Estudo da combustão do óleo pirolítico de pneus

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Polycyclic aromatic hydrocarbons (PAHs) in a large South American industrial coastal area (Santos Estuary, Southeastern Brazil): Sources and depositional history

Located in southeastern Brazil, the Santos Estuary has the most important industrial and urban population area of South America. Since the 1950`s, increased urbanization and industrialization near the estuary margins has caused the degradation of mangroves and has increased the discharge of sewage and industrial effluents. The main objectives of this work were to determine the concentrations and sources of polycyclic aromatic hydrocarbons (PAHs) in sediment cores in order to investigate the input of these substances in the last 50 years. The PAHs analyses indicated multiple sources of these compounds (oil and pyrolitic origin), basically anthropogenic contributions from biomass, coal and fossil fuels combustion. The distribution of PAHs in the cores was associated with the formation and development of Cubatao industrial complex and the Santos harbour, waste disposal, world oil crisis and the pollution control program, which results in the decrease of organic pollutants input in this area. (C) 2011 Elsevier Ltd. All rights reserved.

Vehicle emissions and PM2.5 mass concentrations in six Brazilian cities

In Brazil, the principal source of air pollution is the combustion of fuels (ethanol, gasohol, and diesel). In this study, we quantify the contributions that vehicle emissions make to the urban fine particulate matter (PM2.5) mass in six state capitals in Brazil, collecting data for use in a larger project evaluating the impact of air pollution on human health. From winter 2007 to winter 2008, we collected 24-h PM2.5 samples, employing gravimetry to determine PM2.5 mass concentrations; reflectance to quantify black carbon concentrations; X-ray fluorescence to characterize elemental composition; and ion chromatography to determine the composition and concentrations of anions and cations. Mean PM2.5 concentrations in the cities of Sao Paulo, Rio de Janeiro, Belo Horizonte, Curitiba, Porto Alegre, and Recife were 28, 17.2, 14.7, 14.4, 13.4, and 7.3 mu g/m(3), respectively. In Sao Paulo and Rio de Janeiro, black carbon explained approximately 30% of the PM2.5 mass. We used receptor models to identify distinct source-related PM2.5 fractions and correlate those fractions with daily mortality rates. Using specific rotation factor analysis, we identified the following principal contributing factors: soil and crustal material; vehicle emissions and biomass burning (black carbon factor); and fuel oil combustion in industries (sulfur factor). In all six cities, vehicle emissions explained at least 40% of the PM2.5 mass. Elemental composition determination with receptor modeling proved an adequate strategy to identify air pollution sources and to evaluate their short- and long-term effects on human health. Our data could inform decisions regarding environmental policies vis-a-vis health care costs.

Genotoxicity assessment of water soluble fractions of biodiesel and its diesel blends using the Salmonella assay and the in vitro MicroFlow (R) kit (Litron) assay

The designation of biodiesel as an environmental-friendly alternative to diesel oil has improved its commercialization and use. However, most biodiesel environmental safety studies refer to air pollution and so far there have been very few literature data about its impacts upon other biotic systems, e.g. water, and exposed organisms. Spill simulations in water were carried out with neat diesel and biodiesel and their blends aiming at assessing their genotoxic potentials should there be contaminations of water systems. The water soluble fractions (WSF) from the spill simulations were submitted to solid phase extraction with C-18 cartridge and the extracts obtained were evaluated carrying out genotoxic and mutagenic bioassays [the Salmonella assay and the in vitro MicroFlow (R) kit (Litron) assay]. Mutagenic and genotoxic effects were observed, respectively, in the Salmonella/microsome preincubation assay and the in vitro MN test carried out with the biodiesel WSF. This interesting result may be related to the presence of pollutants in biodiesel derived from the raw material source used in its production chain. The data showed that care while using biodiesel should be taken to avoid harmful effects on living organisms in cases of water pollution. (C) 2011 Elsevier Ltd. All rights reserved.

Processi di biorefining per l'estrazione di secondary chemical building blocks da sottoprotti dell'agro-industria

