Potential to decrease GHG emissions from biomass resources in China

This paper describes the environment issues which are caused by fossil fuel utilization, and the available of biomass resources and relevant applications in China and relevant policy for supporting biomass resources development. In addition the sustainable technology for energy and fuels generation in China and the advantages and disadvantages of technologies are presented as well. This paper aims to find out how the policy can promotes the biomass resource development and from environment aspect to see why the biomass resources should replace fossil fuels in the future. In this paper the life cycle assessment of straw biomass resource will be as an example to present the same amount of energy produced by straw and coal, the different amount of emission will be emitted.

Biomass based energy system for a South Indian village

The biomass resources, existing utilization levels and the efficiency of its use have been analyzed for a South Indian village. A biomass based energy efficient strategy has been devised to meet all the energy needs of the village, including substitution of fuels such as electricity and kerosene used in specific activities. Results indicate that the potential as well as the technologies exist for such substitutions. The proposed strategy will lead to an increase in the efficiency of energy use, reduce human drudgery and make villages more self reliant.

A review of biomass co-firing in North America

Biomass fuels have long been accepted as useful renewable energy sources, especially in mitigating greenhouse gases (GHG), nitrogen oxides, and sulfur oxide emissions. Biomass fuel is carbon neutral and is usually low in both nitrogen and sulfur. For the past decade, various forms of biomass fuels have been co-combusted in existing coal-fired boilers and gas-fired power plants. Biomass is used as a supplemental fuel to substitute for up to 10% of the base fuel in most full commercial operations. There are several successful co-firing projects in many parts of the world, particularly in Europe and North America. However, despite remarkable commercial success in Europe, most of the biomass co-firing in North America is limited to demonstration levels. This review takes a detailed look at several aspects of biomass co-firing with a direct focus on North America. It also explores the benefits, such as the reduction of GHG emissions and its implications. This paper shows the results of our studies of the biomass resources available in North America that can be used in coal-fired boilers, their availability and transportation to the power plant, available co-firing levels and technologies, and various technological and environmental issues associated with biomass co-firing. Finally, the paper proffers solutions to help utility companies explore biomass co-firing as a transitional option towards a completely carbon-free power sector in North America.

Biomass fuelled combined heat and power:situation in the UK and the Netherlands

Combined Heat and Power (CHP) is the simultaneous generation of usable heat and power in a single process. Despite its obvious advantages in terms of increased efficiency when compared to a single heat or power generation unit, there are a number of technical and economic reasons that have limited their selection. Biomass resources can be, and actually are used as fuel in CHP installations; however several hurdles have to be sorted beforehand, among the most important is the fact that biomass energy sources are not as energy intense as conventional CHP fuels. The ultimate outcome is a limited number of CHP units making use of biomass as fuel. Even fewer CHP units use bioliquids (e.g.: fast pyrolysis biomass liquids, biodiesel and vegetable oil). The Bioliquid-CHP project is carried out by a consortium of seven European and Russian complementary partners, funded by the EU and by the Federal Agency for Science and Innovation of the Russian Federation. The project aim is to develop microturbine and internal combustion engine adaptations in order to adjust these prime movers to bioliquids for CHP applications. This paper will show a summary of the current biomass CHP installations in the UK and the Netherlands, making reference to number of units, capacity, fuel used, the conversion technology involved and the preferred prime movers. The information will give an insight of the current market, with probable future trends and areas where growth could be expected. A similar paper describing the biomass CHP situation in Italy and Russia will be prepared in the near future.

Trigeneration using biomass energy for sustainable development

Purpose: The paper aims to design and prove the concept of micro-industry using trigeneration fuelled by biomass, for sustainable development in rural NW India. Design/methodology/approach: This is being tested at village Malunga, near Jodhpur in Rajasthan. The system components comprise burning of waste biomass for steam generation and its use for power generation, cooling system for fruit ripening and the use of steam for producing distilled water. Site was selected taking into account the local economic and social needs, biomass resources available from agricultural activities, and the presence of a NGO which is competent to facilitate running of the enterprise. The trigeneration system was designed to integrate off-the-shelf equipment for power generation using boilers of approximate total capacity 1 tonne of fuel per hour, and a back-pressure steam turbo-generator (200 kW). Cooling is provided by a vapour absorption machine (VAM). Findings: The financial analysis indicates a payback time of less than two years. Nevertheless, this is sensitive to market fluctuations and availabilities of raw materials. Originality/value: Although comparable trigeneration systems already exist in large food processing industries and in space heating and cooling applications, they have not previously been used for rural micro-industry. The small-scale (1-2 m3/h output) multiple effect distillation (3 effect plus condenser) unit has not previously been deployed at field level. © Emerald Group Publishing Limited.

