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.

Use of solvents and environmental friendly materials for applications in Green Chemistry

The present Thesis studies three alternative solvent groups as sustainable replacement of traditional organic solvents. Some aspects of fluorinated solvents, supercritical fluids and ionic liquids, have been analysed with a critical approach and their effective “greenness” has been evaluated from the points of view of the synthesis, the properties and the applications. In particular, the attention has been put on the environmental and human health issues, evaluating the eco-toxicity, the toxicity and the persistence, to underline that applicability and sustainability are subjects with equal importance. The “green” features of fluorous solvents and supercritical fluids are almost well-established; in particular supercritical carbon dioxide (scCO2) is probably the “greenest” solvent among the alternative solvent systems developed in the last years, enabling to combine numerous advantages both from the point of view of industrial/technological applications and eco-compatibility. In the Thesis the analysis of these two classes of alternative solvents has been mainly focused on their applicability, rather than the evaluation of their environmental impact. Specifically they have been evaluated as alternative media for non-aqueous biocatalysis. For this purpose, the hydrophobic ion pairing (HIP), which allows solubilising enzymes in apolar solvents by an ion pairing between the protein and a surfactant, has been investigated as effective enzymatic derivatisation technique to improve the catalytic activity under homogeneous conditions in non conventional media. The results showed that the complex enzyme-surfactant was much more active both in fluorous solvents and in supercritical carbon dioxide than the native form of the enzyme. Ionic liquids, especially imidazolium salts, have been proposed some years ago as “fully green” alternative solvents; however this epithet does not take into account several “brown” aspects such as their synthesis from petro-chemical starting materials, their considerable eco-toxicity, toxicity and resistance to biodegradation, and the difficulty of clearly outline applications in which ionic liquids are really more advantageous than traditional solvents. For all of these reasons in this Thesis a critical analysis of ionic liquids has been focused on three main topics: i) alternative synthesis by introducing structural moieties which could reduce the toxicity of the most known liquid salts, and by using starting materials from renewable resources; ii) on the evaluation of their environmental impact through eco-toxicological tests (Daphnia magna and Vibrio fischeri acute toxicity tests, and algal growth inhibition), toxicity tests (MTT test, AChE inhibition and LDH release tests) and fate and rate of aerobic biodegradation in soil and water; iii) and on the demonstration of their effectiveness as reaction media in organo-catalysis and as extractive solvents in the recovery of vegetable oil from terrestrial and aquatic biomass. The results about eco-toxicity tests with Daphnia magna, Vibrio fischeri and algae, and toxicity assay using cultured cell lines, clearly indicate that the difference in toxicity between alkyl and oxygenated cations relies in differences of polarity, according to the general trend of decreasing toxicity by decreasing the lipophilicity. Independently by the biological approach in fact, all the results are in agreement, showing a lower toxicity for compounds with oxygenated lateral chains than for those having purely alkyl lateral chains. These findings indicate that an appropriate choice of cation and anion structures is important not only to design the IL with improved and suitable chemico-physical properties but also to obtain safer and eco-friendly ILs. Moreover there is a clear indication that the composition of the abiotic environment has to be taken into account when the toxicity of ILs in various biological test systems is analysed, because, for example, the data reported in the Thesis indicate a significant influence of salinity variations on algal toxicity. Aerobic biodegradation of four imidazolium ionic liquids, two alkylated and two oxygenated, in soil was evaluated for the first time. Alkyl ionic liquids were shown to be biodegradable over the 6 months test period, and in contrast no significant mineralisation was observed with oxygenated derivatives. A different result was observed in the aerobic biodegradation of alkylated and oxygenated pyridinium ionic liquids in water because all the ionic liquids were almost completely degraded after 10 days, independently by the number of oxygen in the lateral chain of the cation. The synthesis of new ionic liquids by using renewable feedstock as starting materials, has been developed through the synthesis of furan-based ion pairs from furfural. The new ammonium salts were synthesised in very good yields, good purity of the products and wide versatility, combining low melting points with high decomposition temperatures and reduced viscosities. Regarding the possible applications as surfactants and biocides, furan-based salts could be a valuable alternative to benzyltributylammonium salts and benzalkonium chloride that are produced from non-renewable resources. A new procedure for the allylation of ketones and aldehydes with tetraallyltin in ionic liquids was developed. The reaction afforded high yields both in sulfonate-containing ILs and in ILs without sulfonate upon addition of a small amount of sulfonic acid. The checked reaction resulted in peculiar chemoselectivity favouring aliphatic substrates towards aromatic ketones and good stereoselectivity in the allylation of levoglucosenone. Finally ILs-based systems could be easily and successfully recycled, making the described procedure environmentally benign. The potential role of switchable polarity solvents as a green technology for the extraction of vegetable oil from terrestrial and aquatic biomass has been investigated. The extraction efficiency of terrestrial biomass rich in triacylglycerols, as soy bean flakes and sunflower seeds, was comparable to those of traditional organic solvents, being the yield of vegetable oils recovery very similar. Switchable polarity solvents as been also exploited for the first time in the extraction of hydrocarbons from the microalga Botryococcus braunii, demonstrating the efficiency of the process for the extraction of both dried microalgal biomass and directly of the aqueous growth medium. The switchable polarity solvents exhibited better extraction efficiency than conventional solvents, both with dried and liquid samples. This is an important issue considering that the harvest and the dewatering of algal biomass have a large impact on overall costs and energy balance.

