Efeito do processo de auto-hidrólise e caracterização química da madeira de Eucalyptus grandis x Eucalyptus urophylla e Eucalyptus grandis

Pós-graduação em Ciência Florestal - FCA

Estudo da utilização de serragem de madeira como adsorvente para o tratamento de efluentes têxteis

The Brazilian textile industry has been a highlight in the global economy. Connected with this high economic performance there is the water consumption and the generation of great volumes of wastewater which present high concentrations of dyes and chemical substances. One of the main techniques used in the treatment of textile effluents is adsorption, which has the activated carbon as the main adsorbent. Recently, studies have been developed to find alternative materials to activated carbon and exhibiting good adsorption capacity of dyes. The aim of this work is to study the potential of sawdust as adsorbent of low cost to remove the dye Direct Green 26. The results of this type of dye removal were obtained through the study of adsorption isotherms obtained by spectrophotometry in the UV-visible region analyzed by the Langmuir model. Finally, a comparison was made of these results with those of other adsorbents. Results showed that the average removal of dye, using sawdust, was 78.8% for an initial concentration of 500mg / L and the maximum adsorption capacity of 119mg / g. These results demonstrate the great potential of sawdust as an adsorbent for the dye Direct Green 26.

Uso de resíduos madeireiros da Amazônia brasileira no cultivo in vitro de Lentinus strigosus

Lentinus strigosus (Schwein.) Fr. is an exploitable edible mushroom occurring in the Brazilian Amazon, being part of a huge diversity of edible mushrooms which are little grown. The use of regional waste is recommended to reduce production costs of any kind of edible mushroom. Thus, the mycelial growth of L. strigosus in culture media based on regional wood waste extract by using substrates based on Protium puncticulatum, Cariniana micrantha and Caryocar glabum sawdust, supplemented with 20% of wheat bran (Triticum aestivum), corn bran (Zea sp.) or rice bran (Oryza sp.) was observed. Eucalyptus (Eucaliptus sp.) sawdust was used for comparison with the other wood wastes because it is commonly used in the cultivation of edible fungi. The experimental design employed was totally randomized, in 4 x 3 factorial scheme (sawdust x bran), adding up 12 treatments with 5 repetitions, being that each repetition corresponded to a Petri dish, totalizing 60 dishes, incubated at 35 ºC. The diameter of the colony was daily evaluated until the fungus reached the borders of the Petri dish in one of the treatments. After that period, the media based on P. puncticulatum sawdust obtained thebest results of mycelial growth, showing potential to be used as an alternative residuein a future production of L. strigosus in the state of Amazonas.

Cultivation and bromatological analysis of the medicinal mushroom Ganoderma lucidum (Curt.: Fr.) P. Karst cultivated in agricultural waste

The objective of the study was to evaluate the production of two strains of Ganoderma lucidum on agricultural waste and carry out bromatological analyses of the basidiomata obtained from the cultivation. The experiment was carried out at the Mushroom Module at the School of Agronomic Sciences of the São Paulo State University (FCA/UNESP - Botucatu, SP, Brazil) and two strains were used (GLM-09/01 and GLM-10/02) which were cultivated on waste, oat straw, bean straw, brachiaria grass straw, Tifton grass straw and eucalyptus sawdust under two situations: with (20%) and without (0%) supplementation with wheat bran. All the waste was taken from dumps of agricultural activities in Botucatu-SP. Both treatments were carried out in 10 repetitions, totaling 200 packages. The mushrooms cultivation took 90 days. Next, the biological efficiency of the treatments and the bromatological analysis of the basidiomata were evaluated. The biological efficiency (BE) values (%) varied from 0.0 to 6.7%. In the mushroom bromatological analyses, the results ranged from 8.7 to 13.7%, from 2.0 to 6.7%, from 0.83 to 1.79% and from 38.8 to 54.5%, for total protein, ethereal extract, ash and crude fiber, respectively. Thus, we conclude that the substrates which presented the greater yield were the brachiaria straw, 20% in both strains tested (GLM-09/01 and GLM-10/02) and the bean straw, 20% in the strain GLM-10/02. The mushrooms showed high levels of ethereal extract, fibers and ashes and a low level of proteins.

