Pilas de combustible de una sola camara, basadas en electrolitos de ceria dopada con gadolinia y operadas con metano y propano

La principal ventaja de las pilas de combustible de óxido sólido (SOFCs) de una sola cámara, frente a las bicamerales convencionales, es que permiten simplificar el diseño del dispositivo y operar con mezclas de hidrocarburos (metano, propano...) y aire, sin necesidad de separar ambos gases, por medio del uso de electrodos selectivos a la oxidación del combustible y reducción del oxidante. En el presente trabajo, se han fabricado monopilas soportadas sobre electrolitos de ceria dopada con gadolinia (GDC), de 200 ¿m de espesor, usando Ni-GDC como ánodo y LSC(La0.5Sr0.5CoO3-¿)-GDC-Ag2O como cátodo. Las propiedades eléctricas de la celda se determinaron en un reactor de una sola cámara, usando mezclas de metano + aire y propano + aire. Se investigó la influencia de la temperatura, de las presiones parciales del combustible y oxígeno, y de la velocidad de flujo total sobre el rendimiento de las pilas preparadas. Así, la densidad de potencia se incrementó fuertemente con el aumento de la temperatura, la velocidad de flujo total y la composición de hidrocarburo. Una vez se optimizaron los parámetros operacionales, la celda presentó unas densidades de potencia máximas de 70 y 320 mW/ cm2, operando con propano a 600ºC y con metano a 795ºC, respectivamente.

An automated microreactor for semi-continuous biosensor measurements.

Living bacteria or yeast cells are frequently used as bioreporters for the detection of specific chemical analytes or conditions of sample toxicity. In particular, bacteria or yeast equipped with synthetic gene circuitry that allows the production of a reliable non-cognate signal (e.g., fluorescent protein or bioluminescence) in response to a defined target make robust and flexible analytical platforms. We report here how bacterial cells expressing a fluorescence reporter ("bactosensors"), which are mostly used for batch sample analysis, can be deployed for automated semi-continuous target analysis in a single concise biochip. Escherichia coli-based bactosensor cells were continuously grown in a 13 or 50 nanoliter-volume reactor on a two-layered polydimethylsiloxane-on-glass microfluidic chip. Physiologically active cells were directed from the nl-reactor to a dedicated sample exposure area, where they were concentrated and reacted in 40 minutes with the target chemical by localized emission of the fluorescent reporter signal. We demonstrate the functioning of the bactosensor-chip by the automated detection of 50 μgarsenite-As l(-1) in water on consecutive days and after a one-week constant operation. Best induction of the bactosensors of 6-9-fold to 50 μg l(-1) was found at an apparent dilution rate of 0.12 h(-1) in the 50 nl microreactor. The bactosensor chip principle could be widely applicable to construct automated monitoring devices for a variety of targets in different environments.

Projeto e construção de um bioreator para síntese orgânica assimétrica catalisada por saccharomyces cerevisiae (fermento biológico de padaria)

A model for the construction of a simple and cheap apparatus to be used as bioreactor for reactions catalyzed by baker's yeast (Saccharomyces cerevisiae) is described. The bioconversion and separation of cells from products and residual substrates are obtained at the same time. The reactions carried out in this type of reactor are faster than those catalyzed by immobilized cells. Yeast cells can be cultivated in this bioreactor operating with cell recycling at appropriated conditions using glucose and other nutrients.

High voltage discharge for degradation of organic contaminants in water

The pulsed dielectric barrier discharge (PDBD) and pulsed corona discharge (PCD) were compared for their efficiency to degrade phenol in water solution. Results show that PCD has higher efficiency than PDBD to degrade phenol. When initial pH of water solution was elevated, phenol degradation in the PCD reactor was significantly enhanced, although no considerable effect was seen in the PDBD reactor. The PCD reactor was also able to degrade lignin significantly, both in synthetically prepared solution and in pulp and paper mill wastewater. Water temperature did not affect phenol degradation; however, lignin was better oxidized at lower temperature.

