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Wastewater Treatment Facilities: Biorefinery for Biofuels T. French, R. Hernandez, A. Mondala, J. Hall, G. Zhang, M. White, E. Alley, B. Holmes Dave C.

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Presentation on theme: "Wastewater Treatment Facilities: Biorefinery for Biofuels T. French, R. Hernandez, A. Mondala, J. Hall, G. Zhang, M. White, E. Alley, B. Holmes Dave C."— Presentation transcript:

1 Wastewater Treatment Facilities: Biorefinery for Biofuels T. French, R. Hernandez, A. Mondala, J. Hall, G. Zhang, M. White, E. Alley, B. Holmes Dave C. Swalm School of Chemical Engineering Mississippi State University

2 Objectives Transform the daily disposal of industrial and domestic sewage into large quantities of lipids using microorganisms Integrate the lipid, sugar, and thermochemical platforms for producing JP-Fuels, gasoline, biodiesel and chemicals web.mit.edu

3 Evaluation of BioDiesel Production Costs Soybean Oil $4.38/gal feedstock cost $0.35/gal processing cost $0.10/gal transportation cost = $4.83/gal total cost Note: Feedstock represent ~90% of total processing costs

4 Sustainability and Logistical Barriers to Biofuels The US Consumes approximately 300,000,000,000 gal/yrThe US Consumes approximately 300,000,000,000 gal/yr –165,000,000,000 gal/yr gasoline – 75,000,000,000 gal/yr diesel Ethanol would account for 2%Ethanol would account for 2% –Must be transported via tanker –Lower energy density than gas –Requires a lot of water –Where will all the steel come from to build Fermentors Soy Bean oil accounts for 0.33%Soy Bean oil accounts for 0.33% When populations need that for food fuel will loseWhen populations need that for food fuel will lose Not Sustainable.Not Sustainable. Single-cell oil produced in a wastewater treatment facility will not have a food marketSingle-cell oil produced in a wastewater treatment facility will not have a food market Wastewater treatment will always occur and scales with population.Wastewater treatment will always occur and scales with population.

5 COMPARISON OF OIL PRODUCTION FROM FEEDSTOCKS Sample% OilTime (D) Soybean19105 Canola33255 Camelina36255 Turnip36255 Flax39240 Tallow46365 Castor55195 H. matrinalis232.5 R. glutinis16-602.5 R. opacus60-802.0

6 WASTEWATER AS CARBON SOURCE Wastewater contains: –Carbon –Nitrogen –Phosphorous –Water –Micronutrients Approximately 10 million gallons* of wastewater are produced daily in Starkville –Residential waste –Industrial waste

7 35 Billion Gallons of Municipal Wastewater Generated Daily

8 Forced Main Primary Clarification Air Aeration Tank Finished Effluent to Discharge Waste Sludge Biogas Anaerobic Digestor Grit Dewatering & Thickening Influent blending Grit Removal Headworks Influent Secondary Clarification Recycled Biomass Solids Effluent Wastewater Primary Solids Thickening Dewatering Biosolids Thickened Waste Sludge Primary Sludge Influent

9 COMPARISON OF GROWTH CURVES Oleaginous Yeast Grown on Wastewater with 0.1g/L of Dextrose 0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4 020406080 Time (hr) Optical Density (600nm) R. glutinis C. curvatus Pos. Control: R. glutinis Pos. Control: C. curvatus Negative control: wastewater Oleaginous Yeast Grown on Wastewater with 1g/L of Dextrose 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 020406080 time (hr) optical density (600nm) R. glutinis C. curvatus Pos. control: R. glutinis Pos. control: C. curvatus Negative control: wastewater

10 CHEMICAL OXYGEN DEMAND 10% Oil Content

11 Carbon Sources Supporting Growth of Oleaginous Microorganisms Sugars –Glucose –Xylose –Ribose –N-acetyl glucosamine Glycerol Flour

12 Lignocellulosic Biomass switchgrass Composition

13 Conversion of Lignocellulosic Biomass to Microbial Oil Sugar Cell mass concentrationTotal Lipid production. in culture g/L% dry wt. Xylose1530 Dextrose2050 Artificial acid hydrolysate1635 Switch Grass Hydrolysates2.6326

14 Conversion of 30 g/L Acid Hydrolysate by Oleaginous Microbes

15 Conversion of 45 g/L Acid Hydrolysate by Oleaginous Microbes

16 Fatty Acid Composition Caproic (6:0) 0.0 0.00.00.00.00.0 Myristic (14:0) 0.00.00.03.00.0 Palmitic (16:0) 14.02.24.023.39.9 Stearic (18:0) 7.0 7.00.92.417.93.6 Oleic (18:1) 32.012.665.038.019.1 Linoleic (18:2) 20.012.117.30.055.6 Linolenic (18:3) 3.08.07.80.010.2 Eicosatrienoic (20:3) 8.07.41.30.00.2 Behenic (22:0) 0.00.70.40.00.3 Erucic (22:1) 0.049.90.10.00.0 YeastRapeCanolaTallowSoy Fatty Acid

17 Envisioned Process: The New Biorefineries Lignocellulose 3 B G/Yr

18 Example Biorefinery Locations

19 ACKNOWLEDGEMENTS Department of Energy Environmental Protection Agency MS/AL Sea Grant 23 students

20 Thank You


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