Aproveitamento de bagaço em usinas de álcool e açúcar-venda, queima ou hidrólise

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Pequenas cidades na região de Catanduva - SP: papéis urbanos, reprodução social e produção de moradias

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

Otimização multiobjetivo no planejamento agregado da produção e na cogeração de energia elétrica de usina do setor sucroenergético

Pós-graduação em Engenharia Mecânica - FEG

Análise termodinâmica, termoeconômica e econômica de uma usina sucroalcooleira para diferentes mix de produção

Pós-graduação em Engenharia Mecânica - FEIS

Acidentes graves fatais no trabalho de corte mecanizado de cana-de-açucar: o olhar através do método mapa

Pós-graduação em Saúde Coletiva - FMB

Experiência de vigilância no setor canavieiro: desafios para interromper a maratona perigosa dos canaviais

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

Controle quimioterápico da mosca Stomoxys calcitrans (Insecta: Muscidae)

Pós-graduação em Medicina Veterinária - FCAV

Os efeitos socioespaciais da expansão canavieira na bacia hidrográfica do rio Ivinhema no Estado de Mato Grosso do Sul

Pós-graduação em Geografia - FCT

Desenvolvimento de modelo matemático de otimização logística para o transporte multimodal de safras agrícolas pelo corredor centro-oeste

Este artigo apresenta um modelo matemático de otimização logística para o transporte multimodal de safras agrícolas pelo corredor Centro-Oeste. Tal ferramenta foi desenvolvida no contexto de três amplos projetos de pesquisa financiados pela FINEP e executados por um grupo de universidades. O modelo, conhecido genericamente como Modelo de fluxo de Custo Mínimo Multiproduto, considera a otimização de fluxos em rede, para os produtos açúcar, álcool, milho, soja, óleo de soja, farelo de soja e trigo. O modelo proposto para estimativa dos fluxos inter-regionais mostrou-se uma ferramenta factível para fins de avaliação do potencial de utilização da multimodalidade. A análise destes resultados gera importantes subsídios para a seleção dos locais com potencial para instalação de mecanismos e equipamentos de transferência de cargas, além de auxiliar no dimensionamento dessas infraestruturas. Também é um resultado importante do ferramental desenvolvido a identificação das zonas de cargas que apresentam potencial captável pelas ferrovias, hidrovias e dutovias, ou seja, possibilita a identificação das regiões que revelam potencial para uso da multimodalidade.

Mikrobiologie der Fermentation in NawaRo-Biogasanlagen unter besonderer Berücksichtigung des Abbaus von Propionsäure