Phenol and cresols represent a good example of primary chemical building blocks of which 2.8 million tons are currently produced in Europe each year. Currently, these primary phenolic building blocks are produced by refining processes from fossil hydrocarbons: 5% of the world-wide production comes from coal (which contains 0.2% of phenols) through the distillation of the tar residue after the production of coke, while 95% of current world production of phenol is produced by the distillation and cracking of crude oil. In nature phenolic compounds are present in terrestrial higher plants and ferns in several different chemical structures while they are essentially absent in lower organisms and in animals. Biomass (which contain 3-8% of phenols) represents a substantial source of secondary chemical building blocks presently underexploited. These phenolic derivatives are currently used in tens thousand of tons to produce high cost products such as food additives and flavours (i.e. vanillin), fine chemicals (i.e. non-steroidal anti-inflammatory drugs such as ibuprofen or flurbiprofen) and polymers (i.e. poly p-vinylphenol, a photosensitive polymer for electronic and optoelectronic applications). European agrifood waste represents a low cost abundant raw material (250 millions tons per year) which does not subtract land use and processing resources from necessary sustainable food production. The class of phenolic compounds is essentially constituted by simple phenols, phenolic acids, hydroxycinnamic acid derivatives, flavonoids and lignans. As in the case of coke production, the removal of the phenolic contents from biomass upgrades also the residual biomass. Focusing on the phenolic component of agrifood wastes, huge processing and marketing opportunities open since phenols are used as chemical intermediates for a large number of applications, ranging from pharmaceuticals, agricultural chemicals, food ingredients etc. Following this approach we developed a biorefining process to recover the phenolic fraction of wheat bran based on enzymatic commercial biocatalysts in completely water based process, and polymeric resins with the aim of substituting secondary chemical building blocks with the same compounds naturally present in biomass. We characterized several industrial enzymatic product for their ability to hydrolize the different molecular features that are present in wheat bran cell walls structures, focusing on the hydrolysis of polysaccharidic chains and phenolics cross links. This industrial biocatalysts were tested on wheat bran and the optimized process allowed to liquefy up to the 60 % of the treated matter. The enzymatic treatment was also able to solubilise up to the 30 % of the alkali extractable ferulic acid. An extraction process of the phenolic fraction of the hydrolyzed wheat bran based on an adsorbtion/desorption process on styrene-polyvinyl benzene weak cation-exchange resin Amberlite IRA 95 was developed. The efficiency of the resin was tested on different model system containing ferulic acid and the adsorption and desorption working parameters optimized for the crude enzymatic hydrolyzed wheat bran. The extraction process developed had an overall yield of the 82% and allowed to obtain concentrated extracts containing up to 3000 ppm of ferulic acid. The crude enzymatic hydrolyzed wheat bran and the concentrated extract were finally used as substrate in a bioconversion process of ferulic acid into vanillin through resting cells fermentation. The bioconversion process had a yields in vanillin of 60-70% within 5-6 hours of fermentation. Our findings are the first step on the way to demonstrating the economical feasibility for the recovery of biophenols from agrifood wastes through a whole crop approach in a sustainable biorefining process.