Cinética micelial dos fungos comestíveis Pleurotus ostreatus e Lentinula edodes em resíduos lignocelulósicos

The objective of this work was to evaluate the mycelial growth of 2 edible fungi (Pleurotus ostreatus and Lentinula edodes) in 6 culture media [(malt-agar, sawdustdextrose-agar-marupá (SDA-MA), sawdust-dextrose-agar-cajuí (SDA-CA), sawdust-dextrose-agaraçaí (SDA-AÇA), sawdust-dextrose-agar-banana 50% (BAN 50%) and sawdust-dextrose-agar-banana 100% (BAN 100%)], in Petri dishes. The experimental design was totally randomized, in a 6x2 factorial scheme. Each treatment consisted of six repetitions in 1 Petri dish, totaling 72 experimental units. It was verified that P. ostreatus presented better mycelial development (81.00; 64.66; 81.00; 50.16 and 33.33mm for SDA-MA, SDA-CA, SDA-AÇA, BAN 50% and BAN 100%, respectively) than L. edodes (32.00; 31.66; 27.66; 37.33 and 21.83mm for SDA-MA, SDA-CA, SDA-AÇA, BAN 50% and BAN 100%, respectively). It was also verified that there was no advantage for L. edodes in relation to mycelial growth, when media based on residues were used, compared to malt-agar medium (control), which obtained the best performance (62.17mm). As for P. ostreatus, SDA-MA and SDA-AÇA medium presented the highest growth averages (81 mm), representing a growth increase of 34% in relation to the control medium (malt-agar), whose growth average was 60.33mm. Thus, the residues tested present potential to be used in fungiculture, especially for the cultivation of P. ostreatus.

Clonagem do pessegueiro 'Aurora-1' e de portaenxertos de umezeiro

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Efeitos da estabulação sobre o trato respiratório de equinos em dois tipos diferentes de camas e a pasto

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

O valor econômico da extração manejada de madeira no baixo Amazonas, estado do Pará

O objetivo deste trabalho foi estimar o valor econômico e a margem de comercialização da madeira em tora oriunda de áreas manejadas. Essa cadeia, além de produzir margem positiva, os valores são relativamente superiores aos gerados nas atividades que concorrem para o desmatamento na Amazônia para se estabelecerem. Adicionalmente, determinou-se o coeficiente médio de desdobramento de 37,3% (2,68 m³ de madeira em tora para cada 1,0 m³ de madeira serrada), o qual revelou baixo grau tecnológico das empresas. O valor econômico médio da extração e comercialização da madeira em pé no mercado local foi de R$ 23,48/m³, tendo um valor mínimo de R$ 9,06/m³ para as espécies da categoria C4 (madeira branca) e um máximo de R$ 55,63/m³ para as espécies da categoria C1 (madeira especial). Assim, para um fluxo de 30 anos e extração de 25 m³/ha nos planos de manejo das áreas de concessão florestal do Estado do Pará, gera-se um valor médio de R$ 587,00/ha, ou R$ 19,56/ha/ano. No fluxo de 30 anos, esse resultado é relativamente superior ao gerado pelas atividades de pecuária extensiva (em torno de R$ 180,00/ha) e das lavouras de grãos (em torno dos R$ 420,00/ha), principais responsáveis pelo desmatamento da Amazônia. Também, apresenta maior rentabilidade do que o reflorestamento com paricá, que gera R$ 192,26/ha. A margem de comercialização indicou que a sociedade tende a se apropriar de 14,3% do valor econômico gerado na cadeia da madeira oriunda dos contratos de concessão florestal.

