Thesis(M.S.)--Auburn University, 2005. / Abstract. Vita. Includes bibliographic references (p.97-102).

Mémoire (M.Eng.)--Université du Québec à Chicoutimi, 1995. / Document électronique également accessible en format PDF. CaQCU

Thesis (doctoral)--Wageningen Universiteit, 2008. / Summary in Dutch: p. 245. "Propositions" ([1] leaf) inserted. Includes vita (p. 149-151). Includes bibliographical references.

Thesis (M.S.)--Simon Fraser University, 1998. / Includes bibliographical references (leaves 141-149).

Thesis (M. S.)--Chemical and Biomolecular Engineering, Georgia Institute of Technology, 2007. / Koros, William, Committee Member ; Hsieh, Jeffery, Committee Chair ; Deng, Yulin, Committee Member.

Thesis (M.A.)--Ohio University, November, 2003. / Title from PDF t.p. Includes bibliographical references (leaves 181-210)

Thesis (MSc)--Stellenbosch University, 2015. / ENGLISH ABSTRACT: Lignocellulosic material is composed of three major macromolecule components i.e., cellulose, hemicelluloses and lignin. These components are chemically associated and directly linked to each other through covalent bonding which is scientifically denoted as lignin-carbohydrate complexes (LCCs) and their interaction is fundamentally important as to understand wood formation and reactivity during chemical and biological processing e.g. pulping and enzymatic hydrolysis. The association of lignin with polysaccharides (covalent linkages) has been surrounded by contradictions and controversy in several wood chemistry studies. These linkages exist in lignocellulosic materials from wood to herbaceous plants. In woody plants, they consist of ester and ether linkages through sugar hydroxyl to α-carbonyl of phenyl-propane unit on lignin. However, in herbaceous plants ferulic and p-coumaric acids are esterified to hemicelluloses and lignin respectively. In recent studies, the existence of the bonds has been shown by applying indirect analysis strategies which resulted to low yields and contaminations. The general aim of the current study was to isolate and fractionate LCCs from raw lignocellulosic materials (E. grandis and sugarcane bagasse) and corresponding processed materials (chemical pulps and water-insoluble residues (WIS)) in order to determine the chemical structure of the residual lignin associated with polysaccharides and how they affected industrial processing. The objective of the study is to compile a document that when the development of pulping and bio-ethanol bio-refinery will greatly depends on the detailed wood chemistry on how the components interact with each before and after hemicelluloses pre-extraction prior to pulping and steam explosion pre-treatment prior to enzymatic hydrolysis. The current study was focusing on understanding the effect LCCs isolated from two different industrial processing methods, i.e. pulping and enzymatic hydrolysis (EH). There were two lignocelluloses feedstocks used for pulping, i.e. Eucalyptus grandis and sugarcane bagasse whereas sugarcane bagasse was the only feedstock used for enzymatic hydrolysis. Hemicelluloses pre-extracted (mild alkali or dilute acid and autohydrolysis for sugarcane bagasse) pulps of Kraft or soda AQ from E. grandis and sugarcane bagasse were used to understand the effect of xylan pre-extraction prior to pulping on lignin-carbohydrate complexes has not been reported to the best knowledge of the primary author. Also prior to EH the material was subjected to two different treatment methods, i.e. steam explosion and ionic liquid fractionation in varying conditions. The study illustrated the types of extracted and fractionated LCCs from hemicelluloses pre-extracted pulps and WIS in comparison to the non-extracted pulps and reports from the literature. Lignin-carbohydrate complexes (LCCs) were isolated and fractionated by an inorganic method which yielded reasonable quantification quantities and no contamination and low yields for the hardwood compared to reports of using an enzymatic method. To the best knowledge of the authors, no work has been done on WIS material. The lignocelluloses were subjected to ball milling which was followed by a sequence of inorganic solvents swelling and dissolution into 2 fractions i.e. glucan-lignin and xylan-lignin-glucan. Characterisation of the isolated LCCs was made using a variety of analytical tools such as FTIR-PCA, HPLC, GPC and GC-MS. LCCs were evident when FTIR and HPLC studies were conducted. Residual lignin isolated from the lignocelluloses was assumed to be chemically bonded to carbohydrates and mostly to xylan. Approximately 60% and 30% of the lignin was linked to xylan while for the second and first fractions respectively. It is reported that lignin associated with xylan is more resistant and reduce the delignification process than when linked to glucan that is easily hydrolysable. With the FTIR and GPC analyses of LCC fractions, it was evident that the ester bonds of LCCs were destroyed through pre-extraction and pre-treatment, where this resulted to more cellulose being more accessible to alkaline pulping and enzymatic hydrolysis respectively. The linkages were either partially broken down or completely destroyed leading to significant changes of chemical structures. The polydispersity of the LCCs assisted in determining the structure of lignin, either existing as monolignols on the surfaces of fibres or a as complex two or three-dimensional structure that is linked to carbohydrates as the Mw increased or decreased. In general, these findings may have an important implication for the overall efficiency on bio-refinery. The molecular weights (Mw) of the extracted LCCs were measured by gel permeation chromatography. From the chromatograms, it was observed that the materials that were subjected to pre-processing prior to further processing, the Mw shifted to lower Mws regions. It was found that LCCs isolated from mild alkali pre-extracted pulps had high lignin syringyl to guaiacyl lignin contents than LCCs isolated from dilute acid pre-extracted pulps. High syringyl/guaiacyl ratio (S/G ratio) was an indication of low lignin content as a result of processing which will result to high product yields after downstream processing. The 5 average S/G ratio for the pulps from E. grandis and sugarcane bagasse was ranging between 1.1 to 19.01 and 1.4 to 18.16 respectively, while for the WIS-material generated from ionic liquid fractionated and steam exploded materials ranged from 3.29 to 9.27 and 3.5 to 13.3 respectively. The S/G ratios of the LCCs extracted from E. grandis and sugarcane bagasse pulps ranged from 0.42 to 2.39 and 0.041 to 0.31 was respectively while for the LCCs extracted from water-insoluble-solids (WIS) material generated from steam exploded material was from 4.87 to 10.40. The determination of S/G ratio is recommended for the LCC extraction and characterisation study as an evaluation of residual lignin in