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Full-Text Articles in Operations Research, Systems Engineering and Industrial Engineering

Techno-Economic Analysis Of Advanced Biofuel Production Based On Bio-Oil Gasification, Qi Li, Yanan Zhang, Guiping Hu Sep 2015

Techno-Economic Analysis Of Advanced Biofuel Production Based On Bio-Oil Gasification, Qi Li, Yanan Zhang, Guiping Hu

Industrial and Manufacturing Systems Engineering Publications

This paper evaluates the economic feasibility of a hybrid production pathway combining fast pyrolysis and bio-oil gasification. The conversion process is simulated with Aspen Plus® for a 2000 t d-1 facility. Techno-economic analysis of this fast pyrolysis and bio-oil gasification pathway has been conducted to assess the economic feasibility. A total capital investment of $438 million has been estimated and the minimum fuel selling price (MSP) is $5.6 per gallon of gasoline equivalent. The sensitivity analysis shows that the MSP is most sensitive to internal rate of return, fuel yield, biomass feedstock cost, and fixed capital investment. Monte-Carlo simulation ...


Life Cycle Assessment Of The Production Of Hydrogen And Transportation Fuels From Corn Stover Via Fast Pyrolysis, Yanan Zhang, Guiping Hu, Robert C. Brown Jul 2014

Life Cycle Assessment Of The Production Of Hydrogen And Transportation Fuels From Corn Stover Via Fast Pyrolysis, Yanan Zhang, Guiping Hu, Robert C. Brown

Industrial and Manufacturing Systems Engineering Publications

This life cycle assessment (LCA) evaluates and quantifies the environmental impacts of the production of hydrogen and transportation fuels from the fast pyrolysis and upgrading of corn stover. Input data for this analysis come from Aspen Plus modeling, a GREET model database and a U.S Life Cycle Inventory Database. SimaPro 7.3 software is employed to estimate the environmental impacts. The results indicate that the net fossil energy input is 0.25 MJ and 0.23 MJ per km traveled for a light-duty vehicle fueled by gasoline and diesel fuel, respectively. Bio-oil production requires the largest fossil energy input ...


Integrated Supply Chain Design For Commodity Chemicals Production Via Woody Biomass Fast Pyrolysis And Upgrading, Yanan Zhang, Guiping Hu, Robert C. Brown Apr 2014

Integrated Supply Chain Design For Commodity Chemicals Production Via Woody Biomass Fast Pyrolysis And Upgrading, Yanan Zhang, Guiping Hu, Robert C. Brown

Industrial and Manufacturing Systems Engineering Publications

This study investigates the optimal supply chain design for commodity chemicals (BTX, etc.) production via woody biomass fast pyrolysis and hydroprocessing pathway. The locations and capacities of distributed preprocessing hubs and integrated biorefinery facilities are optimized with a mixed integer linear programming model. In this integrated supply chain system, decisions on the biomass chipping methods (roadside chipping vs. facility chipping) are also explored. The economic objective of the supply chain model is to maximize the profit for a 20-year chemicals production system. In addition to the economic objective, the model also incorporates an environmental objective of minimizing life cycle greenhouse ...


Mild Catalytic Pyrolysis Of Biomass For Production Of Transportation Fuels: A Techno-Economic Analysis, Rajeeva Thilakaratne, Tristan Brown, Yihua Li, Guiping Hu, Robert C. Brown Jan 2014

Mild Catalytic Pyrolysis Of Biomass For Production Of Transportation Fuels: A Techno-Economic Analysis, Rajeeva Thilakaratne, Tristan Brown, Yihua Li, Guiping Hu, Robert C. Brown

Industrial and Manufacturing Systems Engineering Publications

A techno-economic analysis of mild catalytic pyrolysis (CP) of woody biomass followed by upgrading of the partially deoxygenated pyrolysis liquid is performed to assess this pathway’s economic feasibility for the production of hydrocarbon-based biofuels. The process achieves a fuel yield of 17.7 wt% and an energy conversion of 39%. Deoxygenation of the pyrolysis liquid requires 2.7 wt% hydrogen while saturation of aromatic rings in the pyrolysis liquid increases total hydrogen consumption to 6.4 wt%. Total project investment is $457 million with annual operating costs of $142 million for a 2000 metric ton per day facility. A ...


