Lignocellulose can become the best opportunity for the society to reduce its dependency on the harmful petroleum based products as well as to produce clean energy. In each part of the production cycle, biomass based products have a better environmental profiles than their petroleum based counterparts. Woody biomass has a vast availability, but it suffers from recalcitrance that is mostly caused by lignin that is functioning as a matrix, surrounding and binding the carbohydrates that are currently the most valuable of the wood components. Lignin-carbohydrate (LC) bonds are believed to be a key element in this recalcitrance and research has shown that these types of bonds are common in wood. These bonds are important in an economical point of view as well, as e.g. residual lignin structures in pulp (lignins bonded to the cellulose and hemicelluloses) require expensive bleaching sequences for their removal. The LC-structures can also be exploited technically as we now have demonstrated. We developed a method that utilizes phenolic end groups that are bonded to different hemicelluloses for cross-linking. The enzyme laccase was used for the cross-linking to create a cost-efficient processing scheme to both isolate and increase the molecular weight of the hemicelluloses. Membrane filtration was used as the key separation technique, which enables the establishment of industrial scale production. The final product had improved mechanical and thermal properties and could be used e.g. as barrier film component in renewable packaging. Nanocomposite formation with nanofibrillated cellulose was also studied. This improved the film properties further. The complexes are also possible to use as model compounds for lignin-carbohydrate complexes in wood. This technique can also be seen to mimick the lignification and lignin-carbohydrate network formation phenomena in plants enabling the formation of entire networks of wood components. Our results suggests that the side chains of hemicellulose might play an important role in network formation and that hemicellulose molecules can carry more than one lignin phenolic end group to fulfill this capability. / <p>QC 20140825</p>

京都大学 / 0048 / 新制・課程博士 / 博士(農学) / 甲第18324号 / 農博第2049号 / 新制||農||1021(附属図書館) / 学位論文||H26||N4831(農学部図書室) / 31182 / 京都大学大学院農学研究科森林科学専攻 / (主査)教授 髙野 俊幸, 教授 西尾 嘉之, 教授 梅澤 俊明 / 学位規則第4条第1項該当 / Doctor of Agricultural Science / Kyoto University / DFAM

京都大学 / 0048 / 新制・課程博士 / 博士(農学) / 甲第19194号 / 農博第2133号 / 新制||農||1034(附属図書館) / 学位論文||H27||N4940(農学部図書室) / 32186 / 京都大学大学院農学研究科森林科学専攻 / (主査)教授 髙野 俊幸, 教授 西尾 嘉之, 教授 梅澤 俊明 / 学位規則第4条第1項該当 / Doctor of Agricultural Science / Kyoto University / DGAM