Zuckertransport und Regulation des Hexosestoffwechsels bei Oenococcus oeni

Das Milchsäurebakterium Oenococcus oeni, welches für den biologischen Säureabbau im Wein eingesetzt wird, verstoffwechselt Hexosen über den Phosphoketolaseweg. Dabei können beträchtliche Mengen Acetat entstehen. Die Ursachen dafür wurden untersucht, insbesondere der Fructosestoffwechsel. Außerdem wurde der Hexosetransport untersucht, über den bei O. oeni noch nichts bekannt war. Die Aufnahme von Hexosen in die Zelle erfolgt mit hoher Affinität (KM=10 µM) über einen Symport mit H+, aber mit sehr niedriger spezifischer Aktivität (Vmax=9 U / g TG). Zusätzlich werden Hexosen mit ausreichender Aktivität über (vermutlich erleichterte) Diffusion in die Zelle transportiert, allerdings nur bei hohen Hexosekonzentrationen. Es wurden Gene gefunden, die für ein Hexose- Phosphotransferasesystem kodieren, welches in O. oeni keine bedeutende Rolle beim Transport spielt, aber vermutlich eine regulative Funktion hat. Zur Bildung von Essigsäure tragen verschiedene Faktoren bei: Der Ethanolweg, der in der heterofermentativen Milchsäuregärung die Reoxidation von NAD(P)H bewerkstelligt, ist durch die niedrige spezifische Aktivität der Acetaldehyddehydrogenase limitiert. Diese Limitierung wird noch verstärkt, wenn die zellulären Gehalte von Coenzym A aufgrund von Pantothensäuremangel niedrig sind. O. oeni umgeht durch Bildung von Erythrit die Limitierung, und Acetylphosphat wird nicht zu Ethanol reduziert, sondern als Acetat ausgeschieden. Bei Cofermentation von Hexosen mit externen Elektronenakzeptoren, wie Fructose, Pyruvat oder Sauerstoff, werden letztere zur Reoxidation von NAD(P)H genutzt, und als Folge wird Acetat ausgeschieden. Der Fluss von Fructose in den Phosphoketolaseweg wird durch das Enzym Phosphoglucoseisomerase verhindert, wenn dieses durch 6-Phosphogluconat gehemmt wird. Als Konsequenz wird Fructose im Mannitweg reduziert, was die Bildung von Essigsäure im Phosphoketolaseweg fördert. Bei niedrigen Wachstums- und Stoffwechselraten, z.B. bei C-Limitierung, ist der Ethanolweg nicht limitierend für den Stoffwechsel, und Hexosen werden über heterofermentative Milchsäuregärung umgesetzt, ohne daß Acetat entsteht. Pyruvat kann gleichzeitig als Elektronenakzeptor und als Energiequelle dienen: O. oeni ist in der Lage, Pyruvat mittels Disproportionierung zu Lactat und Acetat+CO2 zu fermentieren, und dabei Energie zu konservieren (0,5 ATP / Pyruvat).