In NawaRo-Biogasanlagen (BGA) kann es durch das Angebot an leicht fermentierbaren Kohlenstoff¬quel¬len zu einer bakteriell bedingten Übersäuerung durch unerwünschte kurzkettige Fettsäuren kommen. Häufiger kommt es zur Akkumulation von Propionsäure. Methanogene Archaea können bei niedrigen pH-Werten nicht mehr wachsen. Somit kann der gesamte Prozess der mikrobiellen Bildung von Biogas zum Erliegen kom¬men, was für die Biogasbetreiber zu erheblichen finanziellen Verlusten führt. Das Ziel dieser Disserta¬tion war die Aufklärung der anaeroben bakteriellen Population, die in Biogasanlagen Propionsäure ab¬bauen kann. Aus Propionat entsteht dabei Acetat und Wasserstoff. Da dieser anaerobe Prozess endergon verläuft, kann Propionsäure anaerob nur abgebaut werden, wenn der Wasserstoffpartialdruck niedrig ge¬halten wird. Diese Aufgabe erfüllen in Biogasanalgen methanogene Archaea. Die sog. sekundären Gärer leben somit in synthropher Kultur mit methanogenen Archaea.rnIn dieser Arbeit wurden die Mikroorganismen von Propionsäure-abbauenden Anreicherungskulturen aus vier NawaRo-BGA‘s identifiziert und ihr Substrat- und Produktspektrum analysiert. Die Anreicherungskul¬turen wurden vom Prüf- und Forschungsinstitut e. V. in Pirmasens zur Verfügung gestellt. Durch Analyse der bakteriellen 16S rDNA-Sequenzen der erhaltenen stabilen Propionsäure-abbauenden Mischkulturen wurde gezeigt, dass sich unter den Bakterien hauptsächlich Verwandte von den Clostridiales, aber auch Bacteroides sp., δ-, ε- so¬wie γ-Proteobakterien, Spirochäten, Synergistales und ungewöhnlicher Weise auch Thermotogales befanden. Aus Propionsäure-abbauenden Mischkulturen und aus Fermentern mesophiler NawaRo-Biogasanlagen wurden anaerobe Bakterien und methanogene Archaea angereichert und isoliert. Es wurden aus den Propionsäure-abbauenden Mischkulturen Stämme in Reinkultur erhalten, die entsprechend der 16S rDNA-Analyse als Clostridium sartagoforme Stamm Ap1a520 und Proteiniphilum acetatigenes Stamm Fp1a520 identifiziert wurden. Sowohl aus Fermentern und Nachgärern von drei NawaRo-BGA‘s als auch aus zwei Laborfermentern des Leibniz-Instituts für Agrartechnik in Potsdam-Bornim e.V. (ATB) wurden Reinkulturen von methanogenen Archaea erhalten. Diese konnten den Species Methanobacterium formicicum, Metha¬noculleus bourgensis, Methanosarcina barkeri, Methanosarcina mazei, Methanosarcina sp., Methanosaeta concilii und Methanomethylovorans sp. zugeordnet werden. Damit wurden in dieser Arbeit unter anderem die typischen bisher nur durch molekularbiologische Methoden identifizierten Species methanogener Ar¬chaea aus unterschiedlichen Fermentern in Reinkultur erhalten. Dabei wurde gezeigt, dass die specifically amplified polymorphic DNA-PCR (SAPD-PCR) eine geeignete Methode darstellt, Stämme der gleichen Art methanogener Archaea voneinander zu unterscheiden. Die Methanproduktion der kultivierten methanoge¬nen Archaea wurde gaschromatographisch analysiert. Es zeigte sich, dass die hydrogenotrophe Metha¬nogenese der effizientere und ergiebigere Weg zur Bildung von Methan ist. Mit der Bestimmung der Zellzahl des Isolates Methanoculleus bourgensis Stamm TAF1.1 bei gleichzeitiger Messung der Methanbildung wurde gezeigt, dass die Methanbildung nicht zwangsläufig mit dem Wachstum korreliert. Ne-ben Pflanzenfasern beinhalteten das hergestellte Reaktorfiltrat in den Kultivierungsansätzen Acetat, die essentielle Aminosäure Valin und den Zuckeralkohol Glycerol. Gezielte Misch¬kul¬turen von sekundären Gärern mit methanogenen Isolaten ergaben einen fördernden Einfluss auf diese Bak¬terien durch hydrogenotrophe Archaea. Diese Bakterien bauten Substrate ab oder bildeten Produkte, die sie unter den gegebenen Bedingungen ohne hydrogenotrophe Archaea nicht umsetzen konnten.

Manipulation of in Vivo Sorbitol Production Alters Boron Uptake and Transport in Tobacco1