Design and construction of fixed bed pyrolysis system and plum seed pyrolysis for bio-oil production

This work investigated the production of bio oil from plum seed (Zyziphus jujuba) by fixed bed pyrolysis technology. A fixed bed pyrolysis system has been designed and fabricated for production of bio oil. The major components of the system are: fixed bed reactor, liquid condenser and liquid collector. Nitrogen gas was used to maintain the inert atmosphere in the reactor where the pyrolysis reaction takes place. The feedstock considered in this study is plum seed as it is available waste material in Bangladesh. The reactor is heated by means of a cylindrical biomass external heater. Rice husk was used as the energy source. The products are oil, char and gas. The parameters varied are reactor bed temperature, running time and feed particle size. The parameters are found to influence the product yields significantly. The maximum liquid yield of 39 wt% at 5200C for a feed particle size of 2.36-4.75 mm and a gas flow rate of 8 liter/min with a running time of 120 minute. The pyrolysis oil obtained at these optimum process conditions are analyzed for some of their properties as an alternative fuel. The density of the liquid was closer with diesel. The viscosity of the plum seed liquid was lower than that of the conventional fuels. The calorific value of the pyrolysis oil is one half of the diesel fuel.

玉米新老品种生理生态特征与竞争力差异研究

本文以中国不同年代主要的玉米品种为试验材料，深入研究了玉米品种更替过程中新老品种的生理生态特征和竞争力差异，分析了差异形成的原因并进行了理论探讨。 玉米新老品种竞争力差异的研究采用了单作和混作两种方式，设高低两个密度。生长过程中全面测量了生物量、形态、生理和群体指标，运用了生长分析的方法来研究竞争，整合了各水平参数来解释竞争结果，并用本研究数据检验了生长冗余理论。 玉米新老品种对比研究发现新品种的生理生态特征普遍优于老品种。这些优势不仅体现在较高的生物量积累、较大的籽粒库容和较强的再分配能力上，而且体现在高的叶面积指数、衰老过程中仍维持较高的叶绿素含量、可溶性蛋白含量和光合效率上，同时新品种的群体特性还具有更低的感病率和更少的无效分蘖。玉米新老品种竞争结果表明在混作条件下，相对总产量这一指标反映出新老品种间明显的互利效应，且这种效应随发育阶段而降低。新品种对老品种的相对竞争力则随着发育阶段波动，并且密度和发育阶段两因子对品种竞争力的影响有明显的相互作用。相对于新品种，老品种的确存在叶片和根系的生长冗余部分，但老品种并没有在混作竞争中获得明显的竞争优势，即玉米品种选育并不完全符合生长冗余理论，因此在理解植物竞争力方面仍需要其他层面更深入的探讨。 同时，玉米品种选育不完全符合生长冗余理论的结论在农学实践上并非毫无价值。因为新品种总生物量的提高，不仅增加了籽粒产量，而且增加了秸秆产量，提供了更多可利用的生物质资源。相对于仅仅关注粮食产量，综合利用中国农村巨大的生物质资源具有更重要的生态意义。

Um modelo de avaliação de fluxos de biomassa e carbono em madeireiras de comunidades isoladas da região amazônica

