Biomass conversion to mixed alcohol fuels using the MixAlco process

The MixAlco process is a patented technology that converts any biodegradable material (e.g., sorted municipal solid waste, sewage sludge, industrial biosludge, manure, agricultural residues, energy crops) into mixed alcohol fuels containing predominantly 2-propanol, but also higher alcohols up to 7-tridecanol. The feed stock is treated with lime to increase its digestibility. then, it is fed to a fermentor in which a mixed culture of acid-forming microorganisms produces carboxylic acids. Calcium carbonate is added to the fermentor to neutralize the acids to their corresponding carboxylate salt. The dilute (−3%) carboxylate salts are concentrated to 19% using an amine solvent that selectively extracts water. Drying is completed using multi-effect evaporators. Finally, the dry salts are thermally converted to ketones which subsequently are hydrogenated to alcohols. All the steps in the MixAlco process have been proven at the laboratory scale. A techno-economic model of the process indicates that with the tipping fees available in New York ($126/dry tonne), mixed alcohol fuels may be sold for $0.04/L ($0.16/gal) with a 60% return on investment (ROI). With the average tipping fee in the United States rates ($63/dry tonne), mixed alcohol fuels may be sold for $0.18/L ($0.69/gal) with a 15% ROI. In the case of sugarcane bagasse, which may be obtained for about $26/dry ton, mixed alcohol fuels may be sold for $0.29/L ($1.09/gal) with a 15% ROI.

[1]  D. Hood,et al.  Structure and Amine-Water Solubility in Desalination by Solvent Extraction. , 1960 .

[2]  G. McClellan,et al.  Distillation of Acetate of Lime. , 1924 .

[3]  R. Davison,et al.  Vapor-liquid equilibrium of binary mixtures of triethylamine with propyl and isopropyl alcohol , 1974 .

[4]  Mark T. Holtzapple,et al.  Lime treatment of agricultural residues to improve rumen digestibility , 1997 .

[5]  J. Macy,et al.  Effects of monensin, pyromellitic diimide and 2-bromoethanesulfonic acid on rumen fermentation in vitro. , 1985, Journal of animal science.

[6]  C. D. Hurd The pyrolysis of carbon compounds , 1929 .

[7]  L. L. Slyter Monensin and Dichloroacetamide Influences on Methane and Volatile Fatty Acid Production by Rumen Bacteria In Vitro , 1979, Applied and environmental microbiology.

[8]  Mark T. Holtzapple,et al.  Lime pretreatment of switchgrass , 1997, Applied biochemistry and biotechnology.

[9]  R. R. Davison,et al.  Vapor-liquid equilibrium of triethylamine-water and methyldiethylamine-water , 1971 .

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

[11]  Mark T. Holtzapple,et al.  Pretreatment of lignocellulosic municipal solid waste by ammonia fiber explosion (AFEX) , 1992 .

[12]  D. Hood,et al.  Phase Equilibria of Desalination Solvents: Water-NaCl-Amines , 1966 .

[13]  D. Wise,et al.  Production of acetic acid from thermally treated sewage sludge in an upflow anaerobic reactor , 1992 .

[14]  William L. Goffe,et al.  SIMANN: FORTRAN module to perform Global Optimization of Statistical Functions with Simulated Annealing , 1992 .