processed materials such as pulps and WIS. The obtained saccharifications were low, possibly due to the severity of the steam explosion pre-treatment and ionic liquid fractionation conditions which resulted on high accumulation of acetic acid and increased in cellulose crystallinity respectively. From quantitative analysis of the LCCs perspective it could be concluded that free lignin was present in mild alkali pre-extracted pulps than for the dilute acid pre-extracted pulps. / AFRIKAANSE OPSOMMING: Cellulose materiaal is saamgestel uit drie groot makromolekule komponente naamlik, sellulose, hemisellulose en lignien. Hierdie komponente is chemies verwante en direk met mekaar verbind deur kovalente binding wat wetenskaplik aangedui as lignien-koolhidraat komplekse (LCCs) en hul interaksie is fundamenteel belangrik as hout vorming en reaktiwiteit tydens chemiese en biologiese verwerking bv om te verstaan verpulping en ensiematiese hidrolise. Die vereniging van lignien met polisakkariede (kovalente verbindings) is omring deur teenstrydighede en omstredenheid in verskeie hout chemie studies. Hierdie skakeling bestaan in cellulose materiaal uit hout te kruidagtige plante. In houtagtige plante, hulle bestaan uit ester en eter bindings deur suiker hidroksiel te α-karboniel van feniel-propaan eenheid op lignien. Maar in kruidagtige plante ferulic en p-coumaric sure veresterd te hemisellulose en lignien onderskeidelik. In onlangse studies, het die bestaan van die bande is getoon deur die toepassing van indirekte analise strategieë wat gelei tot lae opbrengste en kontaminasie. Die algemene doel van die huidige studie was om te isoleer en fraksioneer LCCs van rou cellulose materiaal (E. grandis en suikerriet bagasse) en die ooreenstemmende verwerkte materiaal (chemiese pulp en water-oplosbare residue (WIS)) ten einde die chemiese struktuur van die te bepaal oorblywende lignien wat verband hou met polisakkariede en hoe hulle geaffekteerde industriële verwerking. Die doel van die studie is 'n dokument op te stel dat wanneer die ontwikkeling van verpulping en bio-etanol bio-raffinadery sal grootliks afhang van die gedetailleerde hout chemie oor hoe om die komponente met mekaar voor en na hemisellulose pre-onttrekking voor verpulping en stoom ontploffing pre-behandeling voor ensiematiese hidrolise. Die huidige studie was die fokus op die begrip van die effek LCCs geïsoleerd van twee verskillende industriële verwerking, maw verpulping en ensiematiese hidrolise (EH). Daar was twee lignocelluloses voerstowwe gebruik vir verpulping, dws Eucalyptus grandis en suikerriet bagasse terwyl suikerriet bagasse was die enigste grondstof gebruik vir ensiematiese hidrolise. Hemisellulose pre-onttrek (ligte alkali of verdunde suur en autohydrolysis vir suikerriet bagasse) pulp van Kraft of soda AQ van E. grandis en suikerriet bagasse is gebruik om die effek van Xylan pre-onttrekking te voor verstaan verpulping op lignien-koolhidraat komplekse het nie aan die berig is beste kennis van die primêre outeur. Ook voor EH die materiaal is onderworpe aan twee verskillende behandeling metodes, naamlik stoom ontploffing en ioniese vloeistof fraksionering in wisselende toestande. Die studie geïllustreer die tipes onttrek en gefractioneerd LCCs van hemisellulose pre-onttrek pulp en WIS in vergelyking met die nie-onttrek pulp en verslae van die literatuur. Lignien-koolhidraat komplekse (LCCs) is geïsoleer en gefraksioneer deur 'n anorganiese metode wat redelike kwantifisering hoeveelhede en geen besoedeling en lae opbrengste opgelewer vir die hardehout vergelyking met verslae van die gebruik van 'n ensiematiese metode. Na die beste kennis van die skrywers, het geen werk op WIS materiaal gedoen. Die lignocelluloses is onderworpe aan die bal maal wat gevolg is deur 'n reeks van anorganiese oplosmiddels swelling en ontbinding in 2 breuke dws glucan-lignien en Xylan-lignien-glucan. Karakterisering van die geïsoleerde LCCs is gemaak met behulp van 'n verskeidenheid van analitiese gereedskap soos FTIR-PCA, HPLC, GPC en GC-MS. LCCs was duidelik wanneer FTIR en HPLC studies is uitgevoer. Residuele lignien geïsoleerd van die lignocelluloses is aanvaar moet word chemies gebind aan koolhidrate en meestal te xylan. Ongeveer 60% en 30% van die lignien is gekoppel aan xylan terwyl dit vir die tweede en eerste breuke onderskeidelik. Dit is gerapporteer dat lignien wat verband hou met Xylan is meer bestand en die delignification proses as wanneer gekoppel aan glucane wat maklik hidroliseerbare verminder. Met die FTIR en GPC ontledings van LCC breuke, was dit duidelik dat die ester bande van LCCs is deur pre-ontginning en pre-behandeling, waar dit gelei tot meer sellulose om meer toeganklik te alkaliese verpulping en ensiematiese hidrolise onderskeidelik vernietig. Die skakeling is óf gedeeltelik afgebreek of heeltemal vernietig lei tot beduidende veranderinge van chemiese strukture. Die polydispersity van die LCCs bygestaan in die bepaling van die struktuur van lignien, hetsy bestaande as monolignols op die oppervlak van die vesel of 'n as komplekse twee of drie-dimensionele struktuur wat gekoppel is aan koolhidrate as die Mw vermeerder of verminder. In die algemeen, kan hierdie bevindinge het 'n belangrike implikasie vir die algehele doeltreffendheid op bio-raffinadery. Die molekulêre gewigte (Mw) die onttrek LCCs gemeet deur gelpermeasie- chromatografie. Van die chromatograms, was dit opgemerk dat die materiaal wat blootgestel is aan die pre-verwerking voor verdere verwerking, die Mw verskuif MWS streke te verlaag. Daar is gevind dat LCCs geïsoleerd van ligte alkali pre-onttrek pulp het hoë lignien syringyl lignien inhoud as LCCs geïsoleerd van verdunde suur vooraf onttrek pulp te guaiacyl. Hoë syringyl / guaiacyl verhouding (S/G-verhouding) was 'n aanduiding van 'n lae lignien inhoud as 'n resultaat van verwerking wat sal lei tot 'n hoë produk opbrengste ná stroomaf verwerking. Die gemiddelde S/G-verhouding vir die pulp van E. grandis en suikerriet bagasse was wat wissel tussen 1,1-19,01 en 1,4-18,16 onderskeidelik, terwyl dit vir die WIS-materiaal gegenereer uit ioniese vloeistof gefraksioneer en stoom ontplof materiaal het gewissel 3,29-9,27 en 3.5 13,3 onderskeidelik. Die S/G verhoudings van die LCCs onttrek uit E. grandis en suikerriet bagasse pulp gewissel 0,42-2,39 en ,041-,31 was onderskeidelik terwyl dit vir die LCCs onttrek uit water-oplosbare-vastestowwe (WIS) materiaal gegenereer uit stoom ontplof materiaal was van 4,87-10,40. Die bepaling van S/G-verhouding word aanbeveel vir die LCC ontginning en karakterisering studie as 'n evaluering van die oorblywende lignien in verwerkte materiaal soos pulp en WIS. Die verkry saccharifications was laag, moontlik as gevolg van die erns van die stoom ontploffing pre-behandeling en ioniese vloeistof fraksionering voorwaardes wat gelei op 'n hoë opeenhoping van asynsuur en vermeerder in sellulose kristalliniteit.

