955 resultados para Residual forestry biomass


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Within a large set of renewable energies being explored to tackle energy sourcing problems, bioenergy can represent an attractive solution if effectively managed. The supply chain design supported by mathematical programming can be used as a decision support tool to the successful bioenergy production systems establishment. This strategic decision problem is addressed in this paper where we intent to study the design of the residual forestry biomass to bioelectricity production in the Portuguese context. In order to contribute to attain better solutions a mixed integer linear programming (MILP) model is developed and applied in order to optimize the design and planning of the bioenergy supply chain. While minimizing the total supply chain cost the production energy facilities capacity and location are defined. The model also includes the optimal selection of biomass amounts and sources, the transportation modes selection, and links that must be established for biomass transportation and products delivers to markets. Results illustrate the positive contribution of the mathematical programming approach to achieve viable economic solutions. Sensitivity analysis on the most uncertain parameters was performed: biomass availability, transportation costs, fixed operating costs and investment costs. (C) 2015 Elsevier Ltd. All rights reserved.

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The residual forest biomass (RFB) sector has been experiencing strong development at European level and particularly in Portugal mainly due to the increase of energy production from renewable sources. The aim of this study is to assess the environmental impacts of eucalyptus RFB chips production chain in Portugal. The environmental and economic impact comparison of the processes included in the production chain is presented as well. The environmental impacts were calculated by the life cycle assessment approach described in the ISO 14040 series of standards. The production chain assessed included all processes from eucalyptus forest until the delivery of RFB chips at the power plant. The main conclusion of this study is that eucalyptus wood production is the process that presents the greatest environmental impact through the product life cycle.

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The use of residual biomass for energy purposes is of great interest in isolated areas like Majorca for waste reduction, energy sufficiency and renewable energies development. In addition, densification processes lead to easy-to-automate solid biofuels which additionally have higher energy density. The present study aims at (i) the estimation of the potential of residual biomass from woody crops as well as from agri-food and wood industries in Majorca, and (ii) the analysis of the optimal location of potential pellet plants by means of a GIS approach (location-allocation analysis) and a cost evaluation of the pellets production chain. The residual biomass potential from woody crops in Majorca Island was estimated at 35,874 metric tons dry matter (t DM) per year, while the wood and agri-food industries produced annually 21,494 t DM and 2717 t DM, respectively. Thus, there would be enough resource available for the installation of 10 pellet plants of 6400 t·year−1 capacity. These plants were optimally located throughout the island of Mallorca with a maximum threshold distance of 28 km for biomass transport from the production points. Values found for the biomass cost at the pellet plant ranged between 57.1 €·t−1 and 63.4 €·t−1 for biomass transport distance of 10 and 28 km. The cost of pelleting amounted to 56.7 €·t−1; adding the concepts of business fee, pellet transport and profit margin (15%), the total cost of pelleting was estimated at 116.6 €·t−1. The present study provides a proposal for pellet production from residual woody biomass that would supply up to 2.8% of the primary energy consumed by the domestic and services sector in the Balearic Islands.

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Estimates of greenhouse-gas emissions from deforestation are highly uncertain because of high variability in key parameters and because of the limited number of studies providing field measurements of these parameters. One such parameter is burning efficiency, which determines how much of the original forest`s aboveground carbon stock will be released in the burn, as well as how much will later be released by decay and how much will remain as charcoal. In this paper we examined the fate of biomass from a semideciduous tropical forest in the ""arc of deforestation,"" where clearing activity is concentrated along the southern edge of the Amazon forest. We estimated carbon content, charcoal formation and burning efficiency by direct measurements (cutting and weighing) and by line-intersect sampling (LIS) done along the axis of each plot before and after burning of felled vegetation. The total aboveground dry biomass found here (219.3 Mg ha(-1)) is lower than the values found in studies that have been done in other parts of the Amazon region. Values for burning efficiency (65%) and charcoal formation (6.0%, or 5.98 Mg C ha(-1)) were much higher than those found in past studies in tropical areas. The percentage of trunk biomass lost in burning (49%) was substantially higher than has been found in previous studies. This difference may be explained by the concentration of more stems in the smaller diameter classes and the low humidity of the fuel (the dry season was unusually long in 2007, the year of the burn). This study provides the first measurements of forest burning parameters for a group of forest types that is now undergoing rapid deforestation. The burning parameters estimated here indicate substantially higher burning efficiency than has been found in other Amazonian forest types. Quantification of burning efficiency is critical to estimates of trace-gas emissions from deforestation. (C) 2009 Elsevier B.V. All rights reserved.