THERMOSTABILITY OF XYLANOLYTIC ENZYMES PRODUCED BY LENTINULA EDODES UFV70

Xylanolytic enzymes produced by Lentinula edodes UFV70, cultivated in eucalyptus sawdust/rice bran medium, were stable at 50, 60 and 65 degrees C for 21 hours, losing only 15-25% activity. Fungus incubation at 50 degrees C for 12 hours and at 65 degrees C for 24 hours increased the amount of xylose produced.

Thermostability of xylanolytic enzymes produced by Lentinula edodes UFV70

Xylanolytic enzymes produced by Lentinula edodes UFV70, cultivated in eucalyptus sawdust/rice bran medium, were stable at 50, 60 and 65ºC for 21 hours, losing only 15-25% activity. Fungus incubation at 50ºC for 12 hours and at 65ºC for 24 hours increased the amount of xylose produced.

Preferencia del conejo silvestre Oryctolagus cuniculus por diferentes tipos de sustratos

Asignatura. Etología de los recursos pesqueros (Licenciatura Ciencias del mar)

Produzione di bioetanolo da scarti lignocellulosici della canna da zucchero: condizioni di saccarificazione e fermentazione simultanee (SSF) e aspetti ambientali del processo

Il presente studio ha avuto l’obiettivo di indagare la produzione di bioetanolo di seconda generazione a partire dagli scarti lignocellulosici della canna da zucchero (bagassa), facendo riscorso al processo enzimatico. L’attività di ricerca è stata svolta presso il Dipartimento di Ingegneria Chimica dell’Università di Lund (Svezia) all’interno di rapporti scambio con l’Università di Bologna. Il principale scopo è consistito nel valutare la produzione di etanolo in funzione delle condizioni operative con cui è stata condotta la saccarificazione e fermentazione enzimatica (SSF) della bagassa, materia prima che è stata sottoposta al pretrattamento di Steam Explosion (STEX) con aggiunta di SO2 come catalizzatore acido. Successivamente, i dati ottenuti in laboratorio dalla SSF sono stati utilizzati per implementare, in ambiente AspenPlus®, il flowsheet di un impianto che simula tutti gli aspetti della produzione di etanolo, al fine di studiarne il rendimento energetico dell’intero processo. La produzione di combustibili alternativi alle fonti fossili oggigiorno riveste primaria importanza sia nella limitazione dell’effetto serra sia nel minimizzare gli effetti di shock geopolitici sulle forniture strategiche di un Paese. Il settore dei trasporti in continua crescita, consuma nei paesi industrializzati circa un terzo del fabbisogno di fonti fossili. In questo contesto la produzione di bioetanolo può portare benefici per sia per l’ambiente che per l’economia qualora valutazioni del ciclo di vita del combustibile ne certifichino l’efficacia energetica e il potenziale di mitigazione dell’effetto serra. Numerosi studi mettono in risalto i pregi ambientali del bioetanolo, tuttavia è opportuno fare distinzioni sul processo di produzione e sul materiale di partenza utilizzato per comprendere appieno le reali potenzialità del sistema well-to-wheel del biocombustibile. Il bioetanolo di prima generazione ottenuto dalla trasformazione dell’amido (mais) e delle melasse (barbabietola e canna da zucchero) ha mostrato diversi svantaggi: primo, per via della competizione tra l’industria alimentare e dei biocarburanti, in secondo luogo poiché le sole piantagioni non hanno la potenzialità di soddisfare domande crescenti di bioetanolo. In aggiunta sono state mostrate forti perplessità in merito alla efficienza energetica e del ciclo di vita del bioetanolo da mais, da