A Amazônia tem imensos recursos florestais, abrigando um terço das florestas tropicais do mundo. A Amazônia brasileira compreende uma área maior que 5 milhões de km², o que corresponde a 61 % do território brasileiro. A região norte produz 72,45% da madeira em tora do Brasil, o estado do Pará contribui com 55,47% de acordo com IBMA (2007). A exploração madeireira na Amazônia é caracterizada como “garimpagem florestal”, ou seja, os exploradores entram na floresta selecionam as toras de valor comercial e a retiram. Passando-se certo tempo, eles voltam novamente a essa área e a exploram, esse processo de exploração está acontecendo em um intervalo de tempo cada vez menor. A Amazônia legal abrigava 833 serrarias circulares em 1998. Essas serrarias estavam localizadas principalmente no estuário amazônico (71%) – nos furos e tributários dos rios Amazonas, Xingu, Tocantins e Pará. Essas processadoras familiares consumiram conjuntamente 1,3 milhões de metros cúbicos de madeira em tora (5% da produção da Amazônia). Neste trabalho estimou-se o balanço de carbono em serrarias do estuário do rio Amazonas e foi desenvolvido o ciclo de vida do carbono para uma serraria no estuarino amazônico. Foi identificado que no processo produtivo da comunidade há um caminho bem definido do recurso natural (biomassa/madeira): exploração florestal, transporte de biomassa, transformação (empresas madeireiras) / processos produtivos, geração e utilização de resíduos, transporte de madeira processada, comercialização/mercado. O objetivo deste trabalho foi avaliar os recursos energéticos através do fluxo (inputs e outputs) da madeira e da energia no processo. Para isso, desenvolveu um modelo que simulou os fluxos de carbono, da madeira e a área afetada pela exploração. Neste trabalho criou-se um modelo específico onde se avaliou o fluxo de carbono para o cenário estudado; a avaliação do impacto ambiental foi alcançada, onde obteve um valor positivo, uma captura de carbono cerca de 55 tCO₂/mês, mesmo com a baixa eficiência do sistema produtivo, em torno de 36% conclui-se que o sistema atual de exploração não polui mas poderia ser melhorado a fim de alcançar uma maior eficiência do processo produtivo. Enquanto ao resíduo gerado aproximadamente 64% do volume de madeira que entra na serraria conseguira gerar aproximadamente 1240 kW de energia elétrica mensal.

Valorización energética de biomasas en el marco de la política energética española. Incentivos económico-financieros y políticos, aportación de valor añadido y prospectiva estratégica de desarrollo

