Polymeerien erotus ultrasuodatuksella

Työssä selvitettiin suodatusolosuhteiden vaikutusta neutraalien polymeerien pidättymiseen niiden vesiliuoksia suodatettaessa. Suodatuksissa käytettiin kahta regeneroidusta selluloosasta valmistettua ultrasuodatuskalvoa (Microdyn-Nadir UC 030T ja JSC STC Vladipor C 30V). Malliaineina käytettiin polyetyleeniglykolia ja dekstraania. Kirjallisuusosassa esiteltiin aluksi lyhyesti ultrasuodatus erotusmenetelmänä. Lisäksi käsiteltiin ultrasuodatuskalvojen huokoskoon karakterisointimenetelmiä ja selvitettiin polymeerien erottumiseen ultrasuodatuksen aikana vaikuttavia tekijöitä. Työn kokeellisessa osassa tutkittiin paineen ja virtausnopeuden vaikutusta malliaineiden pidättymiseen ultrasuodatuskalvoilla. Lisäksi pyrittiin löytämään suodatusolosuhteet, joissa toinen aineista läpäisisi suodatuskalvon lähes täydellisesti toisen konsentroituessa syöttöliuokseen. Työssä myös määritettiin tutkimuksissa käytetyille kalvoille katkaisukoko, joka kuvaa kalvon kykyä pidättää moolimassaltaan erikokoisia molekyylejä. Lisäksi kokeellisessa osassa selvitettiin työssä käytettyjen kalvojen tasalaatuisuutta vertailemalla keskenään samanlaisissa suodatusolosuhteissa eri kalvopaloilla tehtyjen suodatusten tuloksia. Työssä saatiin erotettua kaksi lähes samankokoista malliaineeksi valittua neutraalia polymeeriä toisistaan siten, että toinen aine pidättyi kalvolla huomattavasti toista ainetta paremmin. Parhaimpaan erotustulokseen päästiin, kun permeaattivuo kalvon läpi oli noin 400 l/(m2 h). Tällöin suodatuspaine oli noin 2 bar ja virtausnopeus alle 2 m/s. Työn aikana määritettyjen katkaisukokojen havaittiin poikkeavan huomattavasti kalvojen valmistajien ilmoittamista arvoista, mutta olevan kuitenkin samaa suuruusluokkaa kuin muiden tutkimusryhmien vastaaville ultrasuodatuskalvoille esittämät arvot. Työn tulosten perusteella C 30V olisi hieman tasalaatuisempi kalvo kuin UC 030T.

Determinação de fósforo orgânico em águas de produção petrolífera por ICP- AES e ICP- MS após pré-concentração em coluna de sílica-C18

Results on the optimization of analytical methods for the determination of phosphorus in phosphino-polycarboxylate (PPCA), used frequently as scale inhibitor during oil production, by ICP-AES and ICP-MS are presented. Due to the complex matrix of production waters (brines) and their high concentration in inorganic phosphorus, the separation of organic phosphorus prior to its determination is necessary. In this work, minicolumns of silica immobilized C18 were used. Optimization of the separation step resulted in the following working conditions: (1) prewashing of the column with methanol (80% v/v); (2) use of a flow rate of 5 mL/min and 10 mL/min, respectively, for the preconditioning step and for percolation of the water sample; (3) final elution of organic phosphorus with 7 mL of buffer of H3BO3/NaOH (0.05 M, pH 9) with a flow rate of 1 mL/min. Sample detection limits (3s) for different combinations of nebulizers and spectrometric methods, based on 10 mL water aliquots, are: ICP-AES -Cross flow (47 mg/L) and Ultrasonic (18 mug/L); ICP-MS -Cross flow (1.2 mug/L), Cyclonic (0.7 mug/L) and Ultrasonic (0.5 mug/L). Typical recoveries of organic phosphorus are between 90 and 95% and the repeatability of the whole procedure is better than 10%. The developed methodology was applied successfully to samples from the oil-well NA 46, platform PNA 2, Campos basin, Brazil. Assessment of the PPCA inhibitor was possible at lower concentrations than achieved by current analytical methods, resulting in benefits such as reduced cost of chemicals, postponed oil production and lower environmental impacts.