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The objective of this master's thesis was to develop a process to increase the value of residual fungal biomass as an animal feed. The increase in value is achieved by enriching the protein content in the biomass and potentially isolating other valuable fractions for productisation. In the literature part of this thesis the composition of fungal biomass and fungal cell wall and the factors affecting them during cultivation are presented. The possible processing options are also presented and evaluated. The soy protein and single cell protein product manufacturing processes are used as examples due to the lack of fungal biomass fractionation processes found in published literature. The second part of this thesis was performed by making laboratory experiments on the developed process, which consisted of acid hydrolysis with subsequent ethanol extraction. Chitin was precipitated from the acid hydrolysate filtrate. The experiments were conducted with three different hydrolysis temperatures and three different acid concentrations. The optimal hydrolysis conditions were 60 °C with 10 %-vol acid concentration. Optimal conditions in hydrolysis resulted in 30 % increase in protein content in the final biomass. The conceptual process was modelled to scale of 10 000 t/a biomass feed. The mass and energy balances were based on the laboratory experiments. Economic calculations were performed to determine the maximal capital expense while achieving 10 % internal rate of return for the investment. For the basic case the capital expense threshold was 25.8 M€. Four optional cases and parameter sensitivity analysis were performed to determine the effects of changes in the process. The chitin sales had the greatest impact of the individual parameters.

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El objetivo principal es la evaluación de la biomasa como recurso energético renovable en Cataluña. Su alcance requiere el estudio de diversas temáticas, desarrolladas en los doce capítulos que componen el documento.El Capítulo 1 describe los objetivos de la tesis. El Capítulo 2 describe los motivos que justifican la valorización energética del recurso biomasa. El Capítulo 3 presenta la metodología general utilizada. El Capítulo 4 realiza un análisis multicriterio del aprovechamiento energético de biomasa forestal. El Capítulo 5 cuantifica la biomasa disponible para usos energéticos en Cataluña. Los Capítulos 6, 7, 8 y 9 analizan las tecnologías y la viabilidad de la producción de energía con colza y chopo. El Capítulo 10 caracteriza físico-químicamente la biomasa de colza como combustible complementario al actual uso del grano para biodiesel. El Capítulo 11 evalua el uso de cultivos para la producción de productos químicos. El Capítulo 12 resume las Conclusiones generales.

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The introduction of nitrogen fixing species (NFS) in fast-growing tree plantations is an alternative option to reduce fertilizer inputs. However, the success of mixed-species plantations depends on the balance between positive interactions among species (resulting from facilitation and/or complementarity) and the negative effects of interspecific competition.Using a carbon budget approach and coupling measurements of standing biomass, aboveground litterfall and soil CO2 efflux, we assessed the influence of replacing half of eucalypt trees by Acacia mangium on total belowground carbon flux (TBCF), net primary production (NPP) and its partitioning between above- and belowground growth at two tropical sites in Brazil (Itatinga) and in Congo (Kissoko) exhibiting contrasting climates, edaphic conditions and wood productions.Annual soil CO2 efflux (FS) was significantly lower in the acacia monocultures than in eucalypt monocultures and mixed-species stands at both sites. Annual FS was significantly lower at Itatinga compared to Kissoko for all stands while TBCF was significantly lower in the eucalypt stands only. In the eucalypt monocultures we found a significantly lower aboveground NPP (ANPP) and wood production (wood NPP) at Kissoko compared to Itatinga that was almost fully balanced by a significantly higher belowground NPP (BNPP), leading to similar NPP. Similarly, acacia monocultures exhibited significantly higher ANPP and wood NPP at Itatinga than at Kissoko. The mixed-species stands exhibited a significantly lower wood NPP and ANPP than the eucalypt monocultures at the Brazilian site while NPP of the mixture was not significantly different than the average NPP of the two monocultures. At the Congolese site, NPP of the mixture was significantly higher than the average NPP of the two monocultures. NPP was similar in the mixed-species stand and the eucalypt monoculture with a significantly lower partitioning of NPP to belowground production, leading to a one third higher wood biomass at harvest in the mixed-species stand.A positive effect of growing eucalypts with the nitrogen fixing acacia trees on stand wood production occurred at Kissoko but not at Itatinga. Mixed-species plantations with NFS can be advocated at sites where the productive gains resulting from nitrogen fixation are not compromised by other resource limitations. © 2012 Elsevier B.V.