Ydinreaktorin painesäiliön ulkoisen jäähdytyksen lämmönsiirtokokeita

The purpose of this work was to design and carry out thermal-hydraulic experiments dealing with overcooling transients of a VVER-440-type nuclear reactor pressure vessel. Sudden overcooling accident could have negative effect on the mechanical strength of the pressure vessel. If part of the pressure vessel is compromised, the intense pressure inside a pressurized water reactor could cause the wall to fracture. Information on the heat transfer along the outside of the pressure vessel wall is necessary for stress analysis. Basic knowledge of the overcooling accident and heat transfer types on the outside of the pressure vessel is presented as background information. Test facility was designed and built based to study and measure heat transfer during specific overcooling scenarios. Two test series were conducted with the first one concentrating on the very beginning of the transient and the second one concentrating on steady state heat transfer. Heat transfer coefficients are calculated from the test data using an inverse method, which yields better results in fast transients than direct calculation from the measurement results. The results show that heat transfer rate varies considerably during the transient, being very high in the beginning and dropping to steady state in a few minutes. The test results show that appropriate correlations can be used in future analysis.

Decomposição catalítica de óleo de soja em presença de diferentes zeólitas

The catalytic decomposition of soybean oil was studied in a fix bed reactor at 673 and 773 K and using amorphous silica-alumina and the zeolites USY, H-Mordenite and H-ZSM-5 as catalysts. Both the selectivity and the catalytic activity were determined by studying the product composition resulting from the chemical reactions. Physicochemical characteristics of the catalysts were obtained by X-ray fluorescence, Fourier Transform infrared spectroscopy, 29Si and 27Al Nuclear Magnetic Ressonance and textural analysis. The zeolites USY and H-ZSM-5, showing higher Brönsted acidity, yielded products with higher concentration in aromatic hydrocarbons, whereas with both H-Mordenite and amorphous silica-alumina the main products were paraffins.

Calcination of aluminum hydroxide over pressure and residence time

This work investigates the possible effect of pressure and residence time to the reaction of aluminum hydroxide into aluminum oxide. Various pressurized conditions are used as well as the help of various residence times. The aim is to increase the conversion of the reaction with the use of different pressures and residence times. The tests were performed with a laboratory scale fluidized bed reactor at the Outotec R&D Center in Frankfurt. Additional test work such as particle size analysis and differential thermal analysis were also carried out. Some calcined samples were also characterized with X-ray diffraction at the University of Auckland to obtain a reaction pathway when using pressurized conditions. All of the results are then compared with previous results.

Titulador potenciométrico automatizado baseado em sistema de fluxo monossegmentado

A new automated system for acid-base flow titrations is proposed. In the operation mode, several sample to titrant volumetric ratios are injected in an air segmented plug. Five three way solenoid valves and three acrilic junctions, assembled in a hidrodynamic injection system, were accountable for the monosegmented reagents plug formation. A turbulent flow reactor was used for a perfect mix of reagents in the plug. The detector system employed a glass combined electrode fitted in an acrilic holder. Titrations of hydrochloric, nitric and acetic acids, in several concentrations, were performed with standard sodium hidroxide, for evaluation of the efficiency of the system. The relative standard deviation of the determinations was about ±0,5% and each titration was carried out in 3-4 minutes. A Quick BASIC 4.5® program was developed for the titrator control.