Anaerobic oxidation of ethanol over spinel mixed oxides: the first step in the steam-iron process for H2 production

The future hydrogen demand is expected to increase, both in existing industries (including upgrading of fossil fuels or ammonia production) and in new technologies, like fuel cells. Nowadays, hydrogen is obtained predominantly by steam reforming of methane, but it is well known that hydrocarbon based routes result in environmental problems and besides the market is dependent on the availability of this finite resource which is suffering of rapid depletion. Therefore, alternative processes using renewable sources like wind, solar energy and biomass, are now being considered for the production of hydrogen. One of those alternative methods is the so-called “steam-iron process” which consists in the reduction of a metal-oxide by hydrogen-containing feedstock, like ethanol for instance, and then the reduced material is reoxidized with water to produce “clean” hydrogen (water splitting). This kind of thermochemical cycles have been studied before but currently some important facts like the development of more active catalysts, the flexibility of the feedstock (including renewable bio-alcohols) and the fact that the purification of hydrogen could be avoided, have significantly increased the interest for this research topic. With the aim of increasing the understanding of the reactions that govern the steam-iron route to produce hydrogen, it is necessary to go into the molecular level. Spectroscopic methods are an important tool to extract information that could help in the development of more efficient materials and processes. In this research, ethanol was chosen as a reducing fuel and the main goal was to study its interaction with different catalysts having similar structure (spinels), to make a correlation with the composition and the mechanism of the anaerobic oxidation of the ethanol which is the first step of the steam-iron cycle. To accomplish this, diffuse reflectance spectroscopy (DRIFTS) was used to study the surface composition of the catalysts during the adsorption of ethanol and its transformation during the temperature program. Furthermore, mass spectrometry was used to monitor the desorbed products. The set of studied materials include Cu, Co and Ni ferrites which were also characterized by means of X-ray diffraction, surface area measurements, Raman spectroscopy, and temperature programmed reduction.

New eco-friendly polyesters from renewable resources

Nowadays the development of sustainable polymers, with convenient properties to substitute the traditional petroleum-based materials, is one of the major issues for material science. The utilization of renewable resources as feedstock for biopolyesters is a challenging target.The research work described in the present thesis is strictly connected to these urgent necessities and is focused mainly in finding new biopolymers, in particular biopolyesters, which are obtainable from biomass and characterized by a wide range of properties, in order to potentially substitute polyolefins and aromatic polyesters (for example, poly(ethylene terephthalate))

Pretrattamenti termo-meccanici ed enzimatici su scarti dell'industria enologica per la produzione di Biogas