Woody plants are the most abundant renewable resources on the earth. From the paper we consume to the house we live in, our daily lives rely heavily on woody plants. Over the past decades, enormous efforts have been expended to improve the utilization of fiber and wood. For example, much research has been conducted to develop environmentally benign, and economically feasible techniques for pulp and papermaking. The economical conversion of wood to useful sugars and alcohol has also been the subject of intensive research. Investigations aimed at the genetic manipulation of wood growth to better meet our needs are also underway. Nonetheless, harsh pulping and bleaching conditions are still required in the pulp and paper industry, and the bioconversion of polysaccharides in biomass to alcohol is still too expensive. An argument could be put forth that a major reason for this is the lack of basic knowledge concerning the structural and biochemical characteristics of the plant cell wall. The three major polymeric components of plant cell walls, cellulose, hemicellulose and lignin, are intimately associated with one another. Cellulose is associated with hemicellulose via non-covalent linkages, whereas lignin is theorized to be associated with cellulose and hemicellulose via both covalent and non-covalent linkages. The nature of associations between wood polymers is still poorly understood. However, it is these intimate associations that make delignification difficult, and make the bioconversion of polysaccharides to alcohol inefficient. It is also believed that the linkages between lignin and polysaccharides are responsible for the reduced digestibility of grasses by ruminants. Besides cellulose, hemicellulose and lignin, there are many secondary metabolites such as lignans, neolignans, tannins and terpenoids. The structures of lignans and neolignans are analogous to the interunits of lignin. Lignin is considered an optically inactive polymer, whereas lignans and neolignans are optically active small molecules. Although it has been proposed that the biosynthesis of lignin, lignans and neolignans are via the same oxidative coupling mechanism, it is still unclear that how the plant cell wall differentiates the formation of lignans, neolignans and lignin. How and why plant cell wall generates so many lignans and neolignans having broad structural variation is also unknown. As a matter of fact, it is still uncertain which enzymes are actually involved in the biosynthesis of lignin. A better understanding of biosynthetic pathways of lignin, lignans and neolignans is a prerequisite for the genetic manipulation of plant growth. Investigations described in this dissertation were an effort to better understand the fundamental aspects of covalent linkages between lignin and hemicellulose in wood. Enantiomeric synthesis of neolignans provides a tool for investigating the optically active nature of neolignans, and may be helpful to study the biosynthetic pathways of neolignans. Chapter | describes chemical structures of wood components and the biosynthesis of lignin, lignans and neolignans. The mechanisms of lignin-carbohydrate bond formation are also discussed, and a concise review of lignin-carbohydrate linkages proposed in the literature concludes Chapter 1. Chapter 2 presents the methods used in investigating covalent linkages in wood, which include methods of isolating lignin-carbohydrate complexes, chemical cleavage methods, DDQ oxidation and model compound/NMR methods. The synthesis of plant cell wall model compounds and neolignans are reviewed in Chapter 3. The experimental work performed for the completion of this thesis is described in Chapters 4-8. A method which provides β-𝘖-4 lignin model dimers with complete threo stereospecificity is described in Chapter 4. This method is complementary to the current method for the preparation of erythro lignin model dimers. Chapter 5 presents a practical synthesis of methyl 4-𝘖-methy] α-D-glucopyranosiduronic acid. Methyl 4-𝘖-methyl-α-D-glucopyranosiduronic acid was prepared from methyl α-D-glucopyranoside in 4 steps (74% overall yield). Previous preparations of this compound were much lengthier, and had very low overall yields. Chapter 6 deals with the synthesis and rearrangement reactions of ester-linked lignin-carbohydrate model compounds. A series of ester-linked lignin-carbohydrate model compounds were synthesized, and migration of the uronosy] group between the primary (γ) and benzyl (α) position of lignin side chain is discussed. Several approaches to synthetic neolignans are described in Chapter 7. Chapter 8 presents a novel approach for the preparation of chiral aryl alkylethers. The successful application of this novel approach to synthesis of several optically active 8-𝘖-4 neolignans and a 1,4- benzodioxane neolignan is described, as is the introduction of an alkyl] aryl ether bond in carbohydrate molecules. Some of the material of this dissertation has been reported in the following papers: 1. Li, K. and Helm, R. F. Approaches to Synthetic Neolignans. J. Chem. Soc. Perkin Trans 1. Accepted. 6. Li, K. and Helm, R. F. Use of Carbohydrates as Building Blocks to Synthesize Neolignans. 211th ACS National ACS Meeting, New Orleans, March 24-28, 1996. CELL-079. 2. Li, K. and Helm, R. F. A Practical Synthesis of Methyl 4-𝘖-Methylα-D-Glucopyranosiduronic Acid. Carbohydr. Res. 273(1995), 249-253. 3. Li, K. and Helm, R. F. Synthesis and Rearrangement Reactions of Ester-Linked Lignin-Carbohydrate Model Compounds. J. Agric. Food Chem. 48(1995), 2098-2103. 4. Helm, R. F. and Li, K. Complete threo Stereospecificity for the Preparation of β-𝘖-4 Lignin Model Dimers. Holzforschung. 49(1995), 533-536. 5. Helm, R. F. and Li, K. Synthesis and Rearrangement Reactions of Lignin-uronic Acid Model Compounds Related to Hardwood Cell Wall Structure. The 8th International Symposium on Wood and Pulping Chemistry. Helsinki, Finland, June 1995, vol. 1, pp107-114. 7. Li, K. and Helm, R. F. Approaches to Synthetic Neolignans, 34th National Organic Symposium, Williamsburg, VA. June 11-15, 1995. Poster 281. / Ph. D.