Modeling reaction kinetics and mass transfer in ozonation in water solutions

This dissertation is based on four articles dealing with modeling of ozonation. The literature part of this considers some models for hydrodynamics in bubble column simulation. A literature review of methods for obtaining mass transfer coefficients is presented. The methods presented to obtain mass transfer are general models and can be applied to any gas-liquid system. Ozonation reaction models and methods for obtaining stoichiometric coefficients and reaction rate coefficients for ozonation reactions are discussed in the final section of the literature part. In the first article, ozone gas-liquid mass transfer into water in a bubble column was investigated for different pH values. A more general method for estimation of mass transfer and Henry’s coefficient was developed from the Beltrán method. The ozone volumetric mass transfer coefficient and the Henry’s coefficient were determined simultaneously by parameter estimation using a nonlinear optimization method. A minor dependence of the Henry’s law constant on pH was detected at the pH range 4 - 9. In the second article, a new method using the axial dispersion model for estimation of ozone self-decomposition kinetics in a semi-batch bubble column reactor was developed. The reaction rate coefficients for literature equations of ozone decomposition and the gas phase dispersion coefficient were estimated and compared with the literature data. The reaction order in the pH range 7-10 with respect to ozone 1.12 and 0.51 the hydroxyl ion were obtained, which is in good agreement with literature. The model parameters were determined by parameter estimation using a nonlinear optimization method. Sensitivity analysis was conducted using object function method to obtain information about the reliability and identifiability of the estimated parameters. In the third article, the reaction rate coefficients and the stoichiometric coefficients in the reaction of ozone with the model component p-nitrophenol were estimated at low pH of water using nonlinear optimization. A novel method for estimation of multireaction model parameters in ozonation was developed. In this method the concentration of unknown intermediate compounds is presented as a residual COD (chemical oxygen demand) calculated from the measured COD and the theoretical COD for the known species. The decomposition rate of p-nitrophenol on the pathway producing hydroquinone was found to be about two times faster than the p-nitrophenol decomposition rate on the pathway producing 4- nitrocatechol. In the fourth article, the reaction kinetics of p-nitrophenol ozonation was studied in a bubble column at pH 2. Using the new reaction kinetic model presented in the previous article, the reaction kinetic parameters, rate coefficients, and stoichiometric coefficients as well as the mass transfer coefficient were estimated with nonlinear estimation. The decomposition rate of pnitrophenol was found to be equal both on the pathway producing hydroquinone and on the path way producing 4-nitrocathecol. Comparison of the rate coefficients with the case at initial pH 5 indicates that the p-nitrophenol degradation producing 4- nitrocathecol is more selective towards molecular ozone than the reaction producing hydroquinone. The identifiability and reliability of the estimated parameters were analyzed with the Marcov chain Monte Carlo (MCMC) method. @All rights reserved. No part of the publication may be reproduced, stored in a retrieval system, or transmitted, in any form or by any means, electronic, mechanical, photocopying, recording, or otherwise, without the prior permission of the author.

Determinação espectrofotométrica de aspartame em adoçantes por injeção em fluxo usando um reator em fase sólida contendo fosfato de zinco imobilizado

A flow injection spectrophotometric method was developed for determining aspartame in sweeteners. Sample was dissolved in water and 250 µL of the solution was injected into a carrier stream of 5.0 x 10-5 mol L-1 sodium borate solution. The sample flowed through a column (14 cm x 2.0 mm) packed with Zn3(PO4)2 immobilized in a polymeric matrix of polyester resin and Zn(II) ions were released from the solid-phase reactor by formation of the Zn(II)-aspartame complex. The mixture merged with a stream of borate buffer solution (pH 9.0) containing 0.030 % (m/v) alizarin red S and the Zn(II)-alizarin red complex formed was measured spectrophotometrically at 540 nm. The calibration graph for aspartame was linear in the concentration range from 10 to 80 µg mL-1 with a detection limit of 4 µg mL-1 of aspartame. The RSD was 0.3 % for a solution containing 40 µg mL-1 aspartame (n = 10) and seventy results were obtained per hour. The proposed method was applied for determining aspartame in commercial sweeteners.

