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Effect of reduction in yeast and enzyme concentrations in a simultaneous- saccharification-and-fermentation-based bioethanol process: technical and economic evaluation.

https://arctichealth.org/en/permalink/ahliterature9212
Source
Appl Biochem Biotechnol. 2005;121-124:485-99
Publication Type
Article
Date
2005
Author
Anders Wingren
Mats Galbe
Christian Roslander
Andreas Rudolf
Guido Zacchi
Author Affiliation
Department of Chemical Engineering, Lund University, PO Box 124, SE-221 00 Lund, Sweden.
Source
Appl Biochem Biotechnol. 2005;121-124:485-99
Date
2005
Language
English
Publication Type
Article
Keywords
Bioreactors - economics - microbiology
Cell Culture Techniques - economics - methods
Cellulase - chemistry - economics - metabolism
Comparative Study
Computer simulation
Cost-Benefit Analysis
Ethanol - chemistry - economics - metabolism
Models, Biological
Models, Econometric
Research Support, Non-U.S. Gov't
Saccharomyces cerevisiae - metabolism
Sweden
beta-Glucosidase - economics - metabolism
Abstract
The ethanol production cost in a simultaneous saccharification and fermentation-based bioethanol process is influenced by the requirements for yeast production and for enzymes. The main objective of this study was to evaluate--technically and economically--the influence of these two factors on the production cost. A base case with 5 g/L of baker's yeast and an initial concentration of water-insoluble solids of 5% resulted in an experimental yield of 85%. When these data were implemented in Aspen Plus, yeast was assumed to be produced from sugars in the hydrolysate, reducing the overall ethanol yield to 69%. The ethanol production cost was 4.80 SEK/L (2.34 US$/gal). When adapted yeast was used at 2 g/L, an experimental yield of 74% was achieved and the estimated ethanol production cost was the same as in the base case. A 50% reduction in enzyme addition resulted in an increased production cost, to 5.06 SEK/L (2.47 US$/gal) owing to reduced ethanol yield.
PubMed ID
15920258 View in PubMed
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Process considerations and economic evaluation of two-step steam pretreatment for production of fuel ethanol from softwood.

https://arctichealth.org/en/permalink/ahliterature9373
Source
Biotechnol Prog. 2004 Sep-Oct;20(5):1421-9
Publication Type
Article
Author
Anders Wingren
Johanna Söderström
Mats Galbe
Guido Zacchi
Author Affiliation
Department of Chemical Engineering, Lund University, P.O. Box 124, SE-221 00 Lund, Sweden.
Source
Biotechnol Prog. 2004 Sep-Oct;20(5):1421-9
Language
English
Publication Type
Article
Keywords
Bioreactors - economics - microbiology
Computer simulation
Conservation of Energy Resources - economics - methods
Cost-Benefit Analysis - methods
Ethanol - chemistry - economics - metabolism
Industrial Microbiology - economics - methods
Models, Biological
Models, Econometric
Research Support, Non-U.S. Gov't
Saccharomyces cerevisiae - metabolism
Steam
Sweden
Technology Assessment, Biomedical - methods
Wood
Abstract
To increase the overall ethanol yield from softwood, the steam pretreatment stage can be carried out in two steps. The two-step pretreatment process was evaluated from a techno-economic standpoint and compared with the one-step pretreatment process. The production plants considered were designed to utilize spruce as raw material and have a capacity of 200,000 tons/year. The two-step process resulted in a higher ethanol yield and a lower requirement for enzymes. However, the two-step process is more capital-intensive and has a higher energy requirement. The estimated ethanol production cost was the same, 4.13 SEK/L (55.1 cent /L) for both alternatives. For the two-step process different energy-saving options were considered, such as a higher concentration of water-insoluble solids in the filter cake before the second step, and the possibility of excluding the pressure reduction between the steps. The most optimistic configuration, with 50% water-insoluble solids in the filter cake in the feed to the second pretreatment step, no pressure reduction between the pretreatment steps, and 77% overall ethanol yield (0.25 kg EtOH/kg dry wood), resulted in a production cost of 3.90 SEK/L (52.0 cent /L). This shows the potential for the two-step pretreatment process, which, however, remains to be verified in pilot trials.
PubMed ID
15458326 View in PubMed
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