An investigation of the direct extrusion process with the application of oscillatory energy

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Role of oxidation-reduction cycle of iron in direct leaching of zinc concentrate

Direct leaching is an alternative to conventional roast-leach-electrowin (RLE) zinc production method. The basic reaction of direct leach method is the oxidation of sphalerite concentrate in acidic liquid by ferric iron. The reaction mechanism and kinetics, mass transfer and current modifications of zinc concentrate direct leaching process are considered. Particular attention is paid to the oxidation-reduction cycle of iron and its role in direct leaching of zinc concentrate, since it can be one of the limiting factors of the leaching process under certain conditions. The oxidation-reduction cycle of iron was experimentally studied with goal of gaining new knowledge for developing the direct leaching of zinc concentrate. In order to obtain this aim, ferrous iron oxidation experiments were carried out. Affect of such parameters as temperature, pressure, sulfuric acid concentration, ferrous iron and copper concentrations was studied. Based on the experimental results, mathematical model of the ferrous iron oxidation rate was developed. According to results obtained during the study, the reaction rate orders for ferrous iron concentration, oxygen concentration and copper concentration are 0.777, 0.652 and 0.0951 respectively. Values predicted by model were in good concordance with the experimental results. The reliability of estimated parameters was evaluated by MCMC analysis which showed good parameters reliability.

Simulation of hydrogen peroxide direct synthesis in a microreactor

A set of models in Aspen plus was built to simulate the direct synthesis process of hydrogen peroxide in a micro-reactor system. This process model can be used to carry out material balance calculation under various experimental conditions. Three thermodynamic property methods were compared by calculating gas solubility and Uniquac-RK method was finally selected for process model. Two different operation modes with corresponding operation conditions were proposed as the starting point of future experiments. Simulations for these two modes were carried out to get the information of material streams. Moreover, some hydrodynamic parameters such as gas/liquid superficial velocity, gas holdup were also calculated with improved process model. These parameters proved the proposed experimental conditions reasonable to some extent. The influence of operation conditions including temperature, pressure and circulation ratio was analyzed for the first operation mode, where pure oxygen was fed into dissolving tank and hydrogen-carbon dioxide mixture was fed into microreactor directly. The preferred operation conditions for the system are low temperature (2°C) and high pressure (30 bar) in dissolving tank. High circulation ratio might be good in the sense that more oxygen could be dissolved and fed into reactor for reactions, but meanwhile hydrodynamics of microreactor should be considered. Furthermore, more operation conditions of reactor gas/liquid feeds in both of two operation modes were proposed to provide guidance for future experiment design and corresponding hydrodynamic parameters were also calculated. Finally, safety issue was considered from thermodynamic point of view and there is no explosion danger at given experimental plan since the released reaction heat will not cause solvent vaporization inside the microchannels. The improvement of process model still needs further study based on the future experimental results.

Safety study of hydrogen peroxide direct synthesis

Kandidaatintyön johdantokappaleessa esitellään vetyperoksidi ja mihin sitä käytetään teollisuudessa. Työssä vertaillaan antrakinoniprosessia ja suoraa prosessia sekä selvitetään nykyisin enemmän vetyperoksidituotantoon käytetyn antrakinoniprosessin ongelmakohdat ja osoitetaan, miksi suora synteesi vetyperoksidin tuotannossa olisi parempi vaihtoehto. Kandidaatintyön käsittelee suurilta osin turvallisuusongelmia, joita esiintyy suoran synteesin yhteydessä. Kirjallisuudesta on etsitty ratkaisuja näihin ongelmiin, kuten membraaniprosessin käyttöä räjähdysvaaran välttämiseksi. Pienemmän reaktorin eli ns. mikroreaktorin käyttö tuo mukanaan monia etuja vetyperoksidin tuotantoon. Tällöin prosessi on turvallisempi ja sitä on helpompi hallita. Mikroreaktorissa voidaan käyttää korkeampia lämpötiloja ja paineita kuin makroreaktorilla ilman, että räjähdysvaara prosessissa kasvaisi. Mikroreaktorin sisällä olevat mikrokanavat luovat turvallisen ympäristön synteesille. Aspen plus – simulointiohjelmalla mallinnettiin ja simulointiin suoran prosessin kriittisiä virtoja mikroreaktorissa. Tarkoituksena oli löytää virrat, joissa kulkee mahdollisesti räjähtävä kaasuseos. Kaasumaiset prosessivirrat ovat kriittisimmät vetyperoksidin suorassa synteesissä, koska ne aiheuttavat todennäköisemmin räjähdyksen kuin nestemäiset prosessivirrat. Kaikkein eniten prosessiturvallisuutta uhkaavat ainevirrat ennen ja jälkeen mikroreaktoria.