Ph.D. / The main objective of this study was to investigate the presence, variations and the fate of lipophilic extractives during all the stages in the dissolving pulp production process. Lipophilic wood extractives which include fatty acids, sterols, hydrocarbons, steroid hydrocarbons and ketones are organic compounds present in the wood and dissolving pulp which are soluble in organic solvents. Their presence in wood and pulp has negative effects on both the pulping process and the quality of the produced dissolving pulp. Comparison of two Eucalyptus species (E. grandis and E. dunnii) at three different sites (Richmond, Umvoti and Ixopo in KwaZulu-Natal Province, South Africa) revealed that lipophilic extractives were higher in E. dunnii than in E. grandis in all the sampled sites and that the woods at the Ixopo site were found to have the highest amount of lipophilic extractives. The quantitative variation of lipophilic extractives in wood was found to be significantly affected by respective sites and tree species. The principal component analysis (PCA) model, which was used to correlate soil parameters and amount of lipophilic extractives in woods per each site, revealed that high amounts of lipophilic extractives were found in trees grown at sites with a high composition of clay soil and organic matter. Thus if the industry is to avoid the high levels of lipophilic extractives in wood, sandy sites should be the choice to grow the trees. Partial least squares (PLS) modelling revealed that sterols and saturated fatty acids significantly influence the quality parameters (Kappa number, viscosity, copper number, cellulose yield and retained carbohydrates) of dissolving pulp, whereas unsaturated fatty acids and unsaturated sterols in particular were found to positively correlate with the Kappa number, thus affecting its measurement.The main objective of this study was to investigate the presence, variations and the fate of lipophilic extractives during all the stages in the dissolving pulp production process. Lipophilic wood extractives which include fatty acids, sterols, hydrocarbons, steroid hydrocarbons and ketones are organic compounds present in the wood and dissolving pulp which are soluble in organic solvents. Their presence in wood and pulp has negative effects on both the pulping process and the quality of the produced dissolving pulp. Comparison of two Eucalyptus species (E. grandis and E. dunnii) at three different sites (Richmond, Umvoti and Ixopo in KwaZulu-Natal Province, South Africa) revealed that lipophilic extractives were higher in E. dunnii than in E. grandis in all the sampled sites and that the woods at the Ixopo site were found to have the highest amount of lipophilic extractives. The quantitative variation of lipophilic extractives in wood was found to be significantly affected by respective sites and tree species. The principal component analysis (PCA) model, which was used to correlate soil parameters and amount of lipophilic extractives in woods per each site, revealed that high amounts of lipophilic extractives were found in trees grown at sites with a high composition of clay soil and organic matter. Thus if the industry is to avoid the high levels of lipophilic extractives in wood, sandy sites should be the choice to grow the trees. Partial least squares (PLS) modelling revealed that sterols and saturated fatty acids significantly influence the quality parameters (Kappa number, viscosity, copper number, cellulose yield and retained carbohydrates) of dissolving pulp, whereas unsaturated fatty acids and unsaturated sterols in particular were found to positively correlate with the Kappa number, thus affecting its measurement. Viscosity of pulp which is an important quality parameter was also found to be positively influenced by sterol residues, whereas the reducing properties of pulp were found to be affected by sterols and saturated fatty acids with a carbon chain length of less than C20.