El modelo económico actual basado en el consumo y en la búsqueda permanente de una mayor calidad de vida, unido a una población mundial en aumento, contribuye a incrementar la demanda de servicios energéticos para cubrir las necesidades de energía de las personas y las industrias. Desde finales del siglo XIX la energía se ha generado fundamentalmente a partir de combustibles fósiles (carbón, petróleo y gas), convertidos en el suministro energético predominante mundialmente. Las emisiones de gases de efecto invernadero que genera la prestación de servicios energéticos han contribuido considerablemente al aumento histórico de las concentraciones de esos gases en la atmósfera, hasta el punto de que el consumo de combustibles fósiles es responsable de la mayoría de las emisiones antropogénicas (IPCC, 2012). Existen diversas opciones para disminuir las emisiones de gases de efecto invernadero del sector energético y con ello contribuir a mitigar el cambio climático, entre otras sería viable aumentar la eficiencia energética y sustituir combustibles de origen fósil por combustibles de origen renovable, pudiendo garantizar un suministro de energía sostenible, competitivo y seguro. De todas las energías renovables susceptibles de formar parte de una cartera de opciones de mitigación, esta tesis se centra en la bioenergía generada a partir de la valorización energética de las biomasas agrícolas, forestales, ganaderas o de otro tipo, con fines eléctricos y térmicos. Con objeto de mostrar su capacidad para contribuir a mitigar el cambio climático y su potencial contribución al desarrollo socioeconómico, a la generación de energía distribuida y a reducir determinados efectos negativos sobre el medio ambiente, se ha analizado minuciosamente el sector español de la biomasa en su conjunto. Desde el recurso biomásico que existe en España, las formas de extraerlo y procesarlo, las tecnologías de valorización energética, sus usos energéticos principales y la capacidad de implementación del sector en España. Asimismo se ha examinado el contexto energético tanto internacional y europeo como nacional, y se han analizado pormenorizadamente los instrumentos de soporte que han contribuido de manera directa e indirecta al desarrollo del sector en España. Además, la tesis integra el análisis de los resultados obtenidos mediante dos metodologías diferentes con fines también distintos. Por un lado se han obtenido los resultados medioambientales y socioeconómicos de los análisis de ciclo de vida input-output generados a partir de las cinco tecnologías biomásicas más ampliamente utilizadas en España. Y por otro lado, en base a los objetivos energéticos y medioambientales establecidos, se han obtenido distintas proyecciones de la implementación del sector a medio plazo, en forma de escenarios energéticos con horizonte 2035, mediante el modelo TIMES-Spain. La tesis ofrece también una serie de conclusiones y recomendaciones que podrían resultar pertinentes para los agentes que constituyen la cadena de valor del propio sector e interesados, así como para la formulación de políticas y mecanismos de apoyo para los agentes decisores, tanto del ámbito de la Administración General del Estado como autonómico y regional, sobre las características y ventajas de determinadas formas de valorización, sobre los efectos sociales y medioambientales que induce su uso, y sobre la capacidad de sector para contribuir a determinadas políticas más allá de las puramente energéticas. En todo caso, esta tesis doctoral aspira a contribuir a la toma de decisiones idóneas tanto a los agentes del sector como a responsables públicos, con objeto de adoptar medidas orientadas a fomentar modificaciones del sistema energético que incrementen la proporción de energía renovable y, de esta forma, contribuir a mitigar la amenaza que supone el cambio climático no solo en la actualidad, sino especialmente en los próximos años para las generaciones venideras. ABSTRACT The current economic model based on both, consumption and the constant search for greater quality of life, coupled with a growing world population, contribute to increase the demand for energy services in order to meet the energy needs of people and industries. Since the late nineteenth century, energy has been basically generated from fossil fuels (coal, oil and gas), which converted fossil fuels into the predominant World energy supply source. Emissions of greenhouse gases generated by the provision of energy services have contributed significantly to the historical increase in the concentrations of these gases in the atmosphere, to the extent that the consumption of fossil fuels is responsible for most of the anthropogenic emissions (IPCC, 2012). There are several options to reduce emissions of greenhouse gases in the energy sector and, thereby, to contribute to mitigate climate change. Among others, would be feasible to increase energy efficiency and progressively replacing fossil fuels by renewable fuels, which are able to ensure a sustainable, competitive and secure energy supply. Of all the renewable energies likely to form part of a portfolio of mitigation options, this thesis focuses on bioenergy generated from agricultural, forestry, farming or other kind of biomass, with electrical and thermal purposes. In order to show their ability to contribute to mitigate climate change and its potential contribution to socio-economic development, distributed energy generation and to reduce certain negative effects on the environment, the Spanish biomass sector as a whole has been dissected. From the types of biomass resources that exist in Spain, ways of extracting and processing them, energy production technologies, its main energy uses and the implementation capacity of the sector in Spain. It has also examined the international, European and national energy context, and has thoroughly analyzed the support instruments that have contributed directly and indirectly to the development of the sector in Spain, so far. Furthermore, the thesis integrates the analysis of results obtained using two different methodologies also with different purposes. On the one hand, the environmental and socio-economic results of the analysis of input-output cycle life generated from the five biomass technologies most widely used in Spain, have been obtained. On the other hand, different projections of the implementation of the sector in the medium term, as energy scenarios with horizon 2035, have been obtained by the model TIMES-Spain, based on several energy and environmental objectives. The thesis also offers a series of conclusions and recommendations that could be relevant to the agents that constitute the value chain of the biomass sector itself and other stakeholders. As well as policy and support mechanisms for decision-makers, from both: The Central and Regional Governments, on the characteristics and advantages of certain forms of valorization, on the social and environmental effects that induce their use, and the ability of the biomass sector to contribute to certain policies beyond the purely energy ones. In any case, this thesis aims to contribute to decision making, suitable for both: Industry players and to public officials. In order to adopt measures to promote significant changes in the energy system that increase the proportion of renewable energy and, consequently, that contribute to mitigate the threat of climate change; not only today but in the coming years, especially for future generations.

Low severity Fischer-Tropsch synthesis for the production of synthetic hydrocarbon fuels

