• Energy Research

AbstractThe influence of carbohydrates: glucose, fructose, galactose, galacturonic acid, xylose, lactose, sucrose, pectin and inulin, were evaluated as sole carbon source for the production of laccases by the ascomycete, Botryosphaeria sp. Veratryl alcohol, a laccase inducer, was added to culture media to study inducible laccase production on the same carbon sources. Inulinase and pectinase were also produced when Botryosphaeria sp. was grown on inulin, and galacturonic acid and pectin, respectively, and their levels were less in the presence of veratryl alcohol. Botryosphaeria sp. produced constitutive laccases on all carbon sources examined, and veratryl alcohol increased the laccase production on most of carbon sources studied except for inulin and galacturonic acid. Evidence is presented that Botryosphaeria sp. is also pectinolytic.

Fast-growing hybrid poplar species are attractive as feedstocks for the production of bio-based chemicals including biofuels. Pretreatment makes cellulose accessible to enzymatic hydrolysis, producing hemicellulose and lignin as major co-products. Poplar woodchips pretreated hydrothermally in an experimental industrial pilot-plant generated two prehydrolyzate streams; purge-condensate collected from cooking the woodchips and press-filtrate collected after the fiber explosion step. Both prehydrolyzates contain hemicellulose sugars (pentoses, hexoses, oligosaccharides), acetic acid, and degradation products from hemicellulose and lignin (furanic and phenolic compounds, respectively). Purge prehydrolyzate was highly diluted, of low sugar content and high biochemical/chemical oxygen demand, and constituted a process waste that was addressed for value-adding through production of enzymes by fermentation. Wood-decay fungi were screened for laccases on purge prehydrolyzate, with Botryosphaeria rhodina producing highest titers. B. rhodina detoxified the prehydrolyzate but at expense of sugar consumption. Adding xylose and glycerol to purge did not inhibit fungal growth or impede laccase production. Phenolics in the purge had inducing effect on enhancing laccase titers. Laccase production was optimized by Box-Behnken-(33)-factorial design varying the concentration of xylose in the purge, together with adding copper as laccase inducer and glycerol to increase the level of fermentable substrate, resulting in optimal enzyme titers (36.37 ± 3.52U/mL; validated). The crude laccase preparation was employed to detoxify the more concentrated press prehydrolyzate, reducing the overall content of phenolics by ∼30 %. Chromatographic (high-performance liquid chromatography-ultraviolet, gas chromatography/mass spectrometry) analysis identified various phenolic compounds present in the press prehydrolyzate following laccase treatment, and in the presence of the mediator, ABTS, the phenolics content decreased further.

For a hundred years or more, oil and natural gas has supplied fuel and other raw chemicals to support economic growth. In the last decades their shrinking reservoirs and the increasing cost of production has become obvious, leading researchers to look for alternative substitutes of all the chemical materials presently derived from oil and gas. This review is focused on xylan, the second most abundant plant polysaccharide on our planet. Some xylan-derived products have already found commercial applications (ethanol, xylitol, xylo-oligosaccharides) while others could have a great future in a wide range of industries. The chemical and structural variations of xylans produced by different plants, and the concentration of xylan in various plant resources are summarized. This review discusses the latest research developments in extraction and purification methodologies, and chemical modification, as well as the analytical methods necessary for xylan related research.

Development of high-valued products through an integrated biorefinery approach is essential for the revival of the Canadian forest industry. Utilization of tree bark is one such example with considerable potential. The bark of trees contains a reservoir of phytochemicals that could be harnessed as value-added co-products. The objective of this study was to identify, characterize, and seek commercial potential of phytochemicals present in poplar bark. Industrially harvested poplar bark (Populus tremuloides) was procured from Quebec. Water-soaked poplar bark was subjected to three steam-explosion treatments (treatments 1 to 3) using a steam-explosion reactor. During the experiment, extracts such as air purge, pre-steam purge, cooked purge, and pressed liquid were collected and subjected to compositional analysis. The results showed that the leftover bark residue even after the treatments was still fit for regular combustion for generating heat. Among the several identified phytochemicals (>100), furfural, 5-HMF, benzoic acid, salicylic acid, and catechol can be obtained as bulk chemicals, and sakuranin present at 15.9 % (extracted with acetone) as a high-valued and fine chemical. Considering the increasing demand for plant-based ingredients, there exists enormous potential to utilize these phytochemicals in agro-pharmaceutical industries. Further end-use studies, however, are required to ascertain the true economic potential of poplar bark phytochemicals.