As part of CSIR Biosciences’ interest in aroma chemicals, the processing of crude sulphated turpentine (CST) into high value aroma products was investigated. The primary target product, linalool, was obtained from a mixture of α- and β-pinene in four steps. It can be transformed into a wide range of high value added aroma chemicals. Isomerisation of linalool in the presence of a transition metal catalyst furnishes geraniol and nerol. The scientific work described in this report was part of a bigger project aimed at developing innovative processes to manufacture aroma, flavour & fragrance chemicals through beneficiation of industrial waste streams and other raw materials, available locally from the Forestry, Paper & Pulp industries. The evaluation of a process for the preparation of precursor aroma, flavour & fragrance compounds, in particular geraniol and nerol, from locally available raw materials and industrial waste streams, was investigated. Preparation of geraniol and nerol from linalool (ex α-pinene stream) was investigated using acids or organometallic complexes as catalysts for the corresponding isomerisation reaction. The investigation was conducted in an effort to find a less costly process utilising milder conditions than via the conventional cleavage of β-pinene to myrcene under extreme pyrolysis conditions (>650°C). The transformation of linalool to geraniol/nerol using mineral acids was found to be dominated by secondary reactions such as dehydration and cyclisation, resulting in poor product selectivities and yields. On the other hand, organometallic complexes, in particular vanadium-based complexes (e.g. (OV(OBu)3) produced satisfactory results in the preliminary assessment (conversion of 79.8 percent and selectivity of 98.3 percent). A set of statistically designed experiments was carried out on the (VO(BuO)3 + [(Bu)4N+]OH¯) catalyst system where three variables were tested, i.e. substrate concentration, temperature, and catalyst loading. The selected model for conversion was significant with the “Probability > F” being < 0.0001. The most important contributing variable to the model for conversion was temperature i.e. 83.9 percent. Temperature was still the most important variable for the selectivity response at 65.0 percent contribution level. The response surface generated for the selectivity response was flat indicating a robust method within the parameter range selected.

No description available.