Rapid depletion of fossil fuel stock with a simultaneous rise in greenhouse gas emissions has led to an increase in the need for alternative energy. Cellulose based biofuels, especially bioethanol is a form of alternative energy that has the potential to replace petrol. The first step in cellulosic bioethanol production is the release of fermentable sugars via pre-treatment. Conventionally, physico-chemical and biological pre-treatment methods are energy intensive, environmentally unfavourable and expensive. This study, however reports on the use of a less energy consuming, cheap and environmental friendly alternative; photocatalysis, to produce fermentable sugars from cellulose. To achieve this, a range of photocatalysts were first screened based on their OH radical production rates using coumarin as a probe. TiO2 P25 was the photocatalyst that was found to have the highest OH radical production rate of 35.6 μM/hr, followed by Pt-C3N4 (0.88 μM/hr) and WO3 (0.28 μM/hr). LaCr-SrTiO3, Cr-SrTiO3 and yellow TiO2 did not produce any OH radicals due to their unsuitable electronic structure. P25 was further used for photocatalytic fermentable sugar production from cellulose. Photocatalytic cellulose I breakdown produced 0.04 % fermentable sugars whereas, with cellulose II feedstock the yield increased to 0.2 %. To further improve the yield, membrane bags were deployed which improved the sugar yields to 0.43 % and 0.71 % respectively from cellulose and cellulose II feedstocks. Photonic efficiencies followed the same trends as the sugar yields. Engineering design was further opted to enhance the sugar yields and hence a stacked frame photocatalytic reactor (SFPR) was designed. Various mixer configurations were designed and their mixing regime was determined using COMSOL Multiphysics 5.1 simulations. Amongst the mixers simulated, an 8-blade Rushton impeller was found to be the best configuration due its superior radial mixing profile and higher fluid velocity. The SFPR was then fabricated and operated with the impeller or a plus shaped magnetic bar as the mixer and the sugar yields were determined. Highest sugar yield and photonic efficiency was obtained from the cellulose II-impeller setup and was calculated to be 2.61 % and 9.45 % respectively. Respective lowest yields were obtained with cellulose I-stirrer bar setup and calculated to be 1.71 % and 5.64 %. Furthermore, the effect of H2O2 on fermentable sugar production was also tested. The cellulose II-stirrer bar configuration yielded 3.15 % fermentable sugars with the addition of 0.01 wt% H2O2 to the reaction mixture. The yield improved significantly to 14.1 % when the concentration of H2O2 was increased to 0.1 wt%.

This thesis project studied microcrystalline cellulose II (CII), a polymorphic form of cellulose, which has lower mechanical properties, less plastic deformation, higher elastic recovery and faster disintegration properties than microcrystalline cellulose I (CI). Also, the effects of processing and silicification on CII materials were investigated. Particle modification through spray drying, wet granulation and spheronization was employed to improve CII performance. Spray-drying (SDCII) and wet granulation (WGCII) produced materials with no difference in mechanical or disintegration properties from unprocessed CII, but did show an increase in density and particle flow. Conversely, spheronization (SPCII) showed the poorest mechanical properties compared to CII. Further, SDCII showed better dilution potential than CII. Thus the advantages of SDCII were apparent when it was mixed with a poorly compressible drug (acetaminophen) because fibrous CII was converted to spheroidal particles through spray drying. The rapid disintegration of SDCII and CII compacts was due to water wicking through capillaries followed by compact bursting. Compacts of ibuprofen mixed with SDCII and Avicel® PH-102 had comparable disintegration rates and release profiles compared to ibuprofen formulated with commercial disintegrants and Avicel® PH-102, especially at levels 10% w/w. Adding fumed silica into CII particles through spray drying, wet granulation (WGCII) and spheronization (SPCII) at 2-20% w/w was also studied. Silicification increased physical properties such as true density, Hausner ratio, porosity, ejection force and specific surface area of SDCII and WGCII. Other properties such as bulk and tap densities were reduced due to the amorphous and light character of fumed silica. Spheronized CII showed no change in these properties with silicification. Silicification diminished lubricant sensitivity with magnesium stearate due to the competition of SiO2 with magnesium stearate to coat CII particles. Silicification also decreased the affinity of CII for water only at the 20% w/w level due to the few silanol groups available for water interaction compared to surface hydroxyl groups on CII alone. Particle size modification of CII was process-dependent rather than silicification-dependent. Additionally, silicification decreased the apparent plasticity and elastic recovery of SDCII and WGCII when compacted. The former effect along with increased powder porosity increased surface area and compressibility of SDCII and WGCII. Compact tensile strength of silicified CII materials was in the order: spray-dried > wet granulated > spheronized. This order was due to the combined effect of particle morphology and how fumed silica was incorporated and distributed within CII particles. Silicification did not affect the rapid disintegration properties of CII. Thus, diphenhydramine HCl and griseofulvin tablets prepared with silicified CII had faster disintegration and release than those prepared with commercial silicified CI (Prosolv®). Moreover, CII beads containing diphenhydramine HCl or griseofulvin had faster release profiles compared to beads prepared with Prosolv® SMCC 50 or Avicel® PH-101. This behavior showed that rapid disintegration is an intrinsic property of CII. Compact tensile strength decreased more for unsilicified CI and CII compacts stored at 75% RH, while silicified CI and CII compacts lost less tensile strength under the same conditions. Reprocessed CI materials containing acetaminophen (1:1mixtures) lost 35-72% of their original strength compared to silicified CII materials (15-25% loss) indicating more particle interaction upon recompression. .