In this work, two types of biomass preparations (VMSM and M3) from the filamentous fungus Botryosphaeria rhodina MAMB-05, which were previously used in a process of production of β-glucan, were assessed as biosorbents of lead. The operating conditions, optimized through response surface methodology and experimental design, were shown to be pH 5.29 and a biosorbent dose of 0.23 g/L for the VMSM biomass type; and pH 5.06 and a dose of biosorbent of 0.60 g/L for the M3 biomass type, at a constant temperature of 27 °C. Fourier transform-infrared spectroscopy analyzed the presence of functional groups on the biomass surface. In addition to give an extra value to the by-product biomass, the VMSM-type from B. rhodina MAMB-05 showed an excellent lead biosorption capacity (qm) with a value of 403.4 mg/g for the Langmuir model, comparing favorably with literature results, while the M3 subtype biomass showed a value of 96.05 mg/g.

beta-Glucosidase production by Debaryomyces pseudopolymorphus UCLM-NS7A using a simple nutrient medium containing cellobiose was evaluated under several biochemical and physiological parameters in submerged fermentation. Enzyme induction was also examined using different carbon and nitrogen sources. Cellobiose and ammonium nitrate were the best C and N sources to enhance beta-glucosidase production. The addition of NaCl, MgSO(4), yeast extract, ethanol and Tween 80 to the nutrient medium before inoculation was also compared. A factorial design to optimize enzyme production was developed using four variables that most influenced beta-glucosidase production and data analyzed by the response surface method. Optimal conditions to produce beta-glucosidase in shake-flasks were 1.25% cellobiose, 0.05% Tween 80, 0.4% NH(4)NO(3) over 72 hours. In another factorial design to further increase enzyme production, a lab fermenter using prior-determined shake-flask optimized conditions resulted in higher beta-glucosidase titres at 72 hours, pH controlled at 6.25 and agitation of 200 rpm.

The global forestry industry after experiencing a market downturn during the past decade has now aimed its vision towards the integrated biorefinery. New business models and strategies are constantly being explored to re-invent the global wood and pulp/paper industry through sustainable resource exploitation. The goal is to produce diversified, innovative and revenue generating product lines using on-site bioresources (wood and tree residues). The most popular product lines are generally produced from wood fibers (biofuels, pulp/paper, biomaterials, and bio/chemicals). However, the bark and other tree residues like foliage that constitute forest wastes, still remain largely an underexploited resource from which extractives and phytochemicals can be harnessed as by-products (biopharmaceuticals, food additives and nutraceuticals, biopesticides, cosmetics). Commercially, Populus (poplar) tree species including hybrid varieties are cultivated as a fast growing bioenergy crop, but can also be utilized to produce bio-based chemicals. This review identifies and underlines the potential of natural products (phytochemicals) from Populus species that could lead to new business ventures in biorefineries and contribute to the bioeconomy. In brief, this review highlights the importance of by-products/co-products in forest industries, methods that can be employed to extract and purify poplar phytochemicals, the potential pharmaceutical and other uses of >160 phytochemicals identified from poplar species - their chemical structures, properties and bioactivities, the challenges and limitations of utilizing poplar phytochemicals, and potential commercial opportunities. Finally, the overall discussion and conclusion are made considering the recent biotechnological advances in phytochemical research to indicate the areas for future commercial applications from poplar tree species.

Abstract Lasiodiplodan, an exopolysaccharide of the (1→6)-β-d-glucan type, is produced by Lasiodiplodia theobromae MMPI when grown under submerged culture on glucose. The objective of this study was to evaluate lasiodiplodan production by examining the effects of carbon (glucose, fructose, maltose, sucrose) and nitrogen sources (KNO3, (NH4)2SO4, urea, yeast extract, peptone), its production in shake flasks compared to a stirred-tank bioreactor, and to study the rheology of lasiodiplodan, and lasiodiplodan’s anti-proliferative effect on breast cancer MCF-7 cells. Although glucose (2.05 ± 0.05 g L−1), maltose (2.08 ± 0.04 g L−1) and yeast extract (2.46 ± 0.06 g L−1) produced the highest amounts of lasiodiplodan, urea as N source resulted in more lasiodiplodan per unit biomass than yeast extract (0.74 ± 0.006 vs. 0.22 ± 0.008 g g−1). A comparison of the fermentative parameters of L. theobromae MMPI in shake flasks and a stirred-tank bioreactor at 120 h on glucose as carbon source showed maximum lasiodiplodan production in agitated flasks (7.01 ± 0.07 g L−1) with a specific yield of 0.25 ± 0.57 g g−1 and a volumetric productivity of 0.06 ± 0.001 g L−1 h−1. A factorial 22 statistical design developed to evaluate the effect of glucose concentration (20–60 g L−1) and impeller speed (100–200 rpm) on lasiodiplodan production in the bioreactor showed the highest production (6.32 g L−1) at 72 h. Lasiodiplodan presented pseudoplastic behaviour, and the apparent viscosity increased at 60°C in the presence of CaCl2. Anti-proliferative activity of lasiodiplodan was demonstrated in MCF-7 cells, which was time- and dose-dependent with an IC50 of 100 μg lasiodiplodan mL−1.