cui si ottiene quasi la metà della produzione di mondiale di etanolo (27 G litri/anno). L’utilizzo di materiali lignocellulosici come scarti agricolturali e dell’industria forestale, rifiuti urbani, softwood e hardwood, al contrario delle precedenti colture, non presentano gli svantaggi sopra menzionati e per tale motivo il bioetanolo prodotto dalla lignocellulosa viene denominato di seconda generazione. Tuttavia i metodi per produrlo risultano più complessi rispetto ai precedenti per via della difficoltà di rendere biodisponibili gli zuccheri contenuti nella lignocellulosa; per tale motivo è richiesto sia un pretrattamento che l’idrolisi enzimatica. La bagassa è un substrato ottimale per la produzione di bioetanolo di seconda generazione in quanto è disponibile in grandi quantità e ha già mostrato buone rese in etanolo se sottoposta a SSF. La bagassa tal quale è stata inizialmente essiccata all’aria e il contenuto d’acqua corretto al 60%; successivamente è stata posta a contatto per 30 minuti col catalizzatore acido SO2 (2%), al termine dei quali è stata pretrattata nel reattore STEX (10L, 200°C e 5 minuti) in 6 lotti da 1.638kg su peso umido. Lo slurry ottenuto è stato sottoposto a SSF batch (35°C e pH 5) utilizzando enzimi cellulolitici per l’idrolisi e lievito di birra ordinario (Saccharomyces cerevisiae) come consorzio microbico per la fermentazione. Un obiettivo della indagine è stato studiare il rendimento della SSF variando il medium di nutrienti, la concentrazione dei solidi (WIS 5%, 7.5%, 10%) e il carico di zuccheri. Dai risultati è emersa sia una buona attività enzimatica di depolimerizzazione della cellulosa che un elevato rendimento di fermentazione, anche per via della bassa concentrazione di inibitori prodotti nello stadio di pretrattamento come acido acetico, furfuraldeide e HMF. Tuttavia la concentrazione di etanolo raggiunta non è stata valutata sufficientemente alta per condurre a scala pilota un eventuale distillazione con bassi costi energetici. Pertanto, sono stati condotti ulteriori esperimenti SSF batch con addizione di melassa da barbabietola (Beta vulgaris), studiandone preventivamente i rendimenti attraverso fermentazioni alle stesse condizioni della SSF. I risultati ottenuti hanno suggerito che con ulteriori accorgimenti si potranno raggiungere gli obiettivi preposti. E’ stato inoltre indagato il rendimento energetico del processo di produzione di bioetanolo mediante SSF di bagassa con aggiunta di melassa in funzione delle variabili più significative. Per la modellazione si è fatto ricorso al software AspenPlus®, conducendo l’analisi di sensitività del mix energetico in uscita dall’impianto al variare del rendimento di SSF e dell’addizione di saccarosio. Dalle simulazioni è emerso che, al netto del fabbisogno entalpico di autosostentamento, l’efficienza energetica del processo varia tra 0.20 e 0.53 a seconda delle condizioni; inoltre, è stata costruita la curva dei costi energetici di distillazione per litro di etanolo prodotto in funzione delle concentrazioni di etanolo in uscita dalla fermentazione. Infine sono già stati individuati fattori su cui è possibile agire per ottenere ulteriori miglioramenti sia in laboratorio che nella modellazione di processo e, di conseguenza, produrre con alta efficienza energetica bioetanolo ad elevato potenziale di mitigazione dell’effetto serra.

Biomass Gasification - Process analysis and dimensioning aspects for downdraft units and gas cleaning lines