A fundamental assumption for by-product from winery industy waste-management is their economic and commercial increase in value. High energetic value recovery from winery industry is an attractive economic solution to stimulate new sustainable process. Approach of this work is based about physic and biological treatment with grape stalks and grape marc to increase polysaccharides components of cell wall and energetic availability of this by-products. Grape stalks for example have a high percentage of lignin and cellulose and can’t be used, whitout pretreatment, for an anaerobic digestion process. Our findings show enzymatic and thermo-mechanical pre-treatments in combined application for optimise hydrolytic mechanism on winemaking wastes which represents 0,9 milion ton/year in Italy and on straw, cereal by-products with high lignin content. A screening of specifically industrial enzymatic complex for the hydrolysis lignocellulosic biomass were tested using the principal polysaccharides component of the vegetal cells. Combined thermo-mechanical and enzymatic pretreatment improve substrates conversion in batch test fermentation experiment. The conservation of the grape stalks, at temperature above 0°C, allow the growth of spontaneus fermentation that reduce their polysaccharides content so had investigated anarobic condition of conservation. The other objective of this study was to investigate the capability of a proprietary strain of L.buchneri LN 40177 to enhance the accessibility of fermentable forage constituents during the anaerobic conservation process by releasing the enzyme ferulate esterase. The time sequence study by batch tests showed that the L. buchneri LN-40177 inoculated grape stalk substrate was more readily available in the fermenter. In batch tests with grape stalk, after mechanical treatment, the L. buchneri LN41077 treated substrate yielded on average 70% more biogas per kg/DM. Thermo-mechanical, enzymatic and biological treatment with L. buchneri LN-40177 can increase the biogas production from low fermented biomasses and the consequent their useful in anaerobic biodigesters for agro-bioenergy production.

Selective photo-oxidation of cellobiose with tio2-supported metal nanoparticles

Upgrade of biomass to valuable chemicals is a central topic in modern research due to the high availability and low price of this feedstock. For the difficulties in biomass treatment, different pathways are still under investigation. A promising way is in the photodegradation, because it can lead to greener transformation processes with the use of solar light as a renewable resource. The aim of my work was the research of a photocatalyst for the hydrolysis of cellobiose under visible irradiation. Cellobiose was selected because it is a model molecule for biomass depolymerisation studies. Different titania crystalline structures were studied to find the most active phase. Furthermore, to enhance the absorption of this semiconductor in the visible range, noble metal nanoparticles were immobilized on titania. Gold and silver were chosen because they present a Surface Plasmon Resonance band and they are active metals in several photocatalytic reactions. The immobilized catalysts were synthesized following different methods to optimize the synthetic steps and to achieve better performances. For the same purpose the alloying effect between gold and silver nanoparticles was examined.

Optimization of bioenergy solutions at different farm scales

RAF is a bio-energetic descriptive model integrates with MAD model to support Integrated Farm Management. RAF model aimed to enhancing economical, social and environmental sustainability of farm production in terms of energy via convert energy crops and animal manure to biogas and digestate (bio-fertilizers) by anaerobic digestion technologies, growing and breeding practices. The user defines farm structure in terms of present crops, livestock and market prices and RAF model investigates the possibilities of establish on-farm biogas system (different anaerobic digestion technologies proposed for different scales of farms in terms of energy requirements) according to budget and sustainability constraints to reduce the dependence on fossil fuels. The objective function of RAF (Z) is optimizing the total net income of farm (maximizing income and minimizing costs) for whole period which is considered by the analysis. The main results of this study refers to the possibility of enhancing the exploitation of the available Italian potentials of biogas production from on-farm production of energy crops and livestock manure feedstock by using the developed mathematical model RAF integrates with MAD to presents reliable reconcile between farm size, farm structure and on-farm biogas systems technologies applied to support selection, applying and operating of appropriate biogas technology at any farm under Italian conditions.

Genus Bifidobacterium: taxonomy studies and gene expression analysis on folate pathway