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This thesis deals with the preparation of chemically and/or enzymatically modified cellulose. This modification can be either irreversible or reversible. Irreversible modification is used to prepare cellulose derivatives as end products, whereas reversible modification is used to enhance solubility in the preparation of regenerated cellulose. The irreversible modification studied here was the preparation of carboxymethyl cellulose (CMC) using extended mercerization of a spruce dissolving pulp. More specifically the parameters studied were the effect of mercerization at different proportions of cellulose I and II in the dissolving pulp, the concentration of alkali, the temperature and the reaction time. The parameters evaluated were the degree of substitution, the filterability and the amount of gel obtained when the resulting CMC was dissolved in water. Molecular structures of CMC and its gel fractions were analysed by using NIR FT Raman spectroscopy. It was found that the alkali concentration in the mercerization stage had an extensive influence on the subsequent etherification reaction. FT Raman spectra of CMC samples and their gel fractions prepared with low NaOH concentrations (9%) in the mercerization stage indicated an incomplete transformation of cellulose to Na-cellulose before carboxymethylation to CMC. Low average DS values of the CMC, i.e. between 0.42 and 0.50 were obtained. Such CMC dissolved in water resulted in very thick and semi solid gum-like gels, probably due to an uneven distribution of substituents along the cellulose backbone. FT Raman spectra of CMC samples and their gel fractions mercerized at higher alkaline concentration, i.e. 18.25 and 27.5% in the mercerization stage, indicated on the other hand a complete transformation of cellulose to Na-cellulose before carboxymethylation to CMC. Higher average DS values of the CMC, i.e. between 0.88 and 1.05 were therefore obtained. When dissolved in water such CMC caused gel formation especially when prepared from dissolving pulp with a high fraction of cellulose II. The reversible modification studied was the dissolution of cellulose in NaOH/ZnO. Here the effect of enzyme pretreatment was investigated by using two mono-component enzymes; namely xylanase and endoglucanase, used in consecutive stages. It was found that although the crystallinity and the specific surface area of the dissolving pulp sustained minimal change during the enzymatic treatment; the solubility of pulp increased in a NaOH/ZnO solution from 29% for untreated pulp up to 81% for enzymatic pretreated pulp. / Baksidetext Cellulose can be chemically and/or enzymatically modified. Irreversible modification is used to prepare cellulose derivatives as end products, reversible modification to enhance solubility in the preparation of regenerated cellulose. The irreversible modification studied here was the preparation of carboxymethyl cellulose (CMC) using extended mercerization of a spruce dissolving pulp. More specifically the parameters studied were the effect of mercerization at different proportions of cellulose I and II in the dissolving pulp, the concentration of alkali, the temperature and the reaction time. It was found that the alkali concentration in the mercerization stage had an extensive influence on the subsequent etherification reaction. The content of cellulose II had little effect on degree of substitution (DS) at low NaOH concentration, but tended to decrease DS at higher NaOH concentration in both cases compared with cellulose I. It was also found that the content of cellulose II correlates with the gel formation obtained when the CMC is dissolved in water. The reversible modification studied was the dissolution of cellulose in NaOH/ZnO. Here the effect of enzyme pretreatment was investigated by using two mono-component enzymes; namely xylanase and endoglucanase, used in consecutive stages. It was found that the solubility of pulp increased in a NaOH/ZnO solution from 29% for untreated pulp up to 81% for enzymatic pretreated pulp.