Electrochemical Characterisation of Filter Media Properties and Their Exploitation in Enhanced Filtration

Streaming potential measurements for the surface charge characterisation of different filter media types and materials were used. The equipment was developed further so that measurements could be taken along the surfaces, and so that tubular membranes could also be measured. The streaming potential proved to be a very useful tool in the charge analysis of both clean and fouled filter media. Adsorption and fouling could be studied, as could flux, as functions of time. A module to determine the membrane potential was also constructed. The results collected from the experiments conducted with these devices were used in the study of the theory of streaming potential as an electrokinetic phenomenon. Several correction factors, which are derived to take into account the surface conductance and the electrokinetic flow in very narrow capillaries, were tested in practice. The surface materials were studied using FTIR and the results compared with those from the streaming potentials. FTIR analysis was also found to be a useful tool in the characterisation of filters, as well as in the fouling studies. Upon examination of the recorded spectra from different depths in a sample it was possible to determine the adsorption sites. The influence of an external electric field on the cross flow microflltration of a binary protein system was investigated using a membrane electroflltration apparatus. The results showed that a significant improvement could be achieved in membrane filtration by using the measured electrochemical properties to help adjust the process conditions.

Treatment of oily wastewater by ultrafiltration: The effect of different operating and solution conditions

In many industries, such as petroleum production, and the petrochemical, metal, food and cosmetics industries, wastewaters containing an emulsion of oil in water are often produced. The emulsions consist of water (up to 90%), oils (mineral, animal, vegetable and synthetic), surfactants and other contaminates. In view of its toxic nature and its deleterious effects on the surrounding environment (soil, water) such wastewater needs to be treated before release into natural water ways. Membrane-based processes have successfully been applied in industrial applications and are considered as possible candidates for the treatment of oily wastewaters. Easy operation, lower cost, and in some cases, the ability to reduce contaminants below existing pollution limits are the main advantages of these systems. The main drawback of membranes is flux decline due tofouling and concentration polarisation. The complexity of oil-containing systems demands complementary studies on issues related to the mitigation of fouling and concentration polarisation in membranebased ultrafiltration. In this thesis the effect of different operating conditions (factors) on ultrafiltration of oily water is studied. Important factors are normally correlated and, therefore, their effect should be studied simultaneously. This work uses a novel approach to study different operating conditions, like pressure, flow velocity, and temperature, and solution properties, like oil concentration (cutting oil, diesel, kerosene), pH, and salt concentration (CaCl2 and NaCl)) in the ultrafiltration of oily water, simultaneously and in a systematic way using an experimental design approach. A hypothesis is developed to describe the interaction between the oil drops, salt and the membrane surface. The optimum conditions for ultrafiltration and the contribution of each factor in the ultrafiltration of oily water are evaluated. It is found that the effect on permeate flux of the various factors studied strongly depended on the type of oil, the type of membrane and the amount of salts. The thesis demonstrates that a system containing oil is very complex, and that fouling and flux decline can be observed even at very low pressures. This means that only the weak form of the critical flux exists for such systems. The cleaning of the fouled membranes and the influence of different parameters (flow velocity, temperature, time, pressure, and chemical concentration (SDS, NaOH)) were evaluated in this study. It was observed that fouling, and consequently cleaning, behaved differently for the studied membranes. Of the membranes studied, the membrane with the lowest propensity for fouling and the most easily cleaned was the regenerated cellulose membrane (C100H). In order to get more information about the interaction between the membrane and the components of the emulsion, a streaming potential study was performed on the membrane. The experiments were carried out at different pH and oil concentration. It was seen that oily water changed the surface charge of the membrane significantly. The surface charge and the streaming potential during different stages of filtration were measured and analysed being a new method for fouling of oil in this thesis. The surface charge varied in different stages of filtration. It was found that the surface charge of a cleaned membrane was not the same as initially; however, the permeability was equal to that of a virgin membrane. The effect of filtration mode was studied by performing the filtration in both cross-flow and deadend mode. The effect of salt on performance was considered in both studies. It was found that salt decreased the permeate flux even at low concentration. To test the effect of hydrophilicity change, the commercial membranes used in this thesis were modified by grafting (PNIPAAm) on their surfaces. A new technique (corona treatment) was used for this modification. The effect of modification on permeate flux and retention was evaluated. The modified membranes changed their pore size around 33oC resulting in different retention and permeability. The obtained results in this thesis can be applied to optimise the operation of a membrane plant under normal or shock conditions or to modify the process such that it becomes more efficient or effective.

