| 1. |
- Börjesson, Johan, et al.
(författare)
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Effect of poly(ethylene glycol) on enzymatic hydrolysis and adsorption of cellulase enzymes to pretreated lignocellulose
- 2007
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Ingår i: Enzyme and Microbial Technology. - : Elsevier BV. - 0141-0229. ; 41:1-2, s. 186-195
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Tidskriftsartikel (refereegranskat)abstract
- There is a need to develop the enzymatic hydrolysis of cellulose for production of ethanol from biomass. In recent years the inhibitory effects of lignin in lignocellulosic substrates has been the focus of several studies. This points to the importance of understanding the interactions between cellulose degrading enzymes and lignin. Surface active substances have been shown to adsorb to lignin surfaces resulting in reduction of unproductive enzyme binding. It is essential to understand the surface properties of both enzymes and lignin to develop pretreatment methods, surface active additives and engineering of cellulose degrading enzyme systems. This study investigates the PEG-lignin interaction as well as interactions between lignin and the enzyme modules of the Hypocrea jecorina (Trichoderma reesei) enzymes Cel7A and Cel7B. Interactions were monitored with C-14 labelled PEG 4000 and by measuring the enzymatic activity in solution. It was found that the dominating driving force of PEG adsorption on lignin is hydrophobic interaction. The effect of PEG addition on enzyme conversion of lignocellulose increased with higher temperature due to increased adsorption of PEG on lignin, thus resulting in a higher surface density of PEG on the surface. The hydrophobic adsorption of enzymes to lignin induces denaturation of enzymes on lignin surfaces. The addition of PEG to the enzyme hydrolysis at a temperature of 50 degrees C is suggested to hinder deactivation of enzymes by exclusion of enzymes from lignin surfaces. The adsorption of full-length Cel7B to lignin was stronger than for Cel7A. A more hydrophobic surface on the flat face of the cellulose binding module (CBM) together with an additional exposed aromatic residue on the rough face of Cel7B CBM compared to Cel7A CBM gives a higher affinity to lignin for the Cel7B enzyme. (c) 2007 Elsevier Inc. All rights reserved.
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| 2. |
- Erdei, Borbala, et al.
(författare)
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Ethanol production from mixtures of wheat straw and wheat meal
- 2010
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Ingår i: Biotechnology for Biofuels. - : Springer Science and Business Media LLC. - 1754-6834. ; 3
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Tidskriftsartikel (refereegranskat)abstract
- Background: Bioethanol can be produced from sugar-rich, starch-rich (first generation; 1G) or lignocellulosic (second generation; 2G) raw materials. Integration of 2G ethanol with 1G could facilitate the introduction of the 2G technology. The capital cost per ton of fuel produced would be diminished and better utilization of the biomass can be achieved. It would, furthermore, decrease the energy demand of 2G ethanol production and also provide both 1G and 2G plants with heat and electricity. In the current study, steam-pretreated wheat straw (SPWS) was mixed with presaccharified wheat meal (PWM) and converted to ethanol in simultaneous saccharification and fermentation (SSF). Results: Both the ethanol concentration and the ethanol yield increased with increasing amounts of PWM in mixtures with SPWS. The maximum ethanol yield (99% of the theoretical yield, based on the available C6 sugars) was obtained with a mixture of SPWS containing 2.5% water-insoluble solids (WIS) and PWM containing 2.5% WIS, resulting in an ethanol concentration of 56.5 g/L. This yield was higher than those obtained with SSF of either SPWS (68%) or PWM alone (91%). Conclusions: Mixing wheat straw with wheat meal would be beneficial for both 1G and 2G ethanol production. However, increasing the proportion of WIS as wheat straw and the possibility of consuming the xylose fraction with a pentose-fermenting yeast should be further investigated.
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| 3. |
- Kreuger, Emma, et al.
(författare)
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Bioconversion of industrial hemp to ethanol and methane: The benefits of steam pretreatment and co-production
- 2011
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Ingår i: Bioresource Technology. - : Elsevier BV. - 1873-2976 .- 0960-8524. ; 102:3, s. 3457-3465
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Tidskriftsartikel (refereegranskat)abstract
- Several scenarios for ethanol production, methane production (by anaerobic digestion) and co-production of these, using autumn harvested hemp as substrate, were investigated and compared in terms of gross energy output. Steam pretreatment improved the methane production rate compared with mechanical grinding. The methane yield of steam pretreated stems was similar both with and without pre-hydrolysis with cellulolytic enzymes. Co-production of ethanol and methane from steam pretreated stems gave a high yield of transportation fuel, 11.1-11.7 MJ/kg processed stem dry matter (DM); more than twice that of ethanol production alone from hexoses, 4.4-5.1 MJ/kg processed stem DM. Co-production from the whole hemp plant would give 2600-3000 L ethanol and 2800-2900 m(3) methane, in total 171-180 GJ per 10,000 m(2) of agricultural land, based on a biomass yield of 16 Mg DM. Of this, the yeast and enzymes from ethanol production were estimated to contribute 700 m(3) (27 GJ) of methane. (C) 2010 Elsevier Ltd. All rights reserved.
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| 4. |
- Sipos, Balint, et al.
(författare)
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Steam pretreatment of dry and ensiled industrial hemp for ethanol production
- 2010
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Ingår i: Biomass & Bioenergy. - : Elsevier BV. - 1873-2909 .- 0961-9534. ; 34:12, s. 1721-1731
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Tidskriftsartikel (refereegranskat)abstract
- Biomass can be converted into liquid and gaseous biofuels with good efficiency. In this study, the conversion of industrial hemp (Cannabis sativa L.), a biomass source that can be cultivated with a high biomass yield per hectare, was used. Steam pretreatment of dry and ensiled hemp was investigated prior to ethanol production. The pretreatment efficiency was evaluated in terms of sugar recovery and polysaccharide conversion in the enzymatic hydrolysis step. For both materials, impregnation with 2% SO2 followed by steam pretreatment at 210 degrees C for 5 min were found to be the optimal conditions leading to the highest overall yield of glucose. Simultaneous saccharification and fermentation experiments carried out with optimised pretreatment conditions resulted in ethanol yields of 163 g kg(-1) ensiled hemp (dry matter) (71% of the theoretical maximum) and 171 g kg(-1) dry hemp (74%), which corresponds to 206-216 l Mg-1 ethanol based on initial dry material. (C) 2010 Elsevier Ltd. All rights reserved.
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