Single stage and two-stage sodium sulfite cooking were carried out on either spruce, pine or pure pine heartwood chips to investigate the influence of several process parameters on the initial phase of such a cook down to about 60 % pulp yield. The cooking experiments were carried out in the laboratory with either a lab-prepared or a mill-prepared cooking acid and the temperature and time were varied. The influences of dissolved organic and inorganic components in the cooking liquor on the final pulp composition and on the extent of side reactions were investigated. Kinetic equations were developed and the activation energies for delignification and carbohydrate dissolution were calculated using the Arrhenius equation. A better understanding of the delignification mechanisms during bisulfite and acid sulfite cooking was obtained by analyzing the lignin carbohydrate complexes (LCC) present in the pulp when different cooking conditions were used. It was found that using a mill-prepared cooking acid beneficial effect with respect to side reactions, extractives removal and higher stability in pH during the cook were observed compared to a lab-prepared cooking acid. However, no significant difference in degrees of delignification or carbohydrate degradation was seen.  The cellulose yield was not affected in the initial phase of the cook however; temperature had an influence on the rates of both delignification and hemicellulose removal. It was also found that the  corresponding activation energies increased in the order:  xylan, glucomannan, lignin and cellulose. The cooking temperature could thus be used to control the cook to a given carbohydrate composition in the final pulp. Lignin condensation reactions were observed during acid sulfite cooking, especially at higher temperatures. The LCC studies indicated the existence of covalent bonds between lignin and hemicellulose components with respect to xylan and glucomannan. LCC in native wood showed the presence of phenyl glycosides, ϒ-esters and α-ethers; whereas the α-ethers  were affected during sulfite pulping. The existence of covalent bonds between lignin and wood polysaccharides might be the rate-limiting factor in sulfite pulping. / The sulfite pulping process is today practised in only a small number of pulp mills around the globe and the number of sulfite mills that use sodium as the base (cation) is less than five. However, due to the increasing interest in the wood based biorefinery concept, the benefits of sulfite pulping and especially the sodium based variety, has recently gained a lot of interest. It was therefore considered to be of high importance to further study the sodium based sulfite process to investigate if its benefits could be better utilized in the future in the production of dissolving pulps. Of specific interest was to investigate how the pulping conditions in the initial part of the cook (≥ 60 % pulp yield) should be performed in the best way. Thus, this thesis is focused on the initial phase of sodium based single stage bisulfite, acid sulfite and two-stage sulfite cooking of either 100 % spruce, 100 % pine or 100 % pine heartwood chips. The cooking experiments were carried out with either a lab prepared or a mill prepared cooking acid and the temperature and cooking time were varied. Activation energies for different wood components were investigated as well as side reactions concerning the formation of thiosulfate. LCC (Lignin carbohydrates complexes) studies were carried out to investigate the influence of different cooking conditions on lignin carbohydrate linkages.

La valorisation de la biomasse lignocellulosique est aujourd’hui un enjeu majeur du fait de la réduction des ressources fossiles. Séparer chaque constituant pour les valoriser de la meilleure façon possible est l’objectif des bioraffineries papetières. L’effluent papetier, la liqueur noire, est actuellement brûlé pour produire de l’énergie, mais sa gazéification permettrait d’augmenter ces rendements énergétiques. Mais pour cela une cuisson sans soufre du bois est nécessaire, le soufre inhibant la gazéification.Cette étude a donc porté en premier lieu sur la faisabilité d’un fractionnement sans soufre du bois, plus ardu qu’un procédé kraft traditionnel contenant du soufre. Le travail a été effectué sur les bois résineux, ceux-ci étant plus difficiles à délignifier que les bois feuillus. Une étape d’autohydrolyse du bois, préalable au fractionnement à la soude, a été effectuée afin d’extraire les hémicelluloses pour une valorisation ultérieure. Les travaux ont montré que ce prétraitement permettait de délignifier le bois plus facilement et ainsi d’envisager un fractionnement sans soufre. La cellulose obtenue par ce procédé présente une pureté et un degré de polymérisation suffisants pour envisager son utilisation pour de la viscose ou pour des applications chimiques.La lignine ne présentant pas de différences structurelles majeures entre du bois préhydrolysé ou non, les complexes entre la lignine et les hydrates de carbone (LCC) ont été analysés. Il a été montré que la préhydrolyse modifie significativement la quantité et la composition de ces complexes, permettant d’expliquer par là les résultats obtenus. / The valorization of lignocellulosic biomass is nowadays a major issue due to the reduction of fossil resources. Separating each component to valorize them the best way as possible is the goal of the pulp and paper biorefineries. The effluent of the mill, called the black liquor, is currently burnt to produce energy, but gasification would increase the energy efficiency. For this, a sulfur-free cooking of wood is necessary, as sulfur inhibits gasification.Therefore this study first focused on the feasibility of cooking without sulfur, which is more difficult than a conventional kraft cooking containing sulfur. The work was done on softwood which is more difficult to delignify than hardwood. The wood was first pretreated with an autohydrolysis to remove hemicelluloses for further valorization.The results were conclusive for the production of cellulose pulp for chemical applications. To explain the differences obtained, structural differences of wood components were looked for. Lignin did not show major differences whether the wood was prehydrolyzed or not, whereas the complexes between lignin and carbohydrates (LCCs) showed significant differences, which would explain the results obtained.