Folates (vitamin B9) are essential water soluble vitamins, whose deficiency in humans may contribute to the onset of several diseases, such as anaemia, cancer, cardiovascular diseases, neurological problems as well as defects in embryonic development. Human and other mammals are unable to synthesize ex novo folate obtaining it from exogenous sources, via intestinal absorption. Recently the gut microbiota has been identified as an important source of folates and the selection and use of folate producing microorganisms represents an innovative strategy to increase human folate levels. The aim of this thesis was to gain a fundamental understanding of folate metabolism in Bifidobacterium adolescentis. The work was subdivided in three main phases, also aimed to solve different problems encountered working with Bifidobacterium strains. First, a new identification method (based on PCR-RFLP of hsp60 gene) was specifically developed to identify Bifidobacterium strains. Secondly, Bifidobacterium adolescentis biodiversity was explored in order to recognize representing strains of this species to be screened for their folate production ability. Results showed that this species is characterized by a wide variability and support the idea that a possible new taxonomic re-organization would be required. Finally B. adolescentis folate metabolism was studied using a double approach. A quantitative analysis of folate content was complemented by the examination of expression levels of genes involved in folate related pathways. For the normalization process, required to increase the robustness of the qRT-PCR analysis, an appropriate set of reference genes was tested using two different algorithms. Results demonstrate that B.adolescentis strains may represent an endogenous source of natural folate and they could be used to fortify fermented dairy products. This bio-fortification strategy presents many advantages for the consumer, providing native folate forms more bio-available, and not implicated in the discussed controversy concerning the safety of high intake of synthetic folic acid.

Evaluation of the photosynthetic efficiency of sweet sorghum under drought and cold conditions

Sweet sorghum, a C4 crop of tropical origin, is gaining momentum as a multipurpose feedstock to tackle the growing environmental, food and energy security demands. Under temperate climates sweet sorghum is considered as a potential bioethanol feedstock, however, being a relatively new crop in such areas its physiological and metabolic adaptability has to be evaluated; especially to the more frequent and severe drought spells occurring throughout the growing season and to the cold temperatures during the establishment period of the crop. The objective of this thesis was to evaluate some adaptive photosynthetic traits of sweet sorghum to drought and cold stress, both under field and controlled conditions. To meet such goal, a series of experiments were carried out. A new cold-tolerant sweet sorghum genotype was sown in rhizotrons of 1 m3 in order to evaluate its tolerance to progressive drought until plant death at young and mature stages. Young plants were able to retain high photosynthetic rate for 10 days longer than mature plants. Such response was associated to the efficient PSII down-regulation capacity mediated by light energy dissipation, closure of reaction centers (JIP-test parameters), and accumulation of glucose and sucrose. On the other hand, when sweet sorghum plants went into blooming stage, neither energy dissipation nor sugar accumulation counteracted the negative effect of drought. Two hybrids with contrastable cold tolerance, selected from an early sowing field trial were subjected to chilling temperatures under controlled growth conditions to evaluate in deep their physiological and metabolic cold adaptation mechanisms. The hybrid which poorly performed under field conditions (ICSSH31), showed earlier metabolic changes (Chl a + b, xanthophyll cycle) and greater inhibition of enzymatic activity (Rubisco and PEPcase activity) than the cold tolerant hybrid (Bulldozer). Important insights on the potential adaptability of sweet sorghum to temperate climates are given.

Assessment and optimization of chemical industrial processes from a life cycle perspective

During the PhD program in chemistry, curriculum in environmental chemistry, at the University of Bologna the sustainability of industry was investigated through the application of the LCA methodology. The efforts were focused on the chemical sector in order to investigate reactions dealing with the Green Chemistry and Green Engineering principles, evaluating their sustainability in comparison with traditional pathways by a life cycle perspective. The environmental benefits associated with a reduction in the synthesis steps and the use of renewable feedstock were assessed through a holistic approach selecting two case studies with high relevance from an industrial point of view: the synthesis of acrylonitrile and the production of acrolein. The current approach wants to represent a standardized application of LCA methodology to the chemical sector, which could be extended to several case studies, and also an improvement of the current databases, since the lack of data to fill the inventories of the chemical productions represent a huge limitation, difficult to overcome and that can affects negatively the results of the studies. Results emerged from the analyses confirms that the sustainability in the chemical sector should be evaluated from a cradle-to-gate approach, considering all the stages and flows involved in each pathways in order to avoid shifting the environmental burdens from a steps to another. Moreover, if possible, LCA should be supported by other tools able to investigate the other two dimensions of sustainability represented by the social and economic issues.