Currently, the main source for the production of liquid transportation fuels is petroleum, the continued use of which faces many challenges including depleting oil reserves, significant oil price rises, and environmental concerns over global warming which is widely believed to be due to fossil fuel derived CO2 emissions and other greenhouse gases. In this respect, lignocellulosic or plant biomass is a particularly interesting resource as it is the only renewable source of organic carbon that can be converted into liquid transportation fuels. The gasification of biomass produces syngas which can then be converted into synthetic liquid hydrocarbon fuels by means of the Fischer-Tropsch (FT) synthesis. This process has been widely considered as an attractive option for producing clean liquid hydrocarbon fuels from biomass that have been identified as promising alternatives to conventional fossil fuels like diesel and kerosene. The resulting product composition in FT synthesis is influenced by the type of catalyst and the reaction conditions that are used in the process. One of the issues facing this conversion process is the development of a technology that can be scaled down to match the scattered nature of biomass resources, including lower operating pressures, without compromising liquid composition. The primary aims of this work were to experimentally explore FT synthesis at low pressures for the purpose of process down-scaling and cost reduction, and to investigate the potential for obtaining an intermediate FT synthetic crude liquid product that can be integrated into existing refineries under the range of process conditions employed. Two different fixed-bed micro-reactors were used for FT synthesis; a 2cm3 reactor at the University of Rio de Janeiro (UFRJ) and a 20cm3 reactor at Aston University. The experimental work firstly involved the selection of a suitable catalyst from three that were available. Secondly, a parameter study was carried out on the 20cm3 reactor using the selected catalyst to investigate the influence of reactor temperature, reactor pressure, space velocity, the H2/CO molar ratio in the feed syngas and catalyst loading on the reaction performance measured as CO conversion, catalyst stability, product distribution, product yields and liquid hydrocarbon product composition. From this parameter study a set of preferred operating conditions was identified for low pressure FT synthesis. The three catalysts were characterized using BET, XRD, TPR and SEM. The catalyst selected was an unpromoted Co/Al2O3 catalyst. FT synthesis runs on the 20cm3 reactor at Aston were conducted for 48 hours. Permanent gases and light hydrocarbons (C1-C5) were analysed in an online GC-TCD/FID at hourly intervals. The liquid hydrocarbons collected were analyzed offline using GC-MS for determination of fuel composition. The parameter study showed that CO conversion and liquid hydrocarbon yields increase with increasing reactor pressure up to around 8 bar, above which the effect of pressure is small. The parameters that had the most significant influence on CO conversion, product selectivity and liquid hydrocarbon yields were reactor temperature and catalyst loading. The preferred reaction conditions identified for this research were: T = 230ºC, P = 10 bar, H2/CO = 2.0, WHSV = 2.2 h-1, and catalyst loading = 2.0g. Operation in the low range of pressures studied resulted in low CO conversions and liquid hydrocarbon yields, indicating that low pressure BTL-FT operation may not be industrially viable as the trade off in lower CO conversions and once-through liquid hydrocarbon product yields has to be carefully weighed against the potential cost savings resulting from process operation at lower pressures.

Termodinâmica e o uso eficiente de recursos : análise exergética de uma biorrefinaria de cana-de-açúcar

Tese (doutorado)—Universidade de Brasília, Faculdade de Tecnologia, Departamento de Engenharia Mecânica, 2015.

New Catalysts for the Renewable Production of Monomers for Bioplastics

Terephthalic acid (PTA) is one of the monomers used for the synthesis of the polyester, polyethylene terephthalate (PET), that is used for the large-scale manufacture of synthetic fibers and plastic bottles. PTA is largely produced from the liquid-phase oxidation of petroleum-derived p-xylene (PX). However, there are now ongoing worldwide efforts exploring alternative routes for producing PTA from renewable, biomass resources.

In this thesis, I present a new route to PTA starting from the biomass-derived platform chemical, 5-hydroxymethylfurfural (HMF). This route utilizes new, selective Diels-Alder-dehydration reactions involving ethylene and is advantageous over the previously proposed Diels-Alder-dehydration route to PTA from HMF via 2,5-dimethylfuran (DMF) since the H₂ reduction of HMF to DMF is avoided. Specifically, oxidized derivatives of HMF are reacted as is, or after etherification-esterification with methanol, with ethylene over solid Lewis acid catalysts that do not contain strong Brønsted acids in order to synthesize intermediates of PTA and its equally important diester, dimethyl terephthalate (DMT). The partially oxidized HMF, 5-(hydroxymethyl)furoic acid (HMFA) is reacted with high pressure ethylene over a pure-silica molecular sieve catalyst containing framework tin (Sn-Beta) to produce the Diels-Alder-dehydration product, 4-(hydroxymethyl)benzoic acid (HMBA), with ~30% selectivity at ~20% yield. If HMFA is protected with methanol to form methyl 5-(methoxymethyl)furan-2-carboxylate (MMFC), MMFC can react with ethylene in the presence of a pure-silica molecular sieve containing framework zirconium (Zr-Beta) to produce methyl 4-(methoxymethyl)benzenecarboxylate (MMBC) with >70% selectivity at >20% yield. HMBA and MMBC can then be oxidized to produce PTA and DMT, respectively. When Lewis acid containing mesoporous silica (MCM-41) and amorphous silica, or Brønsted acid containing zeolites (Al-Beta), are used as catalysts, a significant decrease in selectivity/yield of the Diels-Alder-dehydration product is observed.

