Development of novel wheat biorefining: Effect of gluten extraction from wheat on bioethanol production

Abstract Wheat has been used in a novel biorefinery as the sole raw material for the production of bioethanol and some co-products (bran-rich pearlings, gluten and pure yeast cells). Minimisation in waste production has been achieved either by generating co-products from major wheat components that are not required for bioethanol fermentation or by re-generating nutrients contained initially in wheat via microbial autolysis. On-site production of enzymes required to hydrolyse wheat macromolecules has been achieved by Aspergillus awamori fermentation of pearled wheat flour. Complete gluten extraction was made feasible by providing the required amount of free amino nitrogen (FAN) for bioethanol fermentations via on-site fungal autolysis. A wheat to ethanol conversion yield of 0.296 g g −1 , which constitutes 77% of the maximum theoretical conversion (0.385 g ethanol (g wheat) −1 ) calculated from the starch content in the wheat used, has been achieved including the starch requirements for enzyme production. A modified unstructured model has been proposed to describe fermentations of Saccharomyces cerevisiae on wheat-derived media for bioethanol production.

[1]  L. Gustafsson,et al.  Influence of the nitrogen source on Saccharomyces cerevisiae anaerobic growth and product formation , 1996, Applied and environmental microbiology.

[2]  Shuichi Aiba,et al.  Kinetics of product inhibition in alcohol fermentation , 2000, Biotechnology and bioengineering.

[3]  L. Olsson,et al.  Characterization of very high gravity ethanol fermentation of corn mash. Effect of glucoamylase dosage, pre-saccharification and yeast strain , 2005, Applied Microbiology and Biotechnology.

[4]  X. Ge,et al.  Intrinsic kinetics of continuous growth and ethanol production of a flocculating fusant yeast strain SPSC01. , 2006, Journal of biotechnology.

[5]  W. M. Ingledew,et al.  Effect of nitrogen limitaton on synthesis of enzymes in Saccharomyces cerevisiae during fermentation of high concentration of carbohydrates , 1996, Biotechnology Letters.

[6]  O. Levenspiel The monod equation: A revisit and a generalization to product inhibition situations , 1980 .

[7]  Colin Webb,et al.  Optimization and Cost Estimation of Novel Wheat Biorefining for Continuous Production of Fermentation Feedstock , 2007, Biotechnology progress.

[8]  S. C. Oliveira,et al.  Continuous alcoholic fermentation process: model considering loss of cell viability , 1999 .

[9]  Colin Webb,et al.  A whole crop biorefinery system: A closed system for the manufacture of non-food products from cereals. , 2006 .

[10]  C. Webb,et al.  Developing a sustainable bioprocessing strategy based on a generic feedstock. , 2004, Advances in biochemical engineering/biotechnology.

[11]  C. Wilke,et al.  Ethanol effects on the kinetics of a continuous fermentation with Saccharomyces cerevisiae. , 1977, Biotechnology and bioengineering symposium.

[12]  Colin Webb,et al.  Process Design and Optimization of Novel Wheat‐Based Continuous Bioethanol Production System , 2007, Biotechnology progress.

[13]  C. Webb,et al.  Cereal‐based biorefinery development: Integrated enzyme production for cereal flour hydrolysis , 2007, Biotechnology and bioengineering.

[14]  Ioannis K Kookos,et al.  Optimization of Batch and Fed‐Batch Bioreactors using Simulated Annealing , 2004, Biotechnology progress.

[15]  W. M. Ingledew,et al.  Fermentation of very high gravity wheat mash prepared using fresh yeast autolysate , 1994 .

[16]  Alison M. Jones,et al.  Fuel alcohol production: appraisal of nitrogenous yeast foods for very high gravity wheat mash fermentation , 1994 .

[17]  J. Guillamón,et al.  Effect of nitrogen limitation and surplus upon trehalose metabolism in wine yeast , 2005, Applied Microbiology and Biotechnology.

[18]  V. Specchia,et al.  Numerical estimation of biokinetic parameters , 1988 .

[19]  W. M. Ingledew,et al.  High-Gravity Brewing: Effects of Nutrition on Yeast Composition, Fermentative Ability, and Alcohol Production , 1984, Applied and environmental microbiology.

[20]  D. Dubourdieu,et al.  Influence of assimilable nitrogen on volatile acidity production by Saccharomyces cerevisiae during high sugar fermentation. , 2003, Journal of bioscience and bioengineering.

[21]  J. Řičica,et al.  Continuous cultivation of microorganisms , 1970, Folia Microbiologica.

[22]  A. Mendes-Ferreira,et al.  Growth and fermentation patterns of Saccharomyces cerevisiae under different ammonium concentrations and its implications in winemaking industry , 2004, Journal of applied microbiology.

[23]  G A Hill,et al.  Effects of high product and substrate inhibitions on the kinetics and biomass and product yields during ethanol batch fermentation , 1992, Biotechnology and bioengineering.

[24]  Birgit Kamm,et al.  Biorefineries – Industrial Processes and Products , 2005 .

[25]  V. Mcdonald Direct Microscopic Technique to Detect Viable Yeast Cells in Pasteurized Orange Drink , 1963 .

[26]  W. Orts,et al.  Thermoformed wheat gluten biopolymers. , 2006, Journal of agricultural and food chemistry.

[27]  Wiwut Tanthapanichakoon,et al.  Mathematical modeling to investigate temperature effect on kinetic parameters of ethanol fermentation , 2006 .

[28]  K. C. Thomas,et al.  Fuel alcohol production: effects of free amino nitrogen on fermentation of very-high-gravity wheat mashes , 1990, Applied and environmental microbiology.

[29]  Rajeshwar Dayal Tyagi,et al.  Rapid ethanol fermentation of cellulose hydrolysate. II. Product and substrate inhibition and optimization of fermentor design , 1979 .

[30]  A. Ghaly,et al.  Kinetics of batch production of ethanol from cheese whey , 1994 .

[31]  Jean-Marie Sablayrolles,et al.  Automatic detection of assimilable nitrogen deficiencies during alcoholic fermentation in oenological conditions , 1990 .

[32]  Colin Webb,et al.  Development of a process for the production of nutrient supplements for fermentations based on fungal autolysis , 2005 .

[33]  A. Koutinas,et al.  Restructuring upstream bioprocessing: technological and economical aspects for production of a generic microbial feedstock from wheat , 2004, Biotechnology and bioengineering.

[34]  S. Lie,et al.  THE EBC‐NINHYDRIN METHOD FOR DETERMINATION OF FREE ALPHA AMINO NITROGEN , 1973 .

[35]  G. A. Hill,et al.  A modified ghose model for batch cultures of Saccharomyces cerevisiae at high ethanol concentrations , 1990 .

[36]  W. M. Ingledew,et al.  Improved ethanol yields through supplementation with excess assimilable nitrogen , 1991, Journal of Industrial Microbiology.

[37]  W. M. Ingledew,et al.  Fuel alcohol production : assessment of selected commercial proteases for very high gravity wheat mash fermentation , 1994 .

[38]  J. Luong Kinetics of ethanol inhibition in alcohol fermentation , 1985, Biotechnology and bioengineering.

[39]  P. Barré,et al.  Use of constant rate alcoholic fermentations to compare the effectiveness of different nitrogen sources added during the stationary phase , 1997 .