Biochar characterization for its environmental and agricultural utilization. Occurrence, distribution and fate of labile organic carbon and polycyclic aromatic hydrocarbons

In this thesis the potential risks associated to the application of biochar in soil as well the stability of biochar were investigated. The study was focused on the potential risks arising from the occurrence of polycyclic aromatic hydrocarbons (PAHs) in biochar. An analytical method was developed for the determination of the 16 USEPA-PAHs in the original biochar and soil containing biochar. The method was successfully validated with a certified reference material for the soil matrix and compared with methods in use in other laboratories during a laboratory exercise within the EU-COST TD1107. The concentration of 16 USEPA-PAHs along with the 15 EU-PAHs, priority hazardous substances in food, was determined in a suite of currently available biochars for agricultural field applications derived from a variety of parent materials and pyrolysis conditions. Biochars analyzed contained the USEPA and some of the EU-PAHs at detectable levels ranging from 1.2 to 19 µg g-1. This method allowed investigating changes in PAH content and distribution in a four years study following biochar addition in soils in a vineyard (CNR-IBIMET). The results showed that biochar addition determined an increase of the amount of PAHs. However, the levels of PAHs in the soil remained within the maximum acceptable concentration for European countries. The vineyard soil performed by CNR-IBIMET was exploited to study the environmental stability of biochar and its impact on soil organic carbon. The stability of biochar was investigated by analytical pyrolysis (Py-GC-MS) and pyrolysis in the presence of hydrogen (HyPy). The findings showed that biochar amendment significantly influence soil stable carbon fraction concentration during the incubation period. Moreover, HyPy and Py-GC-MS were applied to biochars deriving from three different feedstock at two different pyrolysis temperatures. The results evidenced the influence of feedstock type and pyrolysis conditions on the degree of carbonisation.

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.

Mikrobielle Synthese von Biopolymeren aus der nachwachsenden Rohstoffquelle Weizenstroh

Weizenstroh als erneuerbare Ressource zur Produktion von Biopolymeren und wichtigen Grundchemikalien stellt eine ökologisch sinnvolle Alternative dar. Durch die vom PFI durchgeführte Thermodruckhydrolyse konnte das Weizenstroh und die darin enthaltenen Zucker fast vollständig mobilisiert werden. Ein umfangreiches Screening nach Organismen, welche die Zucker des Weizenstrohs verwerten konnten, ergab, dass einige wenige Stämme zur PHB-Bildung aus Xylose befähigt waren (10 %). Zur PHB-Synthese aus Glucose waren indes ca. doppelt so viele Organismen in der Lage (20 %). Zwei der insgesamt 118 untersuchten Organismen zeigten besonders gute PHB-Bildung sowohl mit Xylose als auch mit Glucose als Substrat. Dabei handelte es sich um die hauseigenen Stämme Bacillus licheniformis KHC 3 und Bacillus megaterium KNaC 2. Nach Enttoxifizierung der hemicellulosischen Fraktion konnte diese als C-Quelle im Mineral Medium eingesetzt werden. Burkholderia sacchari DSM 17165 und Hydrogenophaga pseudoflava DSM 1034, sowie die hauseigenen Isolate Bacillus licheniformis KHC 3 und Bacillus megaterium KNaC 2 wurden für die Synthese von PHB aus der hemicellulosischen Fraktion verwendet. Die Zucker der hemicellulosischen Fraktion (Xylose, Glucose, Arabinose) konnten durch diese Organismen zur PHB-Synthese genutzt werden. Hierbei stellte sich heraus, dass die beiden Bacillus-Stämme besser zur Produktion von PHB aus dem hemicellulosischen Hydrolysat geeignet waren als die Stämme der DSMZ. Die alternative Umsetzung der im hemicellulosischem Hydrolysat enthaltenen Zucker (Xylose, Glucose und Arabinose) in die wichtigen Grundchemikalien Lactat und Acetat konnte durch die Verwendung von heterofermentativen Milchsäurebakterien verwirklicht werden. Die Bildung dieser wichtigen Grundchemikalien stellt eine interessante Alternative zur PHB-Synthese dar. Die Menge an teuren Zusätzen wie Tomatensaft, welcher für das Wachstum der MSB essentiell war, konnte reduziert werden. Die Glucose der zweiten Fraktion des Weizenstrohs, der cellulosischen Fraktion, konnte ebenfalls durch den Einsatz von Mikroorganismen in PHB umgewandelt werden. Kommerzielle Cellulasen der Firma Novozymes konnten große Mengen an Glucose (≥10 g/l) aus der cellulosischen Fraktion freisetzen. Diese freie Glucose wurde mit Hilfe von Cupriavidus necator DSM 545, Cupriavidus necator NCIMB 11599, Bacillus licheniformis KHC 3 und Bacillus megaterium KNaC 2 zu PHB fermentiert. Wie auch beim hemicellulosischen Hydrolysat konnten hier die beiden Bacillus-Stämme die besten Ergebnisse erzielen. Bei ihnen machte die PHB mehr als die Hälfte der Trockenmasse aus. Die Abtrennung des Zielprodukts ohne die Verwendung von umweltschädlichen Lösungsmitteln wurde durch die Lyse der Zielzellen durch eigens isolierte Enzyme aus Streptomyceten verwirklicht. Die Zelllyse durch die Enzyme aus Streptomyces globisporus subsp. caucasius DSM 40814 und Streptomyces albidoflavus DSM 40233 war erfolgreich und zeigte vor allem bei den Bacillen hohe Wirkung (83 % und 99 % Zelllyse). Bei dem Gram-negativen Organismus Cupriavidus necator DSM 428 konnte die anfangs niedrige Zelllyse von 38 % durch Ultraschallbehandlung auf ca. 75 % erhöht werden.