An investigation to elucidate the reaction network and side products in the conversion of MMFC to MMBC was performed, and the main side products are found to be methyl 4-formylcyclohexa-1,3-diene-1-carboxylate and the ethylene Diels-Alder adduct of this cyclohexadiene. These products presumably form by a different dehydration pathway of the MMFC/ethylene Diels-Alder adduct and should be included when determining the overall selectivity to PTA or DMT since, like MMBC, these compounds are precursors to PTA or DMT.

Fundamental physical and chemical information on the ethylene Diels-Alder-dehydration reactions catalyzed by the Lewis acid-containing molecular sieves was obtained. Madon-Boudart experiments using Zr-Beta as catalyst show that the reaction rates are limited by chemical kinetics only (physical transport limitations are not present), all the Zr⁴⁺ centers are incorporated into the framework of the molecular sieve, and the whole molecular sieve crystal is accessible for catalysis. Apparent activation energies using Zr-Beta are low, suggesting that the overall activation energy of the system may be determined by a collection of terms and is not the true activation energy of a single chemical step.

Sustainable Energy Production in the United States: Life Cycle Assessment of Biofuels and Bioenergy

The United States of America is making great efforts to transform the renewable and abundant biomass resources into cost-competitive, high-performance biofuels, bioproducts, and biopower. This is the key to increase domestic production of transportation fuels and renewable energy, and reduce greenhouse gas and other pollutant emissions. This dissertation focuses specifically on assessing the life cycle environmental impacts of biofuels and bioenergy produced from renewable feedstocks, such as lignocellulosic biomass, renewable oils and fats. The first part of the dissertation presents the life cycle greenhouse gas (GHG) emissions and energy demands of renewable diesel (RD) and hydroprocessed jet fuels (HRJ). The feedstocks include soybean, camelina, field pennycress, jatropha, algae, tallow and etc. Results show that RD and HRJ produced from these feedstocks reduce GHG emissions by over 50% compared to comparably performing petroleum fuels. Fossil energy requirements are also significantly reduced. The second part of this dissertation discusses the life cycle GHG emissions, energy demands and other environmental aspects of pyrolysis oil as well as pyrolysis oil derived biofuels and bioenergy. The feedstocks include waste materials such as sawmill residues, logging residues, sugarcane bagasse and corn stover, and short rotation forestry feedstocks such as hybrid poplar and willow. These LCA results show that as much as 98% GHG emission savings is possible relative to a petroleum heavy fuel oil. Life cycle GHG savings of 77 to 99% were estimated for power generation from pyrolysis oil combustion relative to fossil fuels combustion for electricity, depending on the biomass feedstock and combustion technologies used. Transportation fuels hydroprocessed from pyrolysis oil show over 60% of GHG reductions compared to petroleum gasoline and diesel. The energy required to produce pyrolysis oil and pyrolysis oil derived biofuels and bioelectricity are mainly from renewable biomass, as opposed to fossil energy. Other environmental benefits include human health, ecosystem quality and fossil resources. The third part of the dissertation addresses the direct land use change (dLUC) impact of forest based biofuels and bioenergy. An intensive harvest of aspen in Michigan is investigated to understand the GHG mitigation with biofuels and bioenergy production. The study shows that the intensive harvest of aspen in MI compared to business as usual (BAU) harvesting can produce 18.5 billion gallons of ethanol to blend with gasoline for the transport sector over the next 250 years, or 32.2 billion gallons of bio-oil by the fast pyrolysis process, which can be combusted to generate electricity or upgraded to gasoline and diesel. Intensive harvesting of these forests can result in carbon loss initially in the aspen forest, but eventually accumulates more carbon in the ecosystem, which translates to a CO2 credit from the dLUC impact. Time required for the forest-based biofuels to reach carbon neutrality is approximately 60 years. The last part of the dissertation describes the use of depolymerization model as a tool to understand the kinetic behavior of hemicellulose hydrolysis under dilute acid conditions. Experiments are carried out to measure the concentrations of xylose and xylooligomers during dilute acid hydrolysis of aspen. The experiment data are used to fine tune the parameters of the depolymerization model. The results show that the depolymerization model successfully predicts the xylose monomer profile in the reaction, however, it overestimates the concentrations of xylooligomers.