Techno-Economic Analysis Of Co-Located Corn Grain And Corn Stover Ethanol Plants, Longwen Ou, Tristan Brown, Rajeeva Thilakaratne, Guiping Hu, Robert C. Brown Jan 2014

Techno-Economic Analysis Of Co-Located Corn Grain And Corn Stover Ethanol Plants, Longwen Ou, Tristan Brown, Rajeeva Thilakaratne, Guiping Hu, Robert C. Brown

Industrial and Manufacturing Systems Engineering Publications

The goal of this paper is to evaluate the economic performance of co-located corn grain ethanol (Gen 1) and cellulosic ethanol (Gen 2) facilities. We present six scenarios to evaluate the impact of stover-to-grain mass (SGM) ratios on overall minimum ethanol selling price (MESP). For the Gen 1 plant, MESP is $3.18/ gasoline gallon equivalent (GGE) while for the Gen 2 plant it is $5.64/GGE. Co-located Gen 1 and Gen 2 plants operating at the lowest SGM ratio of 0.4 generates the lowest overall MESP of $3.73/GGE as well as the highest MESP for ...


Regional Differences In The Economic Feasibility Of Advanced Biorefineries: Fast Pyrolysis And Hydroprocessing, Tristan Brown, Rajeeva Thilakaratne, Robert C. Brown, Guiping Hu Jun 2013

Regional Differences In The Economic Feasibility Of Advanced Biorefineries: Fast Pyrolysis And Hydroprocessing, Tristan Brown, Rajeeva Thilakaratne, Robert C. Brown, Guiping Hu

Industrial and Manufacturing Systems Engineering Publications

This analysis identifies the sensitivity of the fast pyrolysis and hydroprocessing pathway to facility location. The economic feasibility of a 2000 metric ton per day fast pyrolysis and hydroprocessing biorefinery is quantified based on 30 different state-specific facility locations within the United States. We calculate the 20-year internal rate of return (IRR) and net present value (NPV) for each location scenario as a function of state- and region-specific factors. This analysis demonstrates that biorefinery IRR and NPV are very sensitive to bio-oil yield, feedstock cost, location capital cost factor, and transportation fuel market value. The IRRs and NPVs generated for ...


Techno-Economic Analysis Of Fast Pyrolysis And Upgrading Facilities Employing Two Depolymerization Pathways, Yanan Zhang, Tristan Brown, Guiping Hu, Robert C. Brown Jun 2013

Techno-Economic Analysis Of Fast Pyrolysis And Upgrading Facilities Employing Two Depolymerization Pathways, Yanan Zhang, Tristan Brown, Guiping Hu, Robert C. Brown

Industrial and Manufacturing Systems Engineering Publications

We evaluate the economic feasibility of fast pyrolysis and upgrading facilities 11 employing either of two depolymerization pathways: two-stage hydrotreating 12 followed by a FCC (fluid catalytic cracking) stage or single-stage hydrotreating 13 followed by a hydrocracking stage. In the hydrotreating/FCC pathway, two options 14 are available as the hydrogen source for hydrotreating: merchant hydrogen or 15 hydrogen from natural gas reforming. The primary products of the hydrotreating/FCC 16 pathway are commodity chemicals whereas the primary products for the 17 hydrotreating/hydrocracking pathway are transportation fuels and hydrogen. The two 18 pathways are modeled using Aspen Plus® for ...


Techno-Economic Analysis Of Biomass To Transportation Fuels And Electricity Via Fast Pyrolysis And Hydroprocessing, Tristan Brown, Guiping Hu Apr 2013

Techno-Economic Analysis Of Biomass To Transportation Fuels And Electricity Via Fast Pyrolysis And Hydroprocessing, Tristan Brown, Guiping Hu

Industrial and Manufacturing Systems Engineering Publications

A previous Iowa State University (ISU) analysis published in 2010 investigated the technical and economic feasibility of the fast pyrolysis and hydroprocessing of biomass, and concluded that the pathway could produce cellulosic biofuels for a minimum fuel selling price (MFSP) of $2.11/gal. The 2010 ISU study was largely theoretical in that no commercial-scale fast pyrolysis facilities were being constructed at the time of publication.

The present analysis expands upon the 2010 ISU study by performing an updated techno-economic analysis of the fast pyrolysis and hydroprocessing pathway. Recent advances in pathway technology and commercialization and new parameters suggested by ...