Hydroksihappojen erotus mustalipeästä nanosuodatuksella

Hydroksihapoille on olemassa useita käyttömahdollisuuksia teollisuudessa, joten niiden hyödyntäminen sellunvalmistuksen sivuvirrasta eli mustalipeästä on suuren kiinnostuksen kohteena. Tässä työssä selvitettiin, onko hydroksihappojen erotus ja puhdistus mustalipeästä mahdollista nanosuodatuksella. Kokeellisessa osassa suodatettiin emäksisen mustalipeän lisäksi hapotettua ja jäähdytyskiteytettyä mustalipeää, johon oli lisätty liuotinta. Mustalipeäsuodatuksissa käytettiin viittä erilaista nanosuodatusmembraania (Microdyn Nadir® NP010 ja NP030, Dow Chemical Company NF-90, Woongjin Chemical NE-70 sekä Ge-Osmonics Desal 5 DK). Kirjallisuusosassa käsiteltiin puun sisältämien yhdisteiden kemiallista koostumusta, sellun valmistuksen pääperiaatteita, mustalipeän ja hydroksihappojen ominaisuuksia sekä hydroksihappojen käyttömahdollisuuksia. Lisäksi tarkasteltiin erilaisia hydroksihappojen erotusmenetelmiä, nanosuodatuksen teoriaa ja prosessiin sopivan membraanin valintakriteerejä. Työn kokeellisessa osassa tutkittiin emäksisen mustalipeän monivaiheisen nanosuodatuksen tehokkuutta hydroksihappojen erotuksessa. Hapotetun ja jäähdytyskiteytetyn mustalipeän suodatuskokeissa tutkittiin erityyppisten membraanien erotuskykyä sekä syötön liuotinlisäyksen vaikutusta hydroksihappojen erottumiseen. Lisäksi tarkasteltiin membraanien kestävyyttä ja foulaantumista suodatusolosuhteissa. Työn tulokset osoittivat, että hydroksihappoja voidaan fraktioida mustalipeästä nanosuodatuksella. Hydroksihappojen fraktiointiin vaikuttaa merkittävästi mustalipeässä käytetyn liuottimen läsnäolo sekä suodatuspaine. Lisäksi koetulosten perusteella havaittiin, että monivaiheisella nanosuodatuksella hydroksihapot läpäisevät membraanin ja permeaattiin saavutetaan puhtaampi happojae.

Arvometallien liuospuhdistus jatkuvatoimisella ioninvaihdolla

Työn tarkoituksena oli tutkia arvometalleja sisältävän liuoksen puhdistamista jat-kuvatoimisella ioninvaihdolla. Teoriaosassa käsitellään ioninvaihdon periaate, sekä jatkuvatoimisen ioninvaihdon laiteratkaisuja ristivirta- ja vastavirtasysteemeissä. Lopuksi esitellään Simuloidun liikkuvapedin (SMB) virtausnopeuksien laske-miseksi käytettävä kolmiomenetelmä. Kokeellisen osan tarkoituksena on demonstroida laboratorioon rakