Title of article :
Propagated fixed-bed mixed-acid fermentation: Effect of volatile solid loading rate and agitation at near-neutral pH
Author/Authors :
Golub، نويسنده , , Kristina W. and Golub، نويسنده , , Stacey R. and Meysing، نويسنده , , Daniel M. and Holtzapple، نويسنده , , Mark T.، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2012
Pages :
11
From page :
146
To page :
156
Abstract :
To increase conversion and product concentration, mixed-acid fermentation can use a countercurrent strategy where solids and liquids pass in opposite directions through a series of fermentors. To limit the requirement for moving solids, this study employed a propagated fixed-bed fermentation, where solids were stationary and only liquid was transferred. To evaluate the role of agitation, continuous mixing was compared with periodic mixing. The periodically mixed fermentation had similar conversion, but lower yield and selectivity. Increasing volatile solid loading rate from 1.5 to 5.1 g non-acid volatile solids/(Lliq·d) and increasing liquid retention time decreased yield, conversion, selectivity, but increased product concentrations. Compared to a previous study at high pH (∼9), this study achieved higher performance at near neutral pH (∼6.5) and optimal C–N ratios. Compared to countercurrent fermentation, propagated fixed-bed fermentations have similar selectivities and produce similar proportions of acetic acid, but have lower yields, conversion, productivities, and acid concentrations.
Keywords :
Mixed-acid fermentation , Carboxylate platform , biofuels , Submerged bed , Propagated fixed-bed fermentation
Journal title :
Bioresource Technology
Serial Year :
2012
Journal title :
Bioresource Technology
Record number :
1930311
Link To Document :
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