Ethanol ProductionWithout Fractionation
EthanolEthanol
DDGS
CO2
Ethanol ProductionS
Ethanol
With FWS Fractionation
Endo
Enhanced DDGS
FWS CO2FWSFractionation System
Bran Germ Oil Extraction
FWS Fractionation Plant
Process Flow
T i
Cleaned Corn Input
Tempering
Cracking & Sizing
Density Separation
Bran Processing
Germ Processing
Bran GermEndo
EquipmentThe FWS system uses minimal processing and conveyanceequipment, but includes for your peace of mind, redundancy onsome major components.some major components.
Types of equipment included are:• Cracker Rolls• Size Reduction & Separation Machinery• Density Separating Machines• Flakers
The fractionation system’s total connected load is1200 HP, operating is 850 HP.*
*assuming 20,000,000 mm/bu/yr of corn plant
Mass Balance ChartMass Balance ChartFWS Fractionation System
Wh l C Lb /B E d Lb /B G Lb /B B Lb /B1.30.71.20.90.3
34.0%8.5%
50.5%3.0%1.2%
30.0%15.0%28.0%20.5%6.5%
38.83.72.61.00.5
80.5%7.8%5.4%2.0%
1%
StarchCrude ProteinFiber (NDF)Fat/OilAsh
Whole Corn Lbs/Bu* Endosperm Lbs/Bu * Germ Lbs/Bu * Bran Lbs/Bu*
73.7 %8.4 %9.9 %3.5 %1.4 %
41.34.75.62.00.8
1.20.31.70.10.0
0.0 2.8%0.0%1.63.4%Other
% Run
56.0 48.2 4.4 3.4
86% 8% 6%
3.1 % 1.7 0.1
*- product “As Fed”
Note: Whole corn moisture: 14.5%
Summary of Fractions
C it E dD i ti C it G C it B Composite Endosperm
48.2 lbs(95% of all available starch).15%
7 5 8 0%
Description
Quantity lbs/bu*
.
Moisture*
P t i
Composite Germ
4.4 lbs
.
15%
14-16%
Composite Bran
3.4 lbs
.
14.5%
8-9% 7.5-8.0%2.00%1%
80-81%(10-11% > Whole Corn)
ProteinFat/OilAsh. Starch
14-16%18-22% **6.5%
30%
8-9%3.0%1.2%
34%
5-5.8%
3,80093.3%
.NDFME (kcal.kg)TDNCalciumPh h
.28%
4,460106%
.47-54%
3,680
89.95%
Phosphorus
* All values are dry matter basis with the exception of Moisture and Quantity.** Dependant on test method used
Summary of Enhanced DDGS
Description
Quantity lbs/bu*
Moisture*
Protein * *
Enhanced DDGS
12.5-13 lbs
10%
35-37%
Fat/Oil
Ash
Starch
NDF
6.5%
3.8%
3-5%
21%NDF
ME (kcal.kg)
TDN
Calcium
21%
3,800
88%
0.06%
Phosphorus 0.6%
* All values are dry matter basis with the exception of Moisture and Quantity.** 9 - 12% increase over standard DDGS product 9 12% increase over standard DDGS product
Performance Expectations
Expected Result
Contains greater than 93.5% of available starch
Contains greater than .80 lbs of fat/oil per bushel of whole
Fraction
Endosperm
Germ g p
Contains greater than 1.3 lbs of NDF bushel corn processedBran
Economic ModelKey Data Variables used in Economic Model spreadsheet
2.8
5%
10%
Current Conversion Rate
Starch Loss
Ethanol Throughput Increase
$ 2.00
$ 85.00
$
g p
Ethanol Price/gal
Current DDGS Selling Price/ton
Eth l DDGS S lli P i /t $ 100.00
$ 90.00
$ 45.00
Ethanol DDGS Selling Price/ton
Germ Product/ton
Bran Product/ton
$ 2.50
$ 0.61
Corn Price/bushel
Natural Gas/gal
Economic Model
Conversion Rate AssumptionCurrent Process With Fractionation
Economic Modeling Utilizing FWS Technologies Corn Fractionation System:50 MMGY Dry Mill Ethanol Plant
2.8 2.66
RevenuesEthanol
Units Unit Amt Unit Price/Cost Totals Totals
Conversion Rate AssumptionAnnual Ethanol CapacityBushels of Corn Required
gal $ 100 000 000 $ 110 000 000
50,000,00017,857,143
55,000,00020,676,692
10% incr.
EthanolDried Distiller GrainsEnhanced DDGSBranGerm
Total Revenues
galtontontonton
155,357 $129,229 $35,150 $45,489 $
85.00100.0045.0090.00
$ 100,000,000$ 13,205,357
$ 113,205,357
$ 110,000,000
$ 12,922,932$ 1,581,767$ 4,093,985
$ 128,598,684
$ 44,642,857$ 25,500,000$ 70,142,857
$ 43,062,500
CostsCornOperating
Total CostsEBIDTAIncrease EBIDTA
bugal
$$
2.500.61 / 0.53
$ 51,691,729$ 24,750,000$ 76,441,729
$ 52,156,955$ 9 094 455
$ 43,062,500
$ 43 062 500
Increase EBIDTA
EBIDTA (from above)DepreciationInterest ExpenseIncome Tax Expense
N t I
$ 9,094,455$ 52,156,955
$ 52 156 955$ 43,062,500Net Income $ 52,156,955
$ 9,904,455Increased Net Income Utilizing FWS Fractionation System
Pricing• FWS The FWS corn fractionation system is among the most cost
effective systems on the market today.
• Base pricing for a 20 mm/bu/yr fractionation plant starts at $9,000,000USD.* (sized for a 50mm/gal/yr ethanol plant)
• Price includes required cleaning equipment to provide clean, free off i t i l f th f ti ti foreign material, corn for the fractionation process.
• Additional pricing for transportation equipment to deliver product to andfrom fractionation facility and storage facilities for co-products, isavailable upon request available upon request.
* base pricing is for budgetary use only and is subject to change based on layout, actual location, marketconditions and does not include piling and any/all additional site preparation costs.
Conclusions
• On-line application• Produces 3 fractions
• Minimal starch loss• High energy DDGS
Simple Effective
• Conventional operation• Low horsepower• Dry system
g gy• High Oil Germ Fraction• High NDF Bran Fraction• Removes non-fermentables• Reduces chemical requirements• Reduces VOC’s/Improves air quality• Promotes full & efficient fermentationProfitable
• Increased ethanol throughput• Increased ethanol revenues• Low capital cost/quicker payback• New value added co product revenues• New value added co-product revenues• Higher protein DDGS
Contact UsFWS Technologies475 Dovercourt Drive475 Dovercourt DriveWinnipeg, MB Canada R3Y 1G4Phone : 866.722.2275Fax : 866 711 2275Fax : 866.711.2275email us @ info@fwstl.comwww.fwstl.com
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