Optimisation of a continuous flash fermentation for butanol production using the response surface methodology
Contribuinte(s) |
Universidade Estadual Paulista (UNESP) |
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Data(s) |
30/09/2013
20/05/2014
30/09/2013
20/05/2014
01/05/2010
|
Resumo |
Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP) Processo FAPESP: 07/00341-1 Processo FAPESP: 06/55177-9 Factorial design and response surface techniques were used in combination with mathematical modelling and computational simulation to optimise an innovative industrial bioprocess, the production of biobutanol employing the flash fermentation technology. A parametric analysis performed by means of a full factorial design at two levels determined the influence of operating variables on butanol yield and productivity. A second set of simulations were carried out based on the central composite rotatable design. This procedure generated simplified statistical models that describe butanol yield and productivity as functions of the significant operating variables. From these models, response surfaces were obtained and used to optimise the process. For a range of substrate concentration from 130 to 180 g/l, the optimum operating ranges ensure butanol productivity between 7.0 and 8.0 g/l h, butanol yield between 19 and 22%, substrate conversion above 90% and final butanol concentration around 25 g/l. (C) 2009 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved. |
Formato |
562-571 |
Identificador |
http://dx.doi.org/10.1016/j.cherd.2009.11.002 Chemical Engineering Research & Design. Rugby: Inst Chemical Engineers, v. 88, n. 5-6A, p. 562-571, 2010. 0263-8762 http://hdl.handle.net/11449/20136 10.1016/j.cherd.2009.11.002 WOS:000279361900005 |
Idioma(s) |
eng |
Publicador |
Inst Chemical Engineers |
Relação |
Chemical Engineering Research & Design |
Direitos |
closedAccess |
Palavras-Chave | #Flash fermentation #Biobutanol #Mathematical modelling #Optimisation #Response surfaces |
Tipo |
info:eu-repo/semantics/article |