Bioremediation of PAHs - Limitations and soultions

Introduction 1.1 Occurrence of polycyclic aromatic hydrocarbons (PAH) in the environment Worldwide industrial and agricultural developments have released a large number of natural and synthetic hazardous compounds into the environment due to careless waste disposal, illegal waste dumping and accidental spills. As a result, there are numerous sites in the world that require cleanup of soils and groundwater. Polycyclic aromatic hydrocarbons (PAHs) are one of the major groups of these contaminants (Da Silva et al., 2003). PAHs constitute a diverse class of organic compounds consisting of two or more aromatic rings with various structural configurations (Prabhu and Phale, 2003). Being a derivative of benzene, PAHs are thermodynamically stable. In addition, these chemicals tend to adhere to particle surfaces, such as soils, because of their low water solubility and strong hydrophobicity, and this results in greater persistence under natural conditions. This persistence coupled with their potential carcinogenicity makes PAHs problematic environmental contaminants (Cerniglia, 1992; Sutherland, 1992). PAHs are widely found in high concentrations at many industrial sites, particularly those associated with petroleum, gas production and wood preserving industries (Wilson and Jones, 1993). 1.2 Remediation technologies Conventional techniques used for the remediation of soil polluted with organic contaminants include excavation of the contaminated soil and disposal to a landfill or capping - containment - of the contaminated areas of a site. These methods have some drawbacks. The first method simply moves the contamination elsewhere and may create significant risks in the excavation, handling and transport of hazardous material. Additionally, it is very difficult and increasingly expensive to find new landfill sites for the final disposal of the material. The cap and containment method is only an interim solution since the contamination remains on site, requiring monitoring and maintenance of the isolation barriers long into the future, with all the associated costs and potential liability. A better approach than these traditional methods is to completely destroy the pollutants, if possible, or transform them into harmless substances. Some technologies that have been used are high-temperature incineration and various types of chemical decomposition (for example, base-catalyzed dechlorination, UV oxidation). However, these methods have significant disadvantages, principally their technological complexity, high cost , and the lack of public acceptance. Bioremediation, on the contrast, is a promising option for the complete removal and destruction of contaminants. 1.3 Bioremediation of PAH contaminated soil & groundwater Bioremediation is the use of living organisms, primarily microorganisms, to degrade or detoxify hazardous wastes into harmless substances such as carbon dioxide, water and cell biomass Most PAHs are biodegradable unter natural conditions (Da Silva et al., 2003; Meysami and Baheri, 2003) and bioremediation for cleanup of PAH wastes has been extensively studied at both laboratory and commercial levels- It has been implemented at a number of contaminated sites, including the cleanup of the Exxon Valdez oil spill in Prince William Sound, Alaska in 1989, the Mega Borg spill off the Texas coast in 1990 and the Burgan Oil Field, Kuwait in 1994 (Purwaningsih, 2002). Different strategies for PAH bioremediation, such as in situ , ex situ or on site bioremediation were developed in recent years. In situ bioremediation is a technique that is applied to soil and groundwater at the site without removing the contaminated soil or groundwater, based on the provision of optimum conditions for microbiological contaminant breakdown.. Ex situ bioremediation of PAHs, on the other hand, is a technique applied to soil and groundwater which has been removed from the site via excavation (soil) or pumping (water). Hazardous contaminants are converted in controlled bioreactors into harmless compounds in an efficient manner. 1.4 Bioavailability of PAH in the subsurface Frequently, PAH contamination in the environment is occurs as contaminants that are sorbed onto soilparticles rather than in phase (NAPL, non aqueous phase liquids). It is known that the biodegradation rate of most PAHs sorbed onto soil is far lower than rates measured in solution cultures of microorganisms with pure solid pollutants (Alexander and Scow, 1989; Hamaker, 1972). It is generally believed that only that fraction of PAHs dissolved in the solution can be metabolized by microorganisms in soil. The amount of contaminant that can be readily taken up and degraded by microorganisms is defined as bioavailability (Bosma et al., 1997; Maier, 2000). Two phenomena have been suggested to cause the low bioavailability of PAHs in soil (Danielsson, 2000). The first one is strong adsorption of the contaminants to the soil constituents which then leads to very slow release rates of contaminants to the aqueous phase. Sorption is often well correlated with soil organic matter content (Means, 1980) and significantly reduces biodegradation (Manilal and Alexander, 1991). The second phenomenon is slow mass transfer of pollutants, such as pore diffusion in the soil aggregates or diffusion in the organic matter in the soil. The complex set of these physical, chemical and biological processes is schematically illustrated in Figure 1. As shown in Figure 1, biodegradation processes are taking place in the soil solution while diffusion processes occur in the narrow pores in and between soil aggregates (Danielsson, 2000). Seemingly contradictory studies can be found in the literature that indicate the rate and final extent of metabolism may be either lower or higher for sorbed PAHs by soil than those for pure PAHs (Van Loosdrecht et al., 1990). These contrasting results demonstrate that the bioavailability of organic contaminants sorbed onto soil is far from being well understood. Besides bioavailability, there are several other factors influencing the rate and extent of biodegradation of PAHs in soil including microbial population characteristics, physical and chemical properties of PAHs and environmental factors (temperature, moisture, pH, degree of contamination). Figure 1: Schematic diagram showing possible rate-limiting processes during bioremediation of hydrophobic organic contaminants in a contaminated soil-water system (not to scale) (Danielsson, 2000). 1.5 Increasing the bioavailability of PAH in soil Attempts to improve the biodegradation of PAHs in soil by increasing their bioavailability include the use of surfactants , solvents or solubility enhancers.. However, introduction of synthetic surfactant may result in the addition of one more pollutant. (Wang and Brusseau, 1993).A study conducted by Mulder et al. showed that the introduction of hydropropyl-ß-cyclodextrin (HPCD), a well-known PAH solubility enhancer, significantly increased the solubilization of PAHs although it did not improve the biodegradation rate of PAHs (Mulder et al., 1998), indicating that further research is required in order to develop a feasible and efficient remediation method. Enhancing the extent of PAHs mass transfer from the soil phase to the liquid might prove an efficient and environmentally low-risk alternative way of addressing the problem of slow PAH biodegradation in soil.

