Traditionally, bio-butanol is produced with the ABE (Acetone Butanol Ethanol) process using Clostridium species to ferment sugars from biomass. However, the route is associated with some disadvantages such as low butanol yield and by-product formation (acetone and ethanol). On the other hand, butanol can be directly produced from ethanol through aldol condensation over metal oxides/ hydroxyapatite catalysts. This paper suggests that the chemical conversion route is more preferable than the ABE process, because the reaction proceeds more quickly compared to the fermentation route and fewer steps are required to get to the product.

No abstract

No abstract

Sweet sorghum is a hardy crop that can be grown on marginal land and can provide both food and energy in an integrated food and energy system. Lignocellulose rich sweet sorghum bagasse (solid left over after starch and juice extraction) can be converted to bioethanol using a variety of technologies. The largest barrier to commercial production of fuel ethanol from lignocellulosic material remains the high processing costs associated with enzymatic hydrolysis and the use of acids and bases in the pretreatment step. In this paper, sweet sorghum bagasse was pretreated and hydrolysed in a single step using microwave irradiation. A conversion efficiency of 96% (0.82 g sugar/g bagasse) was obtained in a 5wt% sulphuric acid solution under 20 minutes of 180W microwave irradiation. An ethanol conversion efficiency of 98% (0.5 g ethanol/g sugar) was obtained after 24 hours of fermentation using a mixed culture of organisms to convert both hexose and pentose sugar in the broth. These results show the potential of producing 13 000 L/ha which is high enough to make the process economically attractive.

No abstract

In this work, crude glycerol liquefaction of lignins produced in the pulp and paper industry, as well as an organosolv lignin (sugarcane bagasse), was studied with the ultimate aim of preparing bio-based polyols for polyurethane (PU) preparation. This is a proposed strategy to valorise the by-products of biodiesel and lignocellulose biorefineries. Size-exclusion chromatography revealed that the lignins behave differently during liquefaction based on a ranging product molecular weight (MW). The MW of the liquefaction products was concluded to be related to the phenolic and aliphatic hydroxyl group content of the respective lignins, as well as the removal of glycerol and monoacylglycerol during liquefaction. Lignin was modified to yield mostly a solid-phase product. Fourier transform infrared spectroscopy suggests that crude glycerol constituents like glycerol and fatty acid esters are bound to lignin during liquefaction through formation of ether and ester bonds. Liquefaction yield further also varied with lignin type. The liquefaction products were effectively employed as bio-based polyols to prepare PU.

Spent coffee ground (SCG), a present waste stream from instant coffee production, represents a potential feedstock for mannooligosaccharides (MOS) production. MOS can be used in nutraceutical products for humans/animals or added to instant coffee, increasing process yield and improving product health properties. The SCG was evaluated for MOS production by steam pretreatment and enzymatic hydrolysis with a recombinant mannanase and a commercial cellulase cocktail (Acremonium, Bioshigen Co. Ltd, Japan). The mannanase was produced using a recombinant strain of Yarrowia lipolytica, used to produce and secrete endo-1,4-β,D-mannanase from Aspergillus aculeatus in bioreactor cultures. Endo-1,4-β,D-mannanase was produced with an activity of 183.5 U/mL and 0.23 mg protein/mL. The enzyme had an optimum temperature of 80 °C, and the activity in the supernatant was improved by 150 % by supplementation with 0.2 % sodium benzoate and 35 % sorbitol as a preservative and stabiliser, respectively. The steam pretreatment of SCG improved the enzymatic digestibility of SCG, thus reducing the required enzyme dosage for MOS release. Combined enzymatic hydrolysis of untreated or steam-pretreated (150, 190 and 200 °C for 10 min) SCG with mannanase and cellulase cocktail resulted in 36-57 % (based on mannan content) of MOS production with a degree of polymerization of up to 6. The untreated material required at least 1 % of both mannanase and cellulase loading. The optimum mannanase and cellulase loadings for pretreated SCG hydrolysis were between 0.3 and 1 and 0.4 and 0.8 %, respectively. Statistical analysis suggested additive effect between cellulase cocktail and mannanase on MOS release, with no indication of synergism observed.

No abstract