Recent evidence that some species can retranslocate boron as complexes with sugar alcohols in the phloem suggests a possible mechanism for enhancing boron efficiency. We investigated the relationship between sugar alcohol (sorbitol) content, boron uptake and distribution, and translocation of foliar-applied, isotopically enriched 10B in three lines of tobacco (Nicotiana tabacum) plants differing in sorbitol production. In tobacco line S11, transformed with sorbitol-6-phosphate dehydrogenase, the production of sorbitol was accompanied by an increase in the concentration of boron in plant tissues and an increased uptake of boron compared with either tobacco line A4, transformed with antisense orientation of sorbitol-6-phosphate dehydrogenase, or wild-type tobacco (line SR1, zero-sorbitol producer). Foliar application of 10B to mature leaves was translocated to the meristematic tissues only in line S11. These results demonstrate that the concentration of the boron-complexing sugar alcohol in the plant tissue has a significant effect on boron uptake and distribution in plants, whereas the translocation of the foliar-applied 10B from the mature leaves to the meristematic tissues verifies that boron is mobile in sorbitol-producing plants (S11) as we reported previously. This suggests that selection or transgenic generation of cultivars with an increased sugar alcohol content can result in increased boron uptake, with no apparent negative effects on short-term growth.

Metabolism of d-Glycero-d-Manno-Heptitol, Volemitol, in Polyanthus. Discovery of a Novel Ketose Reductase1

Volemitol (d-glycero-d-manno-heptitol, α-sedoheptitol) is an unusual seven-carbon sugar alcohol that fulfills several important physiological functions in certain species of the genus Primula. Using the horticultural hybrid polyanthus (Primula × polyantha) as our model plant, we found that volemitol is the major nonstructural carbohydrate in leaves of all stages of development, with concentrations of up to 50 mg/g fresh weight in source leaves (about 25% of the dry weight), followed by sedoheptulose (d-altro-2-heptulose, 36 mg/g fresh weight), and sucrose (4 mg/g fresh weight). Volemitol was shown by the ethylenediaminetetraacetate-exudation technique to be a prominent phloem-mobile carbohydrate. It accounted for about 24% (mol/mol) of the phloem sap carbohydrates, surpassed only by sucrose (63%). Preliminary 14CO2 pulse-chase radiolabeling experiments showed that volemitol was a major photosynthetic product, preceded by the structurally related ketose sedoheptulose. Finally, we present evidence for a novel NADPH-dependent ketose reductase, tentatively called sedoheptulose reductase, in volemitol-containing Primula species, and propose it as responsible for the biosynthesis of volemitol in planta. Using enzyme extracts from polyanthus leaves, we determined that sedoheptulose reductase has a pH optimum between 7.0 and 8.0, a very high substrate specificity, and displays saturable concentration dependence for both sedoheptulose (apparent Km = 21 mm) and NADPH (apparent Km = 0.4 mm). Our results suggest that volemitol is important in certain Primula species as a photosynthetic product, phloem translocate, and storage carbohydrate.

Sequence analysis of a mannitol dehydrogenase cDNA from plants reveals a function for the pathogenesis-related protein ELI3.

Mannitol is the most abundant sugar alcohol in nature, occurring in bacteria, fungi, lichens, and many species of vascular plants. Celery (Apium graveolens L.), a plant that forms mannitol photosynthetically, has high photosynthetic rates thought to results from intrinsic differences in the biosynthesis of hexitols vs. sugars. Celery also exhibits high salt tolerance due to the function of mannitol as an osmoprotectant. A mannitol catabolic enzyme that oxidizes mannitol to mannose (mannitol dehydrogenase, MTD) has been identified. In celery plants, MTD activity and tissue mannitol concentration are inversely related. MTD provides the initial step by which translocated mannitol is committed to central metabolism and, by regulating mannitol pool size, is important in regulating salt tolerance at the cellular level. We have now isolated, sequenced, and characterized a Mtd cDNA from celery. Analyses showed that Mtd RNA was more abundant in cells grown on mannitol and less abundant in salt-stressed cells. A protein database search revealed that the previously described ELI3 pathogenesis-related proteins from parsley and Arabidopsis are MTDs. Treatment of celery cells with salicylic acid resulted in increased MTD activity and RNA. Increased MTD activity results in an increased ability to utilize mannitol. Among other effects, this may provide an additional source of carbon and energy for response to pathogen attack. These responses of the primary enzyme controlling mannitol pool size reflect the importance of mannitol metabolism in plant responses to divergent types of environmental stress.