Effetto di un packaging innovativo sulla qualità di nettarine

L’imballaggio alimentare si può definire come un sistema coordinato per disporre i beni per il trasporto, la distribuzione, la conservazione, la vendita e l’utilizzo. Uno dei materiali maggiormente impiegati, nell’industria alimentare, per la produzione di imballaggi sono le materie plastiche. Esse sono sostanze organiche derivanti da petrolio greggio, sono composti solidi allo stato finito, ma possono essere modellate allo stato fluido. Un imballaggio alimentare deve svolgere determinate funzioni tra cui: - contenimento del prodotto - protezione del prodotto da agenti esterni - logistica - comunicativa - funzionale - ecologica L'ultimo punto sopracitato è il principale problema delle materie plastiche derivanti dal petrolio greggio. Questi materiali sono difficilmente riciclabili perché spesso un imballaggio è composto da più materiali stratificati o perché si trova a diretto contatto con gli alimenti. Inoltre questi materiali hanno un lungo tempo di degradazione (da 100 a 1000 anni) che ne rendono difficile e costoso lo smaltimento. Per questo nell’ultimo decennio è cominciata la ricerca di un materiale plastico, flessibile alle esigenze industriali e nel contempo biodegradabile. Una prima idea è stata quella di “imitare la natura” cercando di replicare macromolecole già esistenti (derivate da amido e zuccheri) per ottenere una sostanza plastico-simile utilizzabile per gli stessi scopi, ma biodegradabile in circa sei mesi. Queste bioplastiche non hanno preso piede per l’alto costo di produzione e perché risulta impossibile riconvertire impianti di produzione in tutto il mondo in tempi brevi. Una seconda corrente di pensiero ha indirizzato i propri sforzi verso l’utilizzo di speciali additivi aggiunti in minima misura (1%) ai classici materiali plastici e che ne permettono la biodegradazione in un tempo inferiore ai tre anni. Un esempio di questo tipo di additivi è l’ECM Masterbatch Pellets che è un copolimero di EVA (etilene vinil acetato) che aggiunto alle plastiche tradizionali rende il prodotto finale completamente biodegradabile pur mantenendo le proprie caratteristiche. Scopo di questo lavoro di tesi è stato determinare le modificazioni di alcuni parametri qualitativi di nettarine di Romagna(cv.-Alexa®) confezionate-con-film-plastici-tradizionali-e-innovativi. I campioni di nettarine sono stati confezionati in cestini in plastica da 1 kg (sigillati con un film flow-pack macroforato) di tipo tradizionale in polipropilene (campione denominato TRA) o vaschette in polipropilene additivato (campione denominato BIO) e conservati a 4°C e UR 90-95% per 7 giorni per simulare un trasporto refrigerato successivamente i campioni sono stati posti in una camera a 20°C e U.R. 50% per 4 giorni al fine di simulare una conservazione al punto vendita. Al tempo 0 e dopo 4, 7, 9 e 11 giorni sono state effettuate le seguenti analisi: - coefficiente di respirazione è stato misurata la quantità di CO2 prodotta - indice di maturazione espresso come rapporto tra contenuto in solidi solubili e l’acidità titolabile - analisi di immagine computerizzata - consistenza della polpa del frutto è stata misurata attraverso un dinamometro Texture Analyser - contenuto in solidi totali ottenuto mediante gravimetria essiccando i campioni in stufa sottovuoto - caratteristiche sensoriali (Test Accettabilità) Conclusioni In base ai risultati ottenuti i due campioni non hanno fatto registrare dei punteggi significativamente differenti durante tutta la conservazione, specialmente per quanto riguarda i punteggi sensoriali, quindi si conclude che le vaschette biodegradabili additivate non influenzano la conservazione delle nettarine durante la commercializzazione del prodotto limitatamente ai parametri analizzati. Si ritiene opportuno verificare se il processo di degradazione del polimero additivato si inneschi già durante la commercializzazione della frutta e soprattutto verificare se durante tale processo vengano rilasciati dei gas che possono accelerare la maturazione dei frutti (p.e. etilene), in quanto questo spiegherebbe il maggiore tasso di respirazione e la più elevata velocità di maturazione dei frutti conservati in tali vaschette. Alimentary packaging may be defined as a coordinate system to dispose goods for transport, distribution, storage, sale and use. Among materials most used in the alimentary industry, for the production of packaging there are plastics materials. They are organic substances deriving from crude oil, solid compounds in the ended state, but can be moulded in the fluid state. Alimentary packaging has to develop determinated functions such as: - Product conteniment - Product protection from fieleders agents - logistic - communicative - functional - ecologic This last term is the main problem of plastic materials deriving from crude oil. These materials are hardly recyclable because a packaging is often composed by more stratified materials or because it is in direct contact with aliments. Beside these materials have a long degradation time(from 100 to 1000 years) that make disposal difficult and expensive. For this reason in the last decade the research for a new plastic material is begin, to make industrial demands more flexible and, at the same time, to make this material biodegradable: At first, the idea to “imitate the nature” has been thought, trying to reply macromolecules already existents (derived from amid and sugars) to obtain a similar-plastic substance that can be used for the same purposes, but it has to be biodegradable in about six months. These bioplastics haven’t more success bacause of the high production cost and because reconvert production facilities of all over the wolrd results impossible in short times. At second, the idea to use specials addictives has been thought. These addictives has been added in minim measure (1%) to classics plastics materials and that allow the biodegradation in a period of time under three years. An example of this kind of addictives is ECM Masterbatch Pellets which is a coplymer of EVA (Ethylene vinyl acetate) that, once it is added to tradizional plastics, make final product completely biodegradable however maintaining their own attributes. The objective of this thesis work has been to determinate modifications of some Romagna’s Nectarines’ (cv. Alexa®) qualitatives parameters which have been packaged-with traditional and innovative-plastic film. Nectarines’ samples have been packaged in plastic cages of 1 kg (sealed with a macro-drilled flow-pack film) of traditional type in polypropylene (sample named TRA) or trays in polypropylene with addictives (sample named BIO) and conservated at 4°C and UR 90-95% for 7 days to simulate a refrigerated transport. After that, samples have been put in a camera at 20°C and U.R. 50% for 4 days to simulate the conservation in the market point. At the time 0 and after 4, 7, 9 and 11 days have been done the following analaysis: - Respiration coefficient wherewith the amount CO2 producted has been misurated - Maturation index which is expressed as the ratio between solid soluble content and the titratable acidity - Analysis of computing images - Consistence of pulp of the fruit that has been measured through Texture Analyser Dynanometer - Content in total solids gotten throught gravimetry by the drying of samples in vacuum incubator - Sensorial characteristic (Panel Test) Consequences From the gotten results, the two samples have registrated no significative different scores during all the conservation, expecially about the sensorial scores, so it’s possible to conclude that addictived biodegradable trays don’t influence the Nectarines’ conservation during the commercialization of the product qualifiedly to analized parameters. It’s advised to verify if the degradation process of the addicted polymer may begin already during the commercialization of the fruit and in particular to verify if during this process some gases could be released which can accelerate the maturation of fruits (p.e. etylene), because all this will explain the great respiration rate and the high speed of the maturation of fruits conservated in these trays.