Comparative Techno-Economic Analysis Of Biohydrogen Production Via Bio-Oil Gasification And Bio-Oil Reforming, Yanan Zhang, Tristan Brown, Guiping Hu, Robert C. Brown Apr 2013

Comparative Techno-Economic Analysis Of Biohydrogen Production Via Bio-Oil Gasification And Bio-Oil Reforming, Yanan Zhang, Tristan Brown, Guiping Hu, Robert C. Brown

Industrial and Manufacturing Systems Engineering Publications

This paper evaluates the economic feasibility of biohydrogen production via two bio-oil processing pathways: bio-oil gasification and bio-oil reforming. Both pathways employ fast pyrolysis to produce bio-oil from biomass stock. The two pathways are modeled using Aspen Plus® for a 2000 t d-1 facility. Equipment sizing and cost calculations are based on Aspen Economic Evaluation® software. Biohydrogen production capacity at the facility is 147 t d-1 for the bio-oil gasification pathway and 160 t d-1 for the bio-oil reforming pathway. The biomass-to-fuel energy efficiencies are 47% and 84% for the bio-oil gasification and bio-oil reforming pathways, respectively. Total capital investment ...


Techno-Economic Analysis Of Monosaccharide Production Via Biomass Fast Pyrolysis, Yanan Zhang, Tristan Brown, Guiping Hu, Robert C. Brown Jan 2013

Techno-Economic Analysis Of Monosaccharide Production Via Biomass Fast Pyrolysis, Yanan Zhang, Tristan Brown, Guiping Hu, Robert C. Brown

Industrial and Manufacturing Systems Engineering Publications

The economic feasibility of a facility producing monosaccharides, hydrogen and transportation fuels via fast pyrolysis and upgrading pathway was evaluated by modeling a 2000 dry metric ton biomass/day facility using Aspen Plus®. Equipment sizing and cost were based on Aspen Economic Evaluation® software. The results indicate that monosaccharide production capacity could reach 338 metric tons/day. Co-product yields of hydrogen and gasoline were 23.4 and 141 metric tons/day, respectively. The total installed equipment and total capital costs were estimated to be $210 million and $326 million, respectively. A facility internal rate of return (IRR) of 11.4 ...


Techno-Economic Analysis Of Biobased Chemicals Production Via Integrated Catalytic Processing, Tristan Brown, Yanan Zhang, Guiping Hu, Robert C. Brown Jan 2012

Techno-Economic Analysis Of Biobased Chemicals Production Via Integrated Catalytic Processing, Tristan Brown, Yanan Zhang, Guiping Hu, Robert C. Brown

Industrial and Manufacturing Systems Engineering Publications

We evaluate the economic feasibility of a fast pyrolysis facility producing biobased commodity chemicals based on various manifestations of Integrated Catalytic Processing (ICP). Five scenarios are analyzed: fluid catalytic cracking (FCC) of whole pyrolysis oil (WPO); one-stage hydrotreating and FCC of WPO; FCC of the aqueous phase of pyrolysis oil (APPO); one-stage hydrotreating and FCC of the APPO; and two-stage hydrotreating followed by FCC of the APPO.

We calculate the internal rate of return (IRR) for each scenario as functions of the costs of feedstock, hydrogen, and catalyst, and projected revenues for the facility. The assumed feedstock cost is $83 ...


Effect Of The Alumina Shell On The Melting Temperature Depression For Aluminum Nanoparticles, Valery I. Levitas, Michelle L. Pantoya, Garima Chauhan, Iris Rivero Aug 2009

Effect Of The Alumina Shell On The Melting Temperature Depression For Aluminum Nanoparticles, Valery I. Levitas, Michelle L. Pantoya, Garima Chauhan, Iris Rivero

Aerospace Engineering Publications

The dependence of aluminum (Al) melting temperature on particle size was studied using a differential scanning calorimeter and thermogravitmetric analyzer for particles encapsulated in an oxide shell. Pressure generation within the Al core leads to an increase in melting temperature in comparison with traditional melting temperature depression calculated using the Gibbs−Thomson equation. On the basis of elasticity theory, the pressure in the Al core at the onset of melting is caused mainly by surface tension at the alumina−air and Al−alumina interfaces. This implies that pressure due to the difference in thermal expansion of aluminum and alumina relaxes ...