Direct functionalization of heterocyclic and non-heterocyclic arenes

L’application des métaux de transition à la fonctionnalisation directe a ouvert la voie à une nouvelle classe de réactions pour la formation de liens carbone-carbone. De par l'omniprésence des liaisons C–H, l’introduction de nouvelles fonctionnalités chimiques par voie directe et pré-activation minimale s’impose comme une stratégie de synthèse très attrayante. Ainsi, il est envisageable de préparer de manière rapide et efficace des supports complexes menant à des molécules complexes, qui pourraient être utiles dans divers domaines de la chimie. L'objectif principal de la présente thèse vise la fonctionnalisation directe des arènes hétérocycliques et non hétérocycliques et, plus précisément, les techniques d’arylation. Dans un premier temps, nous allons aborder le thème de l’arylation directe tout en mettant l’accent sur les pyridines (Chapitre 1). Ces molécules sont à la base d'une multitude de composés biologiquement actifs et jouent un rôle important dans le domaine des sciences des matériaux, de l’agrochimie et de la synthèse des produits naturels. Dans un deuxième temps, nous discuterons de nos travaux sur l’arylation directe catalysé par un complex de palladium sur des ylures de N-iminopyridinium en soulignant la dérivatisation du sel de pyridinium après une phénylation sp2 (Chapitre 2). L’étude de ce procédé nous a permis de mettre en lumière plusieurs découvertes importantes, que nous expliquerons en détails une à une : l’arylation benzylique directe lorsque des ylures N-iminopyridinium substituées avec un groupement alkyl à la position 2 sont utilisés comme partenaires dans la réaction; les allylations Tsuji-Trost catalysée par un complex de palladium; et l’alkylation directe et sans métal via une catalyse par transfert de phase. Plusieurs défis restent à relever pour le développement de procédés directs utilisant des métaux de transition peu coûteux, d’autant plus que la synthèse par transformation directe des pyridines 2-alcényles, lesquelles sont pertinentes sur le plan pharmacologique, n’a pas encore été rapportée à ce jour. Avec cette problématique en tête, nous avons réussi à mettre au point une alcénylation directe catalysé par un complex de cuivre sur des ylures de N-iminopyridinium. Nous discuterons également d’une nouvelle méthode pour la préparation des iodures de vinyle utilisés dans les couplages. Ces réactions sont non seulement remarquablement chimiosélectives, mais sont aussi applicables à plusieurs substrats (Chapitre 3). En optimisant ce procédé direct, nous avons découvert une façon unique de synthétiser les pyrazolo[1,5-a]pyridines 2-substituées (Chapitre 4). Le mécanisme global met en jeu une séquence tandem de fonctionnalisation-cyclisation directe et un procédé direct en cascade, qui n’avais jamais été rapporté. Cela simplifie ansi la synthèse autrement compliquée de ces substrats en y apportant une solution à un problème de longue date. Dans les deux derniers chapitres, nous examinerons en détail les techniques d’arylation directe qui n'impliquent pas les partenaires de couplage hétérocycliques. Entre autres, au Chapitre 5, nous soulignerons notre découverte d’un umpolung dirigé et catalysé par un complexe de palladium du benzène et de quelques autres dérivés arènes. Il s’agit là du premier cas de fonctionnalisation directe dans laquelle le groupe directeur se trouve sur le partenaire halogène et il s’ajoute à la courte liste d’exemples connus dans la littérature rapportant une arylation directe du benzène. Finalement, au Chapitre 6, nous passerons en revue une nouvelle arylation directe catalysée au fer, qui se veut un procédé peu coûteux, durable et présentant une économie d’atomes. Nous discutons des substrats possibles ainsi des études mécanistiques réalisés.

Site-selective direct arylation of unprotected adenine nucleosides mediated by palladium and copper:insights into the reaction mechanism

Reaction conditions facilitating the site-selective direct aryl functionalisation at the C-8 position of adenine nucleosides have been identified. Many different aromatic components may be effectively cross-coupled to provide a diverse array of arylated adenine nucleoside products without the need for ribose or adenine protecting groups. The optimal palladium catalyst loading lies between 0.5 and 5 mol %. Addition of excess mercury to the reaction had a negligible affect on catalysis, suggesting the involvement of a homogeneous catalytic species. A study by transmission electron microscopy (TEM) shows that metal containing nanoparticles, ca. 3 nm with good uniformity, are formed during the latter stages of the reaction. Stabilised PVP palladium colloids (PVP=N-polyvinylpyrrolidone) are catalytically active in the direct arylation process, releasing homogenous palladium into solution. The effect of various substituted 2-pyridine ligand additives has been investigated. A mechanism for the site-selective arylation of adenosine is proposed. © 2008 Elsevier Ltd. All rights reserved.