Entwicklung massenspektrometrischer Isotopenverdünnungstechniken für die zuverlässige Bestimmung von Elementspuren und Schwefelspezies in Erdölprodukten

Einer der Hauptschwerpunkte der Arbeit lag in der Entwicklung einer spezies-spezifischen und einer spezies-unspezifischen GC-ICP-Q-MSIVA von Schwefelspezies in Petroprodukten. Es wurden hierzu Indikatoren, ausgehend von elementarem 34S-angereichertem Schwefel, im Mikromaßstab synthetisiert. Für die spezies-spezifische GC-ICP-Q-MSIVA wurde die erstmalige Synthese von 34S-markiertem Thiophen, Dibenzothiophen und 4-Methyldibenzothiophen verwirklicht. Als Indikatorsynthese für die spezies-unspezifische GC-ICP-Q-MSIVA erfolgte die erstmalige Darstellung von 34S-angereichertem Dimethyldisulid. Mit Hilfe der synthetisierten Verbindungen wurden spezies-spezifische und spezies-unspezifische massenspektrometrische Isotopenverdünnungsanalysen von Schwefelspezies in Petroprodukten durchgeführt. Vor allen GC-ICP-Q-MSIVA-Analysen erfolgte eine umfangreiche Speziesidentifizierung durch Aufstockexperimente mit kommerziell erhältlichen Standards und mit einem mit der GC gekoppelten Elektronenstoß (EI)-MS. Beide ICP-Q-MS Methoden zeichnen sich durch sehr niedrige Nachweisgrenzen (7 ng S/g) aus, welche auch eine Anwendbarkeit auf tiefentschwefelte Kraftstoffe garantieren. Mit der spezies-unspezifischen GC-ICP-Q-MSIVA ist neben einer Speziesanalyse auch eine Gesamtschwefelanalyse durch Aufsummierung aller in der Probe vorhandenen Spezies möglich. Es wurde im Rahmen dieser Arbeit auch der Einfluss möglicher Empfindlichkeitsänderungen des ICP-Q-MS durch koeluierende Kohlenwasserstoffe überprüft, wobei diese erwartungsgemäß auf das Ergebnis der spezies-spezifischen und spezies-unspezifischen GC-ICP-Q-MSIVA keinerlei Einfluss haben. Der zweite Hauptschwerpunkt der Arbeit lag auf der Ausarbeitung routinefähiger, schneller und zuverlässiger Methoden zur Gesamtelementspurenanalytik von Schwefel und Schwermetallen in Erdölen und Petroprodukten. Für die Gesamtschwefelanalyse wurde eine MSIVA nach thermaler Verdampfung mit 34S-markierten Dibenzothiophen als Indikator entwickelt. Die neu entwickelte Methode erlaubt eine sehr schnelle Bestimmung des Gesamtschwefelgehalts, wobei die eigentliche Messung des Isotopenverhältnisses innerhalb von Sekunden nach der Injektion der Probe erfolgt. Weiterhin zeichnet sich die Methode durch Robustheit und eine niedrige Nachweisgrenze (40 ng S/g) aus. Für die Analyse von Schwermetallen wurden erstmals Möglichkeiten einer direkten MSIVA von Erdölproben ohne zeitraubenden, kontaminationsträchtigen Aufschluss bzw. die schwierige Erzeugung einer Mikroemulsion zwischen hydrophober Probe und wässrigem Indikator entwickelt. Um eine homogene Verteilung des Indikators in der hydrophoben Probe zu ermöglichen, musste ausgehend von den zur Verfügung stehenden wässrigen Indikatorlösungen, eine Überführung des Indikators in ein organisches Lösungsmittel erfolgen. Hierzu wurde der jeweilige Metallindikator unter Komplexierung aus wässrigen Metallindikatorlösungen extrahiert. Für die Analyse der mit diesen Indikatorlösungen in organischer Phase versetzten Proben wurden zwei alternative Methoden ausgearbeitet. Bei der mit der Laserablation (LA) kombinierten ICP-SF-MSIVA wird die isotopenverdünnte Probe aus einer eigens für diesen Zweck entwickelten Probenhalterung ablatiert und so dem ICP-SF-MS zugeführt wird. Bei zeitlich sich verändernden Intensitäten der gemessenen Isotope werden aber reproduzierbare und konstante Isotopenverhältnisse erhalten. Im Falle einer homogenen Verteilung der Metallspuren wurde eine hervorragende Übereinstimmung mit Vergleichsmethoden und einem Referenzmaterial festgestellt. Im Falle einer heterogenen partikulären Verteilung der Metallspuren, wie sie z.B. bei Eisenspuren in den Erdölen vorlag, ist die Anwendbarkeit der LA-ICP-SF-MSIVA aufgrund des kleinen Probenvolumens (20 µL) jedoch begrenzt. Als Alternative zur LA-ICP-SF-MSIVA wurde ein System unter Verwendung der Fließinjektion für die Zuführung der isotopenverdünnten Probe zum ICP-SF-MS ausgearbeitet. Die isotopenverdünnte Probe wird hierbei in einen Eluentenstrom von Toluol injiziert und mit Hilfe einer Total-Consumption-Zerstäuber/Sprühkammer-Einheit vollständig bei einer Flussrate von 10 µL/min in das Plasma eingebracht. Neben einer nochmaligen Verkürzung der Analysenzeit und Vereinfachung der Probenvorbereitung bietet diese Methode zusätzlich stark verbesserte Nachweisgrenzen (z.B. Ni 0,9 ng/g). Leider sind mit diesem Verfahren bis jetzt nur Ni und Mo zuverlässig bestimmbar. Das in dieser Arbeit ausgearbeitete Methodenpaket erlaubt erstmals eine breite Einführung der ICP-MSIVA als zuverlässige Methode in die Routineanalytik der Petroindustrie. Durch die bewiesene Zuverlässigkeit, den geringen Zeitaufwand und die Robustheit der Methoden steht ihrem routinemäßigen Einsatz, außer einer weitergehenderen Automatisierung einzelner Verfahrensteile, prinzipiell nichts entgegen.