Paperin puhtauden parantaminen lajittelun ja muiden prosessiteknisten keinojen avulla

Tämä työ suoritettiin UPM- Kymmene Oyj:n Tervasaaren tehtaan PK 5:llä. PK 5 valmistaa tarrantaustapaperia. Tämän työn tarkoituksena oli löytää eri keinoja paperin puhtauden parantamiseksi. Puhtaamman paperin valmistaminen parantaa paperikoneen kilpailukykyä kilpailijoihinsa nähden sekä vähentää asiakasvalituskustannuksia. Työn kirjallinen osa koostuu kolmesta suuremmasta kokonaisuudesta, joiden tarkoituksena on luoda teoriapohjaa kokeellisen osan suoritusta varten. Kirjallisuusosan pääpaino on kohdistettu PK 5:llä esiintyviin saostumanaiheuttajiin, kuten uuteaineisiin, ASA- liimaan ja mikrobeihin. Tarkemmassa tarkastelussa on kirjallisuusosassa myös painelajittelu ja pyörrepuhdistus. Kokeellisessa osassa suoritettiin PK 5:n prosessissa syntyvien epäpuhtauksien karakterisointi. Suurimmat saostuman aiheuttajat analyysien perusteella olivat puuperäiset uuteaineet ja ASA- liima. Epäorgaanisista aineista päällystyskomponenttina toimiva kaoliini ja sellun mukana tuleva pihkatalkki esiintyi useimpien saostumien komponentteina. Selvityksessä havaittiin, että prosessille vieraita aineita ei löydetty muista, kuin kalanteroidusta paperista analysoiduista tummista täplistä. Tummista täplistä analysoitu styreenin alkuperä voi selittyä mm. prosessiin päässeellä kumilla tai muovilla. PK 5:n prosessissa selvityksen mukaan silikonipohjainen vaahdonestoaine aiheuttaa erittäin suuria tummia saostumia, joten sen pääsy prosessiin tulee estää sellutehtaalla tarkoin. Epäpuhtauksien määrä on suurin PK 5:n prosessissa hylkylinjassa ja lyhyessä kierrossa. Hylyn painelajittelu poistaa hyvin roskia syöttömassasta. Hylyn lajittelun toisen portaan lajittimen rejektin roskapitoisuus on suhteellisen suuri. Rejektin ohjaaminen ulos prosessista vähentää roskaisuuden rikastumista prosessiin. Sakeamassalajittelun sijoittaminen PK 5:n konekyypin jälkeen vähentää roskien päätymistä paperiin. Hylyn painelajittelun ja PP- laitoksen rejektin ohjaaminen sakeamassalajittelun toiseen portaaseen vähentäisi priimakuitutappiota ja roskien määrää käytetyissä massoissa. Seisokin aikaisen putkilinjojen pesujen lopputulos parani huomattavasti BA- pesuaineen käyttöönoton jälkeen. Kyseisen pesuaine soveltuu liuottamaan putkistosta mm. PK 5:llä esiintyvät uuteaine- ja ASA- saostumat. BSA- sellun pH- säädön lopettamisella oli suuri vähentävä vaikutus tummien täplien esiintymistiheyteen. pH- säädössä BSA- tornin pohjalaimennukseen annosteltu lipeä edesauttoi tummien saostumien syntymistä saippuoiden uuteaineita.

Construção e otimização de um reator de baixo custo para a fotodegradação da matéria orgânica em águas naturais e sua aplicação no estudo da especiação do cobre por voltametria

This work describes the construction of a home-made low-cost reactor, using easily available materials, capable of destroying efficiently dissolved organic matter. Just 30 minutes of irradiation were sufficient to destroy more than 99% of the humic acids present in a solution of 4 mg C L-1. Copper speciation was evaluated in natural waters of different salinities to test the reactor's efficiency in destroying organically complexed metal species. The effect of the organic matter concentration, salinity, dissolved oxygen and temperature in the photo-oxidation process is discussed.

Descoloração e degradação de poluentes orgânicos em soluções aquosas através do processo fotoeletroquímico

Organic compounds responsible for the color of wastewaters are usually refractory to biological digestion. In this paper the photo-assisted electrolysis process is used for color removal from three of the most colored wastewaters, which are daily generated in large amounts: the E1 bleach Kraft mill effluent, a textile reactive dye effluent and a landfill leachate. Electrolysis was carried out at 26,5 mA cm-2 in a flow reactor in which the anode surface was illuminated by a 400 W high pressure Hg bulb. In all experiments 70-75% of color reduction was observed which was also followed by a net organic load oxidation.