Microstructure and texture assessment of Al-Mn-Fe-Si (3003) aluminum alloy produced by continuous and semicontinuous casting processes

Aluminum sheets are currently produced by the direct-chill process (DC). The need for low-cost aluminum sheets is a challenge for the development of new materials produced by the twin roll caster (TRC) process. It is expected that sheets produced from these different casting procedures will differ in their microstructure. These differences in microstructure and in the crystallographic texture have great impact on sheet mechanical properties and formability. The present study investigated microstructure and evaluated texture of two strips of Al-Mn-Fe-Si (3003) aluminum alloy produced by TRC and by hot-rolling processes. It was possible to notice that the microstructure, morphology, and grain size of the TRC sample were more homogenous than those found in hot-rolled samples. Both strips, obtained by the two processes, showed strong texture gradient across the thickness.

Viewpoints and goals: towards an integrated approach

Dissertação de Mestrado em Engenharia Informática

Towards sustainable Iron- and steelmaking with economic optimization

The iron and steelmaking industry is among the major contributors to the anthropogenic emissions of carbon dioxide in the world. The rising levels of CO2 in the atmosphere and the global concern about the greenhouse effect and climate change have brought about considerable investigations on how to reduce the energy intensity and CO2 emissions of this industrial sector. In this thesis the problem is tackled by mathematical modeling and optimization using three different approaches. The possibility to use biomass in the integrated steel plant, particularly as an auxiliary reductant in the blast furnace, is investigated. By pre-processing the biomass its heating value and carbon content can be increased at the same time as the oxygen content is decreased. As the compression strength of the preprocessed biomass is lower than that of coke, it is not suitable for replacing a major part of the coke in the blast furnace burden. Therefore the biomass is assumed to be injected at the tuyere level of the blast furnace. Carbon capture and storage is, nowadays, mostly associated with power plants but it can also be used to reduce the CO2 emissions of an integrated steel plant. In the case of a blast furnace, the effect of CCS can be further increased by recycling the carbon dioxide stripped top gas back into the process. However, this affects the economy of the integrated steel plant, as the amount of top gases available, e.g., for power and heat production is decreased. High quality raw materials are a prerequisite for smooth blast furnace operation. High quality coal is especially needed to produce coke with sufficient properties to ensure proper gas permeability and smooth burden descent. Lower quality coals as well as natural gas, which some countries have in great volumes, can be utilized with various direct and smelting reduction processes. The DRI produced with a direct reduction process can be utilized as a feed material for blast furnace, basic oxygen furnace or electric arc furnace. The liquid hot metal from a smelting reduction process can in turn be used in basic oxygen furnace or electric arc furnace. The unit sizes and investment costs of an alternative ironmaking process are also lower than those of a blast furnace. In this study, the economy of an integrated steel plant is investigated by simulation and optimization. The studied system consists of linearly described unit processes from coke plant to steel making units, with a more detailed thermodynamical model of the blast furnace. The results from the blast furnace operation with biomass injection revealed the importance of proper pre-processing of the raw biomass as the composition of the biomass as well as the heating value and the yield are all affected by the pyrolysis temperature. As for recycling of CO2 stripped blast furnace top gas, substantial reductions in the emission rates are achieved if the stripped CO2 can be stored. However, the optimal recycling degree together with other operation conditions is heavily dependent on the cost structure of CO2 emissions and stripping/storage. The economical feasibility related to the use of DRI in the blast furnace depends on the price ratio between the DRI pellets and the BF pellets. The high amount of energy needed in the rotary hearth furnace to reduce the iron ore leads to increased CO2 emissions.