In such territories where food production is mostly scattered in several small / medium size or even domestic farms, a lot of heterogeneous residues are produced yearly, since farmers usually carry out different activities in their properties. The amount and composition of farm residues, therefore, widely change during year, according to the single production process periodically achieved. Coupling high efficiency micro-cogeneration energy units with easy handling biomass conversion equipments, suitable to treat different materials, would provide many important advantages to the farmers and to the community as well, so that the increase in feedstock flexibility of gasification units is nowadays seen as a further paramount step towards their wide spreading in rural areas and as a real necessity for their utilization at small scale. Two main research topics were thought to be of main concern at this purpose, and they were therefore discussed in this work: the investigation of fuels properties impact on gasification process development and the technical feasibility of small scale gasification units integration with cogeneration systems. According to these two main aspects, the present work was thus divided in two main parts. The first one is focused on the biomass gasification process, that was investigated in its theoretical aspects and then analytically modelled in order to simulate thermo-chemical conversion of different biomass fuels, such as wood (park waste wood and softwood), wheat straw, sewage sludge and refuse derived fuels. The main idea is to correlate the results of reactor design procedures with the physical properties of biomasses and the corresponding working conditions of gasifiers (temperature profile, above all), in order to point out the main differences which prevent the use of the same conversion unit for different materials. At this scope, a gasification kinetic free model was initially developed in Excel sheets, considering different values of air to biomass ratio and the downdraft gasification technology as particular examined application. The differences in syngas production and working conditions (process temperatures, above all) among the considered fuels were tried to be connected to some biomass properties, such elementary composition, ash and water contents. The novelty of this analytical approach was the use of kinetic constants ratio in order to determine oxygen distribution among the different oxidation reactions (regarding volatile matter only) while equilibrium of water gas shift reaction was considered in gasification zone, by which the energy and mass balances involved in the process algorithm were linked together, as well. Moreover, the main advantage of this analytical tool is the easiness by which the input data corresponding to the particular biomass materials can be inserted into the model, so that a rapid evaluation on their own thermo-chemical conversion properties is possible to be obtained, mainly based on their chemical composition A good conformity of the model results with the other literature and experimental data was detected for almost all the considered materials (except for refuse derived fuels, because of their unfitting chemical composition with the model assumptions). Successively, a dimensioning procedure for open core downdraft gasifiers was set up, by the analysis on the fundamental thermo-physical and thermo-chemical mechanisms which are supposed to regulate the main solid conversion steps involved in the gasification process. Gasification units were schematically subdivided in four reaction zones, respectively corresponding to biomass heating, solids drying, pyrolysis and char gasification processes, and the time required for the full development of each of these steps was correlated to the kinetics rates (for pyrolysis and char gasification processes only) and to the heat and mass transfer phenomena from gas to solid phase. On the basis of this analysis and according to the kinetic free model results and biomass physical properties (particles size, above all) it was achieved that for all the considered materials char gasification step is kinetically limited and therefore temperature is the main working parameter controlling this step. Solids drying is mainly regulated by heat transfer from bulk gas to the inner layers of particles and the corresponding time especially depends on particle size. Biomass heating is almost totally achieved by the radiative heat transfer from the hot walls of reactor to the bed of material. For pyrolysis, instead, working temperature, particles size and the same nature of biomass (through its own pyrolysis heat) have all comparable weights on the process development, so that the corresponding time can be differently depending on one of these factors according to the particular fuel is gasified and the particular conditions are established inside the gasifier. The same analysis also led to the estimation of reaction zone volumes for each biomass fuel, so as a comparison among the dimensions of the differently fed gasification units was finally accomplished. Each biomass material showed a different volumes distribution, so that any dimensioned gasification unit does not seem to be suitable for more than one biomass species. Nevertheless, since reactors diameters were found out quite similar for all the examined materials, it could be envisaged to design a single units for all of them by adopting the largest diameter and by combining together the maximum heights of each reaction zone, as they were calculated for the different biomasses. A total height of gasifier as around 2400mm would be obtained in this case. Besides, by arranging