Polycyclic aromatic hydrocarbons (PAHs) in river bank soils

Polycyclic aromatic hydrocarbons (PAHs) are ubiquitous and found in the atmosphere, aquatic environment, sediments and soils. For environmental risk assessments and the allocation of the polluter it is important to know the PAH sources. PAH contamination sites are usually the result of anthropogenic processes. Three major sources are known: i) petroleum, including crude oil and its refined products and coals (petrogenic PAHs), ii) burning of organic matter (pyrogenic PAHs) and iii) transformation products of natural organic precursors present in the environment (diagenetic processes). In one case elevated PAH concentrations were found in river bank soils when building a retention area along the Mosel River. The source of the PAHs in this area was unclear and required the investigation of possible sources. To evaluate the PAH distribution along the Mosel River, a section of ~ 160 km along the river and a short section along the Saar River were investigated within this study. Concentrations of the Σ16 EPA PAHs were as high as 81 mg kg-1 dry weight (dw). Additionally, coal particles were identified in some soils, which originated from mining activities in the Saarland region. PAH distribution patterns of the 16 EPA PAHs suggest a mainly pyrogenic origin and in some cases a mixture of pyrogenic and petrogenic origin. For a comprehensive investigation five sampling sites were selected. Two sites were located before the confluence of the Mosel and Saar River, one site at the confluence and two sites after the confluence. The examination included typical forensic methods such as PAH distribution patterns of 45 PAHs (including alkylated PAHs), calculation of PAH ratios, determination of PAH alkyl homologues, n-alkanes, principal component analysis (PCA) and coal petrography. The results revealed a mainly pyrogenic source at sampling sites before the confluence of the two rivers. At and after the confluence, a mixture of pyrogenic and petrogenic inputs were present. With the help of coal petrography, coal derived particles could be identified in these soils. Therefore, coal was suggested to be the petrogenic source. It could be shown that sites with diffuse sources of contaminants, like the bank soils of the Mosel River, are difficult to characterize. As previously mentioned for detailed source identifications, the use of various forensic methods is essential. Determination of PAH alkyl homologue series, biomarkers and isotopes are often recommended. Source identification was evaluated using three different methods (i.e. PAH distribution patterns of an extended PAH spectrum, PAH ratios and analyses of n-alkanes). It was assessed if these methods were sufficient for the initial steps in identifying sources of PAHs in selected samples, and if they could be used for decision-making purposes. Point- and non-point sources were identified by applying the three methods and it could be shown that these relatively simple methods are sufficient in determining the primary source. In a last step of this study two soils (one before the confluence of the Mosel and Saar rivers and one after the confluence), and one sediment of the Mosel River were evaluated by investigating the mutagenic potential of the soils and the sediment with a fluctuation version of the Ames-test. The study showed that coal bearing soils at the Mosel River do not exhibit a greater mutagenic potential than other soils or sediments without coal particles.

