Techno-Economic Analysis of Biochemical Scenarios for Production of Cellulosic Ethanol

A techno-economic analysis on the production of cellulosic ethanol by fermentation was conducted to understand the viability of liquid biofuel production processes within the next 5-8 years. Initially, 35 technologies were reviewed, then a two-step down selection was performed to choose scenarios to be evaluated in a more detailed economic analysis. The lignocellulosic ethanol process was selected because it is well studied and portions of the process have been tested at pilot scales. Seven process variations were selected and examined in detail. Process designs were constrained to public data published in 2007 or earlier, without projecting for future process improvements. Economic analysis was performed for an 'nth plant' (mature technology) to obtain total investment and product value (PV). Sensitivity analysis was performed on PV to assess the impact of variations in process and economic parameters. Results show that the modeled dilute acid pretreatment process without any downstream process variation had the lowest PV of $3.40/gal of ethanol ($5.15/gallon of gasoline equivalent) in 2007 dollars. Sensitivity analysis shows that PV is most sensitive to feedstock and enzyme costs.

[1]  R. Elander,et al.  Process and economic analysis of pretreatment technologies. , 2005, Bioresource technology.

[2]  Andrew J. McAloon,et al.  Ethanol production by continuous fermentation–pervaporation: a preliminary economic analysis , 2000 .

[3]  Farzaneh Teymouri,et al.  Optimization of the ammonia fiber explosion (AFEX) treatment parameters for enzymatic hydrolysis of corn stover. , 2005, Bioresource technology.

[4]  Christopher W. Myers,et al.  Understanding cost growth and performance shortfalls in pioneer process plants , 1981 .

[5]  A. Faaij,et al.  Ethanol from lignocellulosic biomass: techno-economic performance in short-, middle- and long-term , 2005 .

[6]  Seungdo Kim,et al.  Recent process improvements for the ammonia fiber expansion (AFEX) process and resulting reductions in minimum ethanol selling price. , 2008, Bioresource technology.

[7]  B. Norment The Energy Independence and Security Act of 2007 , 2011 .

[8]  F. P. Eddy,et al.  Two-stage dilute-acid pretreatment of softwoods , 2000, Applied biochemistry and biotechnology.

[9]  M. Ruth,et al.  Lignocellulosic Biomass to Ethanol Process Design and Economics Utilizing Co-Current Dilute Acid Prehydrolysis and Enzymatic Hydrolysis Current and Futuristic Scenarios , 1999 .

[10]  A. Aden,et al.  Process Design Report for Stover Feedstock: Lignocellulosic Biomass to Ethanol Process Design and Economics Utilizing Co-Current Dilute Acid Prehydrolysis and Enzymatic Hydrolysis for Corn Stover , 2002 .

[11]  Toshi Hayashi,et al.  Understanding process plant schedule slippage and startup costs , 1986 .

[12]  M. Galbe,et al.  Process Considerations and Economic Evaluation of Two‐Step Steam Pretreatment for Production of Fuel Ethanol from Softwood , 2004, Biotechnology progress.

[13]  A. Aden Biochemical Production of Ethanol from Corn Stover: 2007 State of Technology Model , 2008 .

[14]  M. Galbe,et al.  Techno‐Economic Evaluation of Producing Ethanol from Softwood: Comparison of SSF and SHF and Identification of Bottlenecks , 2008, Biotechnology progress.

[15]  Mark Holtzapple,et al.  Comparative sugar recovery data from laboratory scale application of leading pretreatment technologies to corn stover. , 2005, Bioresource technology.

[16]  John N. Saddler,et al.  An integrated model for the technical and economic evaluation of an enzymatic biomass conversion process , 1991 .

[17]  Klaus D. Timmerhaus,et al.  Plant design and economics for chemical engineers , 1958 .