Bedeutung von allelen Varianten des Hexose-Transporters Hxt3p und der Hexokinasen Hxk1p und Hxk2p für Aufnahme und Verwertung von Glucose und Fructose durch Weinhefen

In Hinsicht darauf, dass sich S. cerevisiae-Stämme im Laufe der Domestizierung und Anpassung an verschiedene Habitate genetisch verändert haben, wurde in dieser Arbeit eine repräsentative Auswahl von Labor-, kommerziellen und in der Natur vorkommenden Saccharomyces-Stämmen und ihren Interspezies-Hybriden auf die Verbreitung alleler Varianten der Hexokinase-Gene HXK1 und HXK2 getestet. Von den Hexose-Transportern stand Hxt3p im Mittelpunkt, da seine essentielle Rolle bei der Vergärung von Glucose und Fructose bereits belegt wurde.rnIn dieser Arbeit wurde gezeigt, dass es bedeutende Unterschiede in der Vergärung von Glucose und Fructose zwischen Weinhefen der Gattung Saccharomyces gibt, die z.T. mit Struktur-Varianten des Hexose-Transporter Hxt3p korrelieren. rnInsgesamt 51 Hefestämme wurden auf ihre allele Variante des HXT3-Gens untersucht. Dabei haben sich drei Hauptgruppen (die Fermichamp®-Typ Gruppe, Bierhefen und Hybrid-Stämme) mit unterschiedlichem HXT3-Allel ergeben. Im Zusammenhang mit der Weinherstellung wurden signifikante Nukleotid-Substitutionen innerhalb des HXT3-Gens der robusten S. cerevisiae-Stämme (wie z.B. Sekthefen, kommerzielle Starterkulturen) und Hybrid-Stämmen festgestellt. Diese Hefen zeichneten sich durch die Fähigkeit aus, den Most trotz stressigen Umwelt-Bedingungen (wie hohe Ethanol-Konzentration, reduzierter Ammonium-Gehalt, ungünstiges Glucose:Fructose-Verhältnis) zu vergären. rnDie Experimente deuten darauf hin, dass die HXT3-Allel-Variante des als Starterkultur verwendbaren Stammes Fermichamp®, für den verstärkten Fructose-Abbau verantwortlich ist. Ein gleiches Verhalten der Stämme mit dieser Allel-Variante wurde ebenfalls beobachtet. Getestet wurden die S. cerevisiae-Stämme Fermichamp® und 54.41, die bezüglich Hxt3p-Aminosäuresequenz gleich sind, gegenüber zwei S. cerevisiae-Stämmen mit dem HXT3-Standard-Alleltyp Fermivin® und 33. Der Unterschied in der Hexose-Verwertung zwischen Stämmen mit Fermichamp®- und Standard-Alleltyp war in der Mitte des Gärverlaufs am deutlichsten zu beobachten. Beide Gruppen, sowohl mit HXT3 Fermichamp®- als auch Fermivin®-Alleltyp vergoren die Glucose schneller als die Fructose. Der Unterschied aber zwischen diesen HXT3-Alleltypen bei der