air injecting nozzles at different levels along the reactor, gasification zone could be properly set up according to the particular material is in turn gasified. Finally, since gasification and pyrolysis times were found to considerably change according to even short temperature variations, it could be also envisaged to regulate air feeding rate for each gasified material (which process temperatures depend on), so as the available reactor volumes would be suitable for the complete development of solid conversion in each case, without even changing fluid dynamics behaviour of the unit as well as air/biomass ratio in noticeable measure. The second part of this work dealt with the gas cleaning systems to be adopted downstream the gasifiers in order to run high efficiency CHP units (i.e. internal engines and micro-turbines). Especially in the case multi–fuel gasifiers are assumed to be used, weightier gas cleaning lines need to be envisaged in order to reach the standard gas quality degree required to fuel cogeneration units. Indeed, as the more heterogeneous feed to the gasification unit, several contaminant species can simultaneously be present in the exit gas stream and, as a consequence, suitable gas cleaning systems have to be designed. In this work, an overall study on gas cleaning lines assessment is carried out. Differently from the other research efforts carried out in the same field, the main scope is to define general arrangements for gas cleaning lines suitable to remove several contaminants from the gas stream, independently on the feedstock material and the energy plant size The gas contaminant species taken into account in this analysis were: particulate, tars, sulphur (in H2S form), alkali metals, nitrogen (in NH3 form) and acid gases (in HCl form). For each of these species, alternative cleaning devices were designed according to three different plant sizes, respectively corresponding with 8Nm3/h, 125Nm3/h and 350Nm3/h gas flows. Their performances were examined on the basis of their optimal working conditions (efficiency, temperature and pressure drops, above all) and their own consumption of energy and materials. Successively, the designed units were combined together in different overall gas cleaning line arrangements, paths, by following some technical constraints which were mainly determined from the same performance analysis on the cleaning units and from the presumable synergic effects by contaminants on the right working of some of them (filters clogging, catalysts deactivation, etc.). One of the main issues to be stated in paths design accomplishment was the tars removal from the gas stream, preventing filters plugging and/or line pipes clogging At this scope, a catalytic tars cracking unit was envisaged as the only solution to be adopted, and, therefore, a catalytic material which is able to work at relatively low temperatures was chosen. Nevertheless, a rapid drop in tars cracking efficiency was also estimated for this same material, so that an high frequency of catalysts regeneration and a consequent relevant air consumption for this operation were calculated in all of the cases. Other difficulties had to be overcome in the abatement of alkali metals, which condense at temperatures lower than tars, but they also need to be removed in the first sections of gas cleaning line in order to avoid corrosion of materials. In this case a dry scrubber technology was envisaged, by using the same fine particles filter units and by choosing for them corrosion resistant materials, like ceramic ones. Besides these two solutions which seem to be unavoidable in gas cleaning line design, high temperature gas cleaning lines were not possible to be achieved for the two larger plant sizes, as well. Indeed, as the use of temperature control devices was precluded in the adopted design procedure, ammonia partial oxidation units (as the only considered methods for the abatement of ammonia at high temperature) were not suitable for the large scale units, because of the high increase of reactors temperature by the exothermic reactions involved in the process. In spite of these limitations, yet, overall arrangements for each considered plant size were finally designed, so that the possibility to clean the gas up to the required standard degree was technically demonstrated, even in the case several contaminants are simultaneously present in the gas stream. Moreover, all the possible paths defined for the different plant sizes were compared each others on the basis of some defined operational parameters, among which total pressure drops, total energy losses, number of units and secondary materials consumption. On the basis of this analysis, dry gas cleaning methods proved preferable to the ones including water scrubber technology in al of the cases, especially because of the high water consumption provided by water scrubber units in ammonia adsorption process. This result is yet connected to the possibility to use activated carbon units for ammonia removal and Nahcolite adsorber for chloride acid. The very high efficiency of this latter material is also remarkable. Finally, as an estimation of the overall energy loss pertaining the gas cleaning process, the total enthalpy losses estimated for the three plant sizes were compared with the respective gas streams energy contents, these latter obtained on the basis of low heating value of gas only. This overall study on gas cleaning systems is thus proposed as an analytical tool by which different gas cleaning line configurations can be evaluated, according to the particular practical application they are adopted for and the size of cogeneration unit they are connected to.

