Optimal Pretreatment of Eucalyptus globulus by Hydrothermolysis and Alkaline Extraction for Microbial Production of Ethanol and Xylitol

Fractionation of Eucalyptus globulus wood chips is mandatory for developing a biorefinery process. In order to achieve this, products released from hydrothermolysis pretreatment were studied within the severity (log R 0) range 3.3–4.5. The highest solubilized xylose yield was 56% (DWB) at log R 0 3....

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Veröffentlicht in:Industrial & engineering chemistry research 2013-04, Vol.52 (16), p.5713-5720
Hauptverfasser: Castro, Jean F, Parra, Carolina, Yáñez-S, Mauricio, Rojas, Jonathan, Teixeira Mendonça, Regis, Baeza, Jaime, Freer, Juanita
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Sprache:eng
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Zusammenfassung:Fractionation of Eucalyptus globulus wood chips is mandatory for developing a biorefinery process. In order to achieve this, products released from hydrothermolysis pretreatment were studied within the severity (log R 0) range 3.3–4.5. The highest solubilized xylose yield was 56% (DWB) at log R 0 3.9. Values higher than log R 0 4.1 have led to high xylose dehydration rates. Detoxification steps applied to the liquor removed acetic acid (55%), furfural (94%), and hydroxymethylfurfural (HMF) (31%). Fermentation of liquor with Candida guilliermondii resulted in a xylitol yield of 0.37 g of xylitol produced per gram of xylose consumed (equivalent to 71% of the control with pure xylose). Pulp-1 (from hydrothermolysis pretreatment) was further pretreated with NaOH for lignin removal (obtaining Pulp-2). Cellulose composition in Pulp-1 and Pulp-2 remains almost unaltered; lignin content in Pulp-2 was 50% lower than in Pulp-1. Simultaneous saccharification and fermentation (SSF) experiments for both pulps reached similar ethanol yields of 0.76 and 0.70 g of ethanol produced per gram of ethanol potentially produced from wood, respectively. Recovery of hemicellulose at the beginning of the process is a key step for getting pulps with high cellulose composition available for developing a biorefinery process of E. globulus.
ISSN:0888-5885
1520-5045
DOI:10.1021/ie301859x