Zucker-Verwertung lag darin, dass der Fermichamp®-Typ eine kleinere Differenz in der Abbau-Geschwindigkeit der beiden Hexosen zeigte als der Fermivin®-Typ. Die Zuckeraufnahme-Messungen haben die relativ gute Fructose-Aufnahme dieser Stämme bestätigt.rnEbenfalls korrelierte der fructophile Charakter des Triple-Hybrides S. cerevisiae x S. kudriavzevii x S. bayanus-Stamm HL78 in Transportexperimenten mit verstärkter Aufnahme von Fructose im Vergleich zu Glucose. Insgesamt zeigte dieser Stamm ähnliches Verhalten wie die S. cerevisiae-Stämme Fermichamp® und 54.41. rnIn dieser Arbeit wurde ein Struktur-Modell des Hexose-Transporters Hxt3p erstellt. Als Basis diente die zu 30 % homologe Struktur des Proton/Xylose-Symporters XylE aus Escherichia coli. Anhand des Hxt3p-Modells konnten Sequenzbereiche mit hoher Variabilität (Hotspots) in drei Hxt3p-Isoformen der Hauptgruppen (die Fermichamp®-Typ Gruppe, Bierhefen und Hybrid-Stämme) detektiert werden. Diese signifikanten Aminosäure-Substitutionen, die eine mögliche Veränderung der physikalischen und chemischen Eigenschaften des Carriers mit sich bringen, konzentrieren sich auf drei Bereiche. Dazu gehören die Region zwischen den N- und C-terminalen Domänen, die cytosolische Domäne und der Outside-Loop zwischen Transmembranregion 9 und Transmembranregion 10. rnObwohl die Transportmessungen keinen Zusammenhang zwischen Stämmen mit unterschiedlichen HXT3-Allelen und ihrer Toleranz gegenüber Ethanol ergaben, wurde ein signifikanter Anstieg in der Zuckeraufnahme nach vorheriger 24-stündiger Inkubation mit 4 Vol% Ethanol bei den Teststämmen beobachtet. rnInsgesamt könnten allele Varianten von HXT3-Gen ein nützliches Kriterium bei der Suche nach robusten Hefen für die Weinherstellung oder für andere industrielle Anwendungen sein. Die Auswirkung dieser Modifikationen auf die Struktur und Effizienz des Hexose-Transporters, sowie der mögliche Zusammenhang mit Ethanol-Resistenz müssen weiter ausführlich untersucht werden. rnEin Zusammenhang zwischen den niedrig variablen Allel-Varianten der Hexokinase-Gene HXK1 und HXK2 und dem Zucker-Metabolismus wurde nicht gefunden. Die Hexokinasen der untersuchten Stämme wiesen allerdings generell eine signifikante geringere Affinität zu Fructose im Vergleich zu Glucose auf. Hier liegt sicherlich eine Hauptursache für den Anstieg des Fructose:Glucose-Verhältnisses im Laufe der Vergärung von Traubenmosten.rn