superpro design presentation- felix&mathias
TRANSCRIPT
![Page 1: Superpro Design presentation- FeliX&Mathias](https://reader036.vdocument.in/reader036/viewer/2022082619/58716d9c1a28ab58758b6d57/html5/thumbnails/1.jpg)
ABE488
Bioprocessing Biomass for FuelSemester Design Project
SuperPro Designer® by Intelligen, Inc. Version 7.0
University of Illinois at Urbana-ChampaignCollege of Agricultural, Consumer and Environmental Sciences
Department of Agricultural & Biological Engineering Professor Dr. Vijay Singh
Student team: Felix Bredoire & Mathias Barreto12/06/2011
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Design performed
50 million dry grind ethanol / yearConventional Dry Grind
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Main assumptions
• SSF• 98% of enzyme conversion• Recycling streams :– Water from distillation and evaporation– 50% of the thin stillage
• Removal of oil from centrifugation and further separation: germ oil and fiber oil
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SuperPro Flowsheet
![Page 5: Superpro Design presentation- FeliX&Mathias](https://reader036.vdocument.in/reader036/viewer/2022082619/58716d9c1a28ab58758b6d57/html5/thumbnails/5.jpg)
INPUTS• Corn:
– 2962960 lb/day– $0.238/kg
• Enzymes (AA & GA):– 592.6 lb/day– $2.25/kg
• Yeast:– 772.22 lb/day– $1.86/kg
• Water:– 2959968 lb/day– $0.0013/kg
OUTPUTS• Ethanol:
– 967363 lb/day– $0.845/kg
• DDGS:– 1085482 lb/day– $0.215/kg
• Germ oil:– 48801 lb/day– $0.35/kg
• Fiber oil:– 26724 lb/day– $4/kg
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Equipment priceSilo/Bin
3% Stirred Reactor 6%
Fermentor 33%
Stripper Column1%
Rectifier Column 0%
Side stripper Column0% Decanter Centrifuge
1%Heat Exchanger
1%
Evaporator 13%
Drum Dryer 38%
Grinder 4%
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Total plant cost
1. Equipment Purchase Cost; 7,541,000
2. Installation ; 3,016,000
4. Instrumentation ; 754,0005. Insulation ; 226,0006. Electrical; 754,0007. Buildings; 754,0008. Yard Improvement ; 754,000
9. Auxiliary Facilities ; 754,000
10. Engineering; 3,639,000
11. Construction; 5,094,000
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Operating cost
65%3%3%0%
28%
Operating cost
Raw MaterialsFacilityLaborLab/QC/QAUtilities
50%
27%
2%
17%
4%
Detail of utilities
ElectricitySteamCooling WaterChilled WaterSteam (High P)
98% of raw materials = corn
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Contribution of each product to the revenue
Ethanol 200 69%
DDGS21%
germ oil1% fiber oil
9%
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New enzyme
• Operating cost = 3.1% less• Payback time:3.02 years vs. 4.35 years• Manufacturing cost of ethanol= $0.87/L vs. $0.91/L
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Scale up evaluation
25 million 50 million 75 million 100 million 50 million - no enzyme0.82
0.84
0.86
0.88
0.9
0.92
0.94
0.96
0.98
0.954690000000001
0.907350.89946
0.891569999999999
0.867900000000001
annual ethanol production
$/L
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Conclusions & Recommendations
• Ethanol selling price < manufacturing cost Importance of coproducts (DDGS, oil)
• Dependency on the market value of corn (63% of operating cost = corn)
• The bigger the plant, the less the manufacturing cost• Actual plant designed: economically viable• BUT, design can be improved by:– Better enzyme efficiency– Use of corn which does not require enzymes addition