Laite- ja työturvallisuus H2S-tiloissa

Tässä työssä selvitettiin, millä tavoin räjähdysvaarallisten työtilojen työturvallisuuteen voidaan vaikuttaa ja miten turvallisuutta pidetään yllä. Työssä selvitettiin, mitä vaatimuksia räjähdysvaaralliset tilat asettavat laite- ja työturvallisuudelle. Työn lähtökohdaksi otettiin ilmanvaihdon vaikutus sisäilman olosuhteisiin ja samalla selvitettiin, mitä muutoksia räjähdysvaarallisten aineiden käyttö teollisuuden tuotantoprosesseissa aiheuttaa ilmanvaihdossa. Räjähdysvaarallisten tilojen suunnittelua ohjailevat säädökset, lait ja direktiivit. Johdonmukaisen suunnittelulla ja säädöksiä noudattamalla pystytään toteuttamaan turvallinen työympäristö. Räjähdysvaarallista tilaa päästiin tarkastelemaan Talvivaaran Kaivososakeyhtiö Oyj:n metallien talteenottolaitoksella. Työssä haluttiin tutkia rakennuksen työturvallisuutta ja työskentelyolosuhteita. Tutkimuskohteena olleessa reaktorihallissa tehtiin ilmanvaihdon suorituskyvyn mittauksia. Tarkoituksena oli myös tehdä rikkivedyn pitoisuus mittauksia, mutta Talvivaaran tuotannon viivästyessä, pitoisuus mittaukset jätettiin tämän diplomityön ulkopuolelle. Talvivaaraan reaktorirakennuksen olosuhteita ja turvallisuutta tarkasteltiin lähemmin teoreettisten laskelmien avulla. Laskelmien ja mittaustulosten perusteella reaktorirakennuksen ilmanvaihdon suorituskyky todettiin riittäväksi ja toiminta työturvalliseksi. Riskin arvioinnin perusteella reaktorirakennuksen riskitason katsotaan olevan siedettävä.

Catalytic gasification of glycerol in supercritical water

The conversion of glycerol in supercritical water (SCW) was studied at 510-550 °C and a pressure of 350 bars using both a bed of inert and non-porous ZrO2 particles (hydrothermal experiments), and a bed of a 1% Ru/ZrO2 catalyst. Experiments were conducted with a glycerol concentration of 5 wt% in a continuous isothermal fixed-bed reactor at a residence time between 2 and 10 s. Hydrothermolysis of glycerol formed water-soluble products such as acetaldehyde, acetic acid, hydroxyacetone and acrolein, and gases like H2, CO and CO2. The catalyst enhanced the formation of acetic acid, inhibited the formation of acrolein, and promoted gasification of the glycerol decomposition products. Hydrogen and carbon oxides were the main gases produced in the catalytic experiments, with minor amounts of methane and ethylene. Complete glycerol conversion was achieved at a residence time of 8.5 s at 510 °C, and at around 5 s at 550 °C with the 1 wt% Ru/ZrO2 catalyst. The catalyst was not active enough to achieve complete gasification since high yields of primary products like acetic acid and acetaldehyde were still present. Carbon balances were between 80 and 60% in the catalytic experiments, decreasing continuously as the residence time was increased. This was attributed partially to the formation of methanol and acetaldehyde, which were not recovered and analyzed efficiently in our set-up, but also to the formation of carbon deposits. Carbon deposition was not observed on the catalyst particles but on the surface of the inert zirconia particles, especially at high residence time. This was related to the higher concentration of acetic acid and other acidic species in the catalytic experiments, which may polymerize to form tar-like carbon precursors. Because of carbon deposition, hydrogen yields were significantly lower than expected; for instance at 550 °C the hydrogen yield potential was only 50% of the stoichiometric value.