A preliminary study into the environmental and economic consequences of a sugar factory depithing operation

Bagasse stockpile operations have the potential to lead to adverse environmental and social impacts. Dust releases can cause occupational health and safety concerns for factory workers and dust emissions impact on the surrounding community. Preliminary modelling showed that bagasse depithing would likely reduce the environmental risks, particularly dust emissions, associated with large scale bagasse stockpiling operations. Dust emission properties were measured and used for dispersion modelling with favourable outcomes. Modelling showed a 70% reduction in peak ground level concentrations of PM10 dust (particles with an aerodynamic diameter less than 10 µm) from operations on depithed bagasse stockpiles compared to similar operations on stockpiles of whole bagasse. However, the costs of a depithing operation at a sugar factory were estimated to be approximately $2.1 million in capital expenditure to process 100,000 t/y of bagasse and operating costs were approximately $200,000 p.a. The total capital cost for a 10,000 t/y operation was approximately $1.6 million. The cost of depithing based on a discounted cash flow analysis was $5.50 per tonne of bagasse for the 100,000 t/y scenario. This may make depithing prohibitively expensive in many situations if installed exclusively as a dust control measure.

Modelling the flow of cane constituents through the milling process of a raw sugar factory

This thesis reports on an investigation to develop an advanced and comprehensive milling process model of the raw sugar factory. Although the new model can be applied to both, the four-roller and six-roller milling units, it is primarily developed for the six-roller mills which are widely used in the Australian sugar industry. The approach taken was to gain an understanding of the previous milling process simulation model "MILSIM" developed at the University of Queensland nearly four decades ago. Although the MILSIM model was widely adopted in the Australian sugar industry for simulating the milling process it did have some incorrect assumptions. The study aimed to eliminate all the incorrect assumptions of the previous model and develop an advanced model that represents the milling process correctly and tracks the flow of other cane components in the milling process which have not been considered in the previous models. The development of the milling process model was done is three stages. Firstly, an enhanced milling unit extraction model (MILEX) was developed to access the mill performance parameters and predict the extraction performance of the milling process. New definitions for the milling performance parameters were developed and a complete milling train along with the juice screen was modelled. The MILEX model was validated with factory data and the variation in the mill performance parameters was observed and studied. Some case studies were undertaken to study the effect of fibre in juice streams, juice in cush return and imbibition% fibre on extraction performance of the milling process. It was concluded from the study that the empirical relations developed for the mill performance parameters in the MILSIM model were not applicable to the new model. New empirical relations have to be developed before the model is applied with confidence. Secondly, a soluble and insoluble solids model was developed using modelling theory and experimental data to track the flow of sucrose (pol), reducing sugars (glucose and fructose), soluble ash, true fibre and mud solids entering the milling train through the cane supply and their distribution in juice and bagasse streams.. The soluble impurities and mud solids in cane affect the performance of the milling train and further processing of juice and bagasse. New mill performance parameters were developed in the model to track the flow of cane components. The developed model is the first of its kind and provides some additional insight regarding the flow of soluble and insoluble cane components and the factors affecting their distribution in juice and bagasse. The model proved to be a good extension to the MILEX model to study the overall performance of the milling train. Thirdly, the developed models were incorporated in a proprietary software package "SysCAD’ for advanced operational efficiency and for availability in the ‘whole of factory’ model. The MILEX model was developed in SysCAD software to represent a single milling unit. Eventually the entire milling train and the juice screen were developed in SysCAD using series of different controllers and features of the software. The models developed in SysCAD can be run from macro enabled excel file and reports can be generated in excel sheets. The flexibility of the software, ease of use and other advantages are described broadly in the relevant chapter. The MILEX model is developed in static mode and dynamic mode. The application of the dynamic mode of the model is still under progress.