Fabrication and integration of planar electrodes for contactless conductivity detection on polyester-toner electrophoresis microchips

In this report, we describe the microfabrication and integration of planar electrodes for contactless conductivity detection on polyester-toner (PT) electrophoresis microchips using toner masks. Planar electrodes were fabricated by three simple steps: (i) drawing and laser-printing the electrode geometry on polyester films, (ii) sputtering deposition onto substrates, and (iii) removal of toner layer by a lift-off process. The polyester film with anchored electrodes was integrated to PT electrophoresis microchannels by lamination at 120 degrees C in less than 1 min. The electrodes were designed in an antiparallel configuration with 750 mu m width and 750 gm gap between them. The best results were recorded with a frequency of 400 kHz and 10 V-PP using a sinusoidal wave. The analytical performance of the proposed microchip was evaluated by electrophoretic separation of potassium, sodium and lithium in 150 mu m wide x 6 mu m deep microchannels. Under an electric field of 250 V/cm the analytes were successfully separated in less than 90 s with efficiencies ranging from 7000 to 13 000 plates. The detection limits (S/N = 3) found for K+, Na+, and Li+ were 3.1, 4.3, and 7.2 mu mol/L, respectively. Besides the low-cost and instrumental simplicity, the integrated PT chip eliminates the problem of manual alignment and gluing of the electrodes, permitting more robustness and better reproducibility, therefore, more suitable for mass production of electrophoresis microchips.

Dynamic Solid Phase DNA Extraction and PCR Amplification in Polyester-Toner Based Microchip

A variety of substrates have been used for fabrication of microchips for DNA extraction, PCR amplification, and DNA fragment separation, including the more conventional glass and silicon as well as alternative polymer-based materials. Polyester represents one such polymer, and the laser-printing of toner onto polyester films has been shown to be effective for generating polyester-toner (PeT) microfluidic devices with channel depths on the order of tens of micrometers. Here, we describe a novel and simple process that allows for the production of multilayer, high aspect-ratio PeT microdevices with substantially larger channel depths. This innovative process utilizes a CO(2) laser to create the microchannel in polyester sheets containing a uniform layer of printed toner, and multilayer devices can easily be constructed by sandwiching the channel layer between uncoated cover sheets of polyester containing precut access holes. The process allows the fabrication of deep channels, with similar to 270 mu m, and we demonstrate the effectiveness of multilayer PeT microchips for dynamic solid phase extraction (dSPE) and PCR amplification. With the former, we found that (i) more than 65% of DNA from 0.6 mu L of blood was recovered, (ii) the resultant DNA was concentrated to greater than 3 ng/mu L., (which was better than other chip-based extraction methods), and (iii) the DNA recovered was compatible with downstream microchip-based PCR amplification. Illustrative of the compatibility of PeT microchips with the PCR process, the successful amplification of a 520 bp fragment of lambda-phage DNA in a conventional thermocycler is shown. The ability to handle the diverse chemistries associated with DNA purification and extraction is a testimony to the potential utility of PeT microchips beyond separations and presents a promising new disposable platform for genetic analysis that is low cost and easy to fabricate.

Comparison of the analytical performance of electrophoresis microchannels fabricated in PDMS, glass, and polyester-toner

This paper compares the analytical performance of microchannels fabricated in PDMS, glass, and polyester-toner for electrophoretic separations. Glass and PDMS chips were fabricated using well-established photolithographic and replica-molding procedures, respectively. PDMS channels were sealed against three different types of materials: native PDMS, plasma-oxidized PDMS, and glass. Polyester-toner chips were micromachined by a direct-printing process using an office laser printer. All microchannels were fabricated with similar dimensions according to the limitations of the direct-printing process (width/depth 150 mu m/12 mu m). LIF was employed for detection to rule out any losses in separation efficiency due to the detector configuration. Two fluorescent dyes, coumarin and fluorescein, were used as model analytes. Devices were evaluated for the following parameters related to electrophoretic separations: EOF, heat dissipation, injection reproducibility, separation efficiency, and adsorption to channel wall.

Bothropoides insularis venom cytotoxicity in renal tubular epithelia cells

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Disposable polyester-toner electrophoresis microchips for DNA analysis

Microchip electrophoresis has become a powerful tool for DNA separation, offering all of the advantages typically associated with miniaturized techniques: high speed, high resolution, ease of automation, and great versatility for both routine and research applications. Various substrate materials have been used to produce microchips for DNA separations, including conventional (glass, silicon, and quartz) and alternative (polymers) platforms. In this study, we perform DNA separation in a simple and low-cost polyester-toner (PeT)-based electrophoresis microchip. PeT devices were fabricated by a direct-printing process using a 600 dpi-resolution laser printer. DNA separations were performed on PeT chip with channels filled with polymer solutions (0.5% m/v hydroxyethylcellulose or hydroxypropylcellulose) at electric fields ranging from 100 to 300Vcm(-1). Separation of DNA fragments between 100 and 1000 bp, with good correlation of the size of DNA fragments and mobility, was achieved in this system. Although the mobility increased with increasing electric field, separations showed the same profile regardless of the electric field. The system provided good separation efficiency (215 000 plates per m for the 500 bp fragment) and the separation was completed in 4 min for 1000 bp fragment ladder. The cost of a given chip is approximately $0.15 and it takes less than 10 minutes to prepare a single device.