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Scientific research in forest production technology area search techniques that increase production per unit area, with high economic viability and reducing environmental impacts. When dealing with forest plantations, studies are needed in the production of biomass and its nutrient content, and these are data parameters for planning the environmental implications of different intensities of forest harvesting. Given the above, this study aimed to elucidate the production and export of biomass and nutrients for two species of the genus Eucalyptus (E. grandis and E. urophylla) grown in the southwestern region of Parana. For this, it was evaluated: the stock of biomass and nutrients in eucalyptus (wood, bark, branches and leaves) at 60 months of age; the export rate of nutrients; the calorific value and economic viability. The biomass and the largest eucalyptus nutrient stocks are predominantly allocated to the stem (wood + bark). The components of biomass showed different chemical compositions, generally being higher in the leaves and bark and lower in wood and branches components. As for the calorific value, the leaves had its calorific value statistically superior than the other fractions, followed by branches, wood and bark. The organic carbon content (C.O.) is directly connected to the calorific value, and the calorific value increases as its content increase. The wood had the highest nutrient use efficiency values, something highly desirable and of great interest to forestry. The leaves showed smaller nutrient utilization efficiency values, with the exception of Ca and Mg that were smaller in the bark, indicating the importance of maintaining these components in the soil after harvest. The wood fraction presents the biomass lower cost when considering the replacement of nutrients exported by its biomass. On the other hand, the leaf fraction showed NPK higher cost of replacement.

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A gasificação de biomassa permite a produção de um gás combustível com capacidade para reduzir o consumo de combustíveis fósseis. Contudo, para promover a utilização deste processo a nível industrial é necessário ultrapassar diversas limitações e elaborar tecnologias de gasificação que sejam mais rentáveis e eficientes. No presente trabalho efetuou-se a gasificação direta com ar, num reator auto-térmico com um leito fluidizado borbulhante, de diferentes tipos de biomassa provenientes da floresta portuguesa, nomeadamente pellets de madeira e diferentes tipos de biomassa florestal residual derivada de eucalipto. A investigação foi realizada numa instalação à escala piloto localizada no Departamento de Ambiente e Ordenamento da Universidade de Aveiro. A infraestrutura foi desenvolvida de modo a permitir o estudo do processo de gasificação de biomassa. O reator utilizado apresenta 3 metros de altura, consistindo a câmara de gasificação em 2.25 metros, 0.25 metros de diâmetro interno e uma potência entre 40 e 70 kWth. O leito é composto por areia (partículas com granulometria entre os 355 e 1000 µm) e tem uma altura de 0.23 m. A infraestrutura experimental oferece condições para efetuar a gasificação de biomassa, determinar a composição do gás produzido em termos de CO, CO2, H2, N2, CH4 e C2H4 e efetuar a sua combustão num queimador localizado a jusante do reator. O leito fluidizado operou com temperaturas médias entre os 700 e 850ºC. Para as razões de equivalência estabelecidas, entre 0.17 e 0.36, o gás seco apresentou uma composição que, em termos volumétricos e em função das condições operatórias, variou entre 14.0 a 21.4% CO, 14.2 a 17.5% CO2, 3.6 a 5.8% CH4, 1.3 a 2.4% C2H4, 2.0 a 10.2% H2 e 48.9 a 61.1% N2. A maior concentração de CO, CH4 e C2H4 foi observada durante a gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.17, contudo, a maior concentração de H2 foi obtida na gasificação de pellets de madeira com razão de equivalência de 0.25. Tendo em conta a composição gasosa, o poder calorífico inferior do gás seco encontrou-se entre 4.4 e 6.9 MJ/Nm3 e os valores mais elevados foram observados durante os processos de gasificação efetuados com menor razão de equivalência. A produção específica de gás variou entre 1.2 e 2.2 Nm3/kg biomassa bs, a eficiência do gás arrefecido entre 41.1 e 62.6% e a eficiência de conversão de carbono entre 60.0 e 87.5%, encontrando-se na gama dos valores reportados na literatura. A melhor condição, em termos da eficiência de gás arrefecido, consistiu na gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.25, e em termos da produção específica de gás seco e eficiência de conversão de carbono, na gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.35. Contudo, o gás com maior poder calorífico inferior foi obtido durante a gasificação de biomassa residual florestal derivada de eucalipto com razão de equivalência de 0.17. O reator demonstrou adequabilidade na gasificação de diferentes tipos de biomassa e foram observadas condições estáveis de operação, tanto em termos de temperatura como da composição do gás produzido. Geralmente, o gás apresentou propriedades combustíveis apropriadas para ser comburido de forma contínua e estável pelo queimador de gás, sem ser necessária uma fonte de ignição permanente ou a utilização de um combustível auxiliar.

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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

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This work presents a mathematical model for helping mills choose sugarcane varieties for planting. It maximizes crop residual biomass energy balance by considering the difference between generated and consumed energy in the process of transferring this biomass from the field to the processing center; it takes into account enterprise demand restrictions and cane planting area. For this full zero-one linear programming techniques were proposed. The model is viable for choosing sugarcane varieties that would benefit sugarcane production and industrial systems, by reducing crop residue and increasing final energy production. (c) 2006 Published by Elsevier Ltd.

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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)