New catalytic processes for the upgrading of furfural and 5-hydroxymethylfurfural to chemicals and fuels

The demand of energy, fuels and chemicals is increasing due to the strong growth of some countries in the developing world and the development of the world economy. Unfortunately, the general picture derived sparked an exponential increase in crude oil prices with a consequent increase of the chemical, by-products and energy, depleting the global market. Nowadays biomass are the most promising alternative to fossil fuels for the production of chemicals and fuels. In this work, the development of three different catalytic processes for the valorization of biomass-derived has been investigated. 5-hydroxymethylfurfural oxidation was studied under mild reaction condition using gold and gold/copper based catalysts synthetized from pre-formed nanoparticles and supported onto TiO2 and CeO2. The analysis conducted on catalysts showed the formation of alloys gold/copper and a strong synergistic effect between the two metals. For this reason the bimetallic catalysts supported on titania showed a higher catalytic activity respect to the monometallic catalysts. The process for the production of 2,5-bishydroxymethyl furan (BHMF) was also optimized by means the 5-hydroxymethylfurfural hydrogenation using the Shvo complex. Complete conversion of HMF was achieved working at 90 °C and 10 bar of hydrogen. The complex was found to be re-usable for at least three catalytic cycles without suffering any type of deactivation. Finally, the hydrogenation of furfural and HMF was carried out, developing the process of hydrogen transfer by using MgO as a catalyst and methanol as a hydrogen donor. Quantitative yields to alcohols have been achieved in a few hours working in mild condition: 160 °C and at autogenous pressure. The only by-products formed were light products such as CO, CO2 and CH4 (products derived from methanol transformation), easily separable from the reaction solution depressurizing the reactor.

The Intersection of Economics and Politics in a Small OPEC Country: the Case of Ecuador, 1990 - March 2014

Today, crude oil remains a vital resource all around the world. This non-renewable resource powers countries worldwide. Besides serving as an energy source, crude oil is also the most important component for different world economies, especially in developing countries. Ecuador, a small member of the OPEC oil cartel, presents a case where its economy is oil dependent. A great percentage of the country¿s GDP and government¿s budget comes from oil revenues. Ecuador has always been a primary exporter of raw materials. In the last centuries, the country experienced three important economic booms: cacao, bananas, and, ultimately, crude oil. In this sense, the country has not been able to fully industrialize and begin to export manufactured goods, i.e., Ecuador suffers from the Dutch disease. The latter has deterred Ecuador from achieving broad-based economic development. Given crude oil¿s importance for the Ecuadorian economy, the government has always tried to influence the oil industry in search of profits and benefits. Therefore, this thesis, explores the question: how and to what extent have political interventions affected the oil industry in Ecuador from 1990 until March 2014? In general, this thesis establishes an economic history context during the last twenty-four years, attempting to research how political interventions have shaped Ecuador¿s oil industry and economy. In the analysis, it covers a period where political instability prevailed, until Rafael Correa became president. The thesis examines Ecuador¿s participation in OPEC, trying to find explanations as to why the country voluntarily left the organization in 1992, only to rejoin in 2007 when Correa rose to power. During the ¿Revolución Ciudadana¿ period, the thesis researches reforms to the Law of Hydrocarbons, variations in the relations with other nations, the controversy surrounding the Yasuní-ITT oil block, and the ¿Refinería del Pacífico¿ construction. The thesis is an Industrial Organization detailed case study that analyzes, updates, and evaluates the intersection of economics and politics in Ecuador¿s crude oil industry during the last 24 years. In this sense I have consulted past theses, newspaper articles, books, and other published data about the petroleum industry, both from a global and Ecuadorian perspective. In addition to published sources, I was able to interview sociologists, public figures, history and economics academics, and other experts, accessing unique unpublished data about Ecuador¿s oil industry. I made an effort to collect information that shows the private and public side of the industry, i.e., from government-related and independent sources. I attempted to remain as objective as possible to make conclusions about the appropriate Industrial Organization policy for Ecuador¿s oil industry, addressing the issue from an economic, social, political, and environmental point of view. I found how Ecuador¿s political instability caused public policy to fail, molding the conduct and market structure of the crude oil industry. Throughout history, developed nations have benefited from low oil prices, but things shifted since oil prices began to rise, which is more beneficial for the developing nations that actually possess and produce the raw material. Nevertheless, Ecuador, a victim of the Dutch disease due to its heavy reliance on crude oil as a primary product, has not achieved broad-based development.