Synthese und Charakterisierung von Polymethylmethacrylat (PMMA)-Silika-Komposit-Partikeln und fluorierten Nanopartikeln unter Verwendung des Miniemulsionsprozesses

In der vorliegenden Dissertation wurden zwei verschiedene Fragestellungen bearbeitet. Zum einen wurde im Rahmen des Schwerpunktprojektes „Kolloidverfahrenstechnik“ und in Zusammenarbeit mit der Arbeitsgruppe von Prof. Dr. Heike Schuchmann vom KIT in Karlsruhe die Verkapselung von Silika-Nanopartikeln in eine PMMA-Hülle durch Miniemulsionspolymerisation entwickelt und der Aufskalierungsprozess unter Verwendung von Hochdruckhomogenisatoren vorangetrieben. Zum anderen wurden verschiedene fluorierte Nanopartikel durch den Miniemulsionsprozess generiert und ihr Verhalten in Zellen untersucht.rnSilika-Partikel konnten durch Miniemulsionspolymerisation in zwei unterschiedlichen Prozessen erfolgreich verkapselt werden. Bei der ersten Methode wurden zunächst modifizierte Silika-Partikel in einer MMA-Monomerphase dispergiert und anschließend durch den normalen Miniemulsionsprozess Silika-beladene Tröpfchen generiert. Diese konnten zu Komposit-Partikeln polymerisiert werden. Bei der Verkapselung durch den Fission/Fusion Prozess wurden die hydrophobisierten Silika-Partikel durch Fission und Fusion Prozesse in schon vorhandene Monomertröpfchen eingebracht, welche hinterher polymerisiert wurden. Um hydrophiles Silika in einem hydrophoben Monomer zu dispergieren, musste zunächst eine Modifizierung der Silika-Partikel stattfinden. Dies geschah unter anderem über eine chemische Anbindung von 3-Methacryloxypropyltri-methoxysilan an der Oberfläche der Silika-Partikel. Des Weiteren wurden die hydrophilen Silika-Partikel durch Adsorption von CTMA-Cl physikalisch modifiziert. Unter anderem durch die Variation des Verkapselungsprozesses, der Silika-Menge, der Tensidart und –menge und der Comonomere konnten Komposit-Partikel mit unterschiedlichen Morphologien, Größen, und Füllgraden erhalten werden.rnFluorierte Nanopartikel wurden erfolgreich über den Prozess der Miniemulsionspolymerisation synthetisiert. Als Monomere dienten dabei fluorierte Acrylate, fluorierte Methacrylate und fluoriertes Styrol. Es war möglich aus jeder dieser drei Gruppen an Monomeren fluorierte Nanopartikel herzustellen. Für genauere Untersuchungen wurden 2,3,4,5,6-Pentafluorstyrol, 3,3,4,4,5,5,6,6,7,7,8,8,9,9,10,10,10-Heptadecafluorodecyl-methacrylat und 1H,1H,2H,2H-Perfluorodecylacrylat als Monomere ausgewählt. Als Hydrophob zur Unterdrückung der Ostwaldreifung wurde Perfluromethyldecalin eingesetzt. Die stabilsten Miniemulsionen wurden wiederum mit den ionischen Tensid SDS generiert. Mit steigendem Gehalt an SDS gelöst in der kontinuierlichen Phase, wurde eine Verkleinerung der Partikelgröße festgestellt. Neben den Homopolymerpartikeln wurden auch Copolymerpartikel mit Acrylsäure erfolgreich synthetisiert. Zudem wurde noch das Verhalten der fluorierten Partikel in Zellen überprüft. Die fluorierten Partikel wiesen ein nicht toxisches Verhalten vor. Die Adsorption von Proteinen aus Humanem Serum wurde über ITC Messungen untersucht. rnSomit konnte gezeigt werden, dass die Technik der Miniemulsionspolymerisation eine abwechslungsreiche und effektive Methode ist, um Hybridnanopartikel mit verschiedenen Morphologien und oberflächenfunktionalisierte Nanopartikel erfolgreich zu generieren.rn