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Subject: search.filters.subject.Pulping

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    Effect of mechanical and chemical pulping on ionic liquid fractionation of wood chips
    (2019) Hlongwa, Nhlanhla; Deenadayalu, Nirmala; Sithole, Bruce; Andrew, Jerome Edward
    In this study, a comparison of two pulping methods namely mechanical and chemical, on the dissolution of Eucalyptus grandis (E. grandis) wood chips was undertaken. The wood chip pulp was treated with an ionic liquid (IL): 1-allyl-3-methylimidazolium chloride to extract the cellulose. The IL was mixed with unbleached mechanical pulp (UBMP), bleached mechanical pulp (BMP), unbleached kraft pulp (UBKP) and bleached kraft pulp (BKP) in ratios of 10%, 20%, 30%. Each solution contained IL, wood pulp and 2-mL of 16 v/v % of dimethyl sulfoxide (DMSO). The 30 % IL pretreatment was the most effective IL pretreatment. The cellulose yield at 30 % IL pretreatment for UBMP, BMP, UBKP and BKP was 65.12%, 63.82%, 67.43%, 67.15%, respectively. This indicated that the kraft pulping method was more effective than the mechanical pulping method for the yield of cellulose after the IL pretreatment. The Crl value at 30 % IL pretreatment was highest for UBMP (72.03%) indicating that the pretreatment used was the least effective in reducing the cellulose crystallinity. The fractions of E. grandis wood chip namely, lignin, regenerated cellulose and hemicelluloses before and after the IL pretreatment, were characterized by a variety of analytical techniques such as High-Performance Liquid Chromatography (HPLC) (carbohydrates), Fourier Transform Infra-Red Attenuated Total Reflection (FTIR-ATR) (functional groups), Pyrolysis-Gas Chromatography /Mass Spectroscopy (Py-GC/MS) (lignin fractions), Ultraviolet/Visible spectroscopy (UV/Vis) (acid soluble lignin), Thermo Gravimetric Analysis (TGA) (degradation of pulp), X-Ray Diffraction (XRD) (crystallinity) and high resolution Scanning Electron Microscopy (SEM) (morphology). Kraft pulping was the most effective method for the yield of cellulose after the [AMIM][Cl]/DMSO pretreatment. The 30% [AMIM][Cl]/DMSO pretreatment gave the highest S/G ratio indicating that minimal bleaching was required.
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    Evaluation of the bleach-enhancing effects of xylanases on bagasse-soda pupil
    (2002) Bissoon, Sadhvir; Singh, Suren
    The extent of diffusion and surface modification of a purified 23.6 kDa xylanase isolated from Thermomyces lanuginosus on bagasse pulp was evaluated. Polyclonal anti-xylanase antibodies were raised in two rabbits and in conjunction with immunogold labeling and microscopic studies enzyme diffusion and degradation studies were performed. The purity of the xylanase was confirmed by SDS-PAGE and western blots confirmed the antigen-antibody hybrid on the nitrocellulose membrane.
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    Purification, application and immunolocalization of thermostable xylanases
    (2014) Govender, Stephanie; Singh, Suren; Permaul, Kugen; Pillai, Santhosh Kumar Kuttan
    Microbial enzymes are gaining worldwide attention due to their potential industrial applications. Microorganisms producing thermostable -xylanase and their associated hemicellulases have significant application in the paper and pulp, food, animal feed, and textile industries. The potential of partially purified xylanase from Thermomyces lanuginosus MC 134, Luminase PB 100, Luminase PB 200 (a commercial xylanase) and T. lanuginosus DSM 5826 (Sigma Aldrich) was evaluated in bleaching of bagasse pulp. The temperature and pH optima for all the enzymes were 60°C and pH 6, respectively. The temperature (50- 80°C) and pH (5-8) stability of the enzymes were also assessed. All the enzymes were relatively stable at 60°C and pH 6 for 180 min. T. lanuginosus MC 134 retained 80% of its activity at 60°C and pH 6 for 180 min and PB 200 retained 75% of its activity at 80°C for 180 min. T. lanuginosus MC 134 also exhibited good alkaline stability at pH 8. The commercial xylanases Luminase PB 100, Luminase PB 200, T. lanuginosus DSM 5826 (Sigma Aldrich) were purified to homogeneity using a gel filtration column packed with sephadex G-100 and characterized for Km and Vmax. However extracellular crude xylanases from T. lanuginosus MC 134 was purified to homogeneity using (N )2S04 precipitation and gel filtration column, packed with sephadex G-100. The purified xylanases exhibited a molecular mass of- 26 to 24 kDa, given range as determined by SDS page. The Km and Vmax values of Luminase PB 100, Luminase PB 200, T. lanuginosus MC 134, and T. lanuginosus DSM 5826, xylanases were determined by the Michaelis-Menten equation using birchwood xylan as the substrate. The Km value for Luminase PB 100, Luminase PB 200, T. lanuginosus DSM 5826 and T. lanuginosus MC 134 were, 8.1 mg/mL, 11.7 mg/mL and 14.3 mg/mL respectively. The Vmax for Luminase PB 100, Luminase PB 200, T lanuginosus DSM 5826 and T lanuginosus MC 134 were 232.6, 454.6 and 74.6 !Jl11ol/min/mg. Biobleaching conditions of the xylanases were also optimised and the release of reducing sugars and lignin derived compounds showed that an enzyme dosage of 50U/g of pulp was ideal for biobleaching at pH 6 and 60°C for 180 min. This brightness for T lanuginosus MC 134, Luminase PB 200, Luminase PB 100 was 45.5 ± 0.11%, 44.1 ± 0.007% and 42.7 ± 0.03% respectively at pH 6, compared to untreated samples. Reducing sugars and UV-absorbing lignin-derived compound values were considerably higher in xylanase-treated samples. All the enzymes analysed exhibited similar trends in the release of lignin derived compounds and reducing sugars which indicated their potential in the pulp and paper industry.