Patentability and Scope of Protection for DNA Sequence

Since the mapping of the human genome and the technical innovations in the field of biotechnology, patent law has gone through great controversies. Protection is required for an investor to make an investment but how broad should the given protection be? Whether the invention is a mi- cro-organism capable of dissolving crude oil, or the gene of a soya plant, the genetic engineering required for their production entails vast amounts of capi- tal. The policy in that respect is tailored by legislative acts and judicial decisions, ensuring a fair balance be- tween the interests of patent right holders and third parties. However, the policy differs from jurisdiction to jurisdiction, thus creating inconsistencies with re- gards to the given protection to the same invention, and as a result this could deter innovation and pro- mote stagnation. The most active actors shaping the patent policy on an international level are the patent offices of the United States of America, Japan and the European Patent Organization. These three patent offices have set up a cooperation programme in order to promote and improve efficiency with regards to their patent policies on a global scale. However, recent judicial de- velopments have shown that the policy in respect to the field of biotechnology differs between the patent regimes of the United States of America and the two- layer system of the European Patent Organisation/ the European Union.

Beyond biofuels: jatropha’s multiple uses for farmers in East Africa

The jatropha plant produces seeds containing 25–40% oil by weight. This oil can be made into biodiesel. During the recent global fuel crisis, the price of crude oil peaked at over USD 130 per barrel. Jatropha attracted huge interest – it was touted as a wonder crop that could generate biodiesel oil on “marginal lands” in semi-arid areas. Its promise appeared especially great in East Africa. Today, however, jatropha’s value in East Africa appears to lie primarily in its multipurpose use by small-scale farmers, not in large-scale biofuel production.

Production of Ethanol from Hardwood

Diminishing crude oil and natural gas supplies, along with concern about greenhouse gas are major driving forces in the search for efficient renewable energy sources. The conversion of lignocellulosic biomass to energy and useful chemicals is a component of the solution. Ethanol is most commonly produced by enzymatic hydrolysis of complex carbohydrates to simple sugars followed by fermentation using yeast. C6Hl0O5 + H2O −Enxymes→ C6H12O6 −Yeast→ 2CH3CH2OH + 2C02 In the U.S. corn is the primary starting raw material for commercial ethanol production. However, there is insufficient corn available to meet the future demand for ethanol as a gasoline additive. Consequently a variety of processes are being developed for producing ethanol from biomass; among which is the NREL process for the production of ethanol from white hardwood. The objective of the thesis reported here was to perform a technical economic analysis of the hardwood to ethanol process. In this analysis a Greenfield plant was compared to co-locating the ethanol plant adjacent to a Kraft pulp mill. The advantage of the latter case is that facilities can be shared jointly for ethanol production and for the production of pulp. Preliminary process designs were performed for three cases; a base case size of 2205 dry tons/day of hardwood (52 million gallons of ethanol per year) as well as the two cases of half and double this size. The thermal efficiency of the NREL process was estimated to be approximately 36%; that is about 36% of the thermal energy in the wood is retained in the product ethanol and by-product electrical energy. The discounted cash flow rate of return on investment and the net present value methods of evaluating process alternatives were used to evaluate the economic feasibility of the NREL process. The minimum acceptable discounted cash flow rate of return after taxes was assumed to be 10%. In all of the process alternatives investigated, the dominant cost factors are the capital recovery charges and the cost of wood. The Greenfield NREL process is not economically viable with the cost of producing ethanol varying from $2.58 to $2.08/gallon for the half capacity and double capacity cases respectively. The co-location cases appear more promising due to reductions in capital costs. The most profitable co-location case resulted in a discounted cash flow rate of return improving from 8.5% for the half capacity case to 20.3% for the double capacity case. Due to economy of scale, the investments become more and more profitable as the size of the plant increases. This concept is limited by the amount of wood that can be delivered to the plant on a sustainable basis as well as the demand for ethanol within a reasonable distance of the plant.

PM2.5, PM10, and PM10-associated elements in the air in Bamako, Mali (2012-2013)

Saharan dust incursions and particulates emitted from human activities degrade air quality throughout West Africa, especially in the rapidly expanding urban centers in the region. Particulate matter (PM) that can be inhaled is strongly associated with increased incidence of and mortality from cardiovascular and respiratory diseases and cancer. Air samples collected in the capital of a Saharan-Sahelian country (Bamako, Mali) between September 2012 - July 2013 were found to contain inhalable PM concentrations that exceeded World Health Organization (WHO) and US Environmental Protection Agency (USEPA) PM2.5 and PM10 24-h limits 58 - 98% of days and European Union (EU) PM10 24-h limit 98% of days. Mean concentrations were 1.2-to-4.5 fold greater than existing limits. Inhalable PM was enriched in transition metals, known to produce reactive oxygen species and initiate the inflammatory reaction, and other potentially bioactive and biotoxic metals/metalloids. Eroded mineral dust composed the bulk of inhalable PM, whereas most enriched metals/metalloids were likely emitted from oil combustion, biomass burning, refuse incineration, vehicle traffic, and mining activities. Human exposure to inhalable PM and associated metals/metalloids over 24-h was estimated. The findings indicate that inhalable PM in the Sahara-Sahel region may present a threat to human health, especially in urban areas with greater inhalable PM and transition metal exposure.