Einfluss der Habitatfragmentierung durch Überflutung auf Laufkäferpopulationen (Coleoptera; Carabidae)

Innerhalb dieser Dissertation wurde zwischen den Jahren 2002 und 2005 mit Hilfe von Barberfallen die Laufkäferfauna der Auwälder am nördlichen Oberrhein zwischen Mainz und Bingen erfasst. Dabei dienten verschiedene Rheininseln und ufernahe Festlandgebiete als Probeflächen. Fünf der typischen Bewohner dieser Flächen (Agonum afrum, Nebria brevicollis, Oxypselaphus obscurus, Platynus assimilis, Pterostichus anthracinus) dienten weiterhin als Modellarten für die Untersuchung der genetischen Diversität zwischen den einzelnen Populationen mittels RAPD-Analysen. Alles in allem konnten im Untersuchungsgebiet über 20.000 Individuen aus 101 Carabidenarten gefangen werden. Die häufigsten Vertreter waren Platynus assimilis, Pterostichus melanarius und Agonum afrum. Hohe Diversitäts- und Dominanzindices auf allen Flächen sprechen für die Dynamik des Lebensraumes und somit die Intaktheit der untersuchten Auwälder. Einen weiteren Hinweis auf die ständig wechselnden Lebensbedingungen durch immer wiederkehrende Überflutungen zeigt das Auftreten verschiedener ökologischer Gruppen. Überall dominierten deutlich die Arten, die mit gewissen Störungen des Habitates auskommen oder durch ihr hohes Ausbreitungspotential davor fliehen können. Das sind die Imaginalüberwinterer, makropteren, hygrophilen und kleinen Spezies. Auch das Geschlechterverhältnis weist auf deutliche Anzeichen für regelmäßige Beeinträchtigungen der Flächen hin. Knapp die Hälfte der beobachteten Arten im Untersuchungsgebiet steht auf einer der Roten Listen von Deutschland, Rheinland-Pfalz oder Hessen. Somit besteht für das gesamte Gebiet ein hoher Schutzbedarf. Das Hauptaugenmerk dieser Arbeit lag bei den Einflüssen der Hochwasserstände auf die Artenzusammensetzungen und die genetischen Diversitäten der Laufkäferpopulationen. Deshalb untersuchte man auch die Wirkung derjenigen Faktoren, die ihrerseits unmittelbar von den Extremwasserständen beeinflusst werden. Hier sind vor allem der Auentyp (Weichholz/Hartholz) und die Lage der Flächen auf Insel oder Festland zu nennen, die die deutlichsten Unterschiede in Artendiversität und Genetik der einzelnen Populationen zeigten. Aber auch weitere Faktoren, wie Wasserstandsdynamik, Auwaldbreite, Entfernung vom Fluss und Lage zum Damm weisen Zusammenhänge mit bestimmten ökologischen Gruppen auf. Lediglich die Habitatgröße scheint keinen Einfluss auf die Diversitäten zu nehmen. Abschließend konnten auch für das Jahr 2003, in dem extrem heiße und trockene Bedingungen herrschten, negative Effekte auf die Laufkäfergemeinschaften gezeigt werden.

Idrolisi diretta di cellulosa e lignocellulosa in catalisi eterogenea

This work deals with a comparison of the catalytic behavior of several heterogeneous acid catalysts in the direct hydrolysis of an untreated softwood dust. Amongst the various catalysts investigated, some were characterized by relatively high yield to monosaccharides, such as a Zirconium phosphate and the reference Amberlyst 15. Conversely, some catalyst types, ie, Sn/W mixed oxide and Zirconia-grafted trifluoromethanesulphonic acid, were selective into glucose, since sugars derived from hemicellulose dissolution and hydrolysis were rapidly degraded. A detailed analysis of the reactivity of Zr/P/O was pursued, in the hydrolysis of both untreated and ball-milled microcrystalline cellulose; at 150°C and 3h reaction time, the catalyst gave high selectivity to glucose, with negligible formation of 5-hydroxymethylfurfural, and moderate cellulose conversion. After ball-milling of the cellulose, a remarkable increase of conversion was achieved, still with a high selectivity to glucose and very low formation of degradation compounds. The catalyst showed high affinity for β-1,4-glucans, as demonstrated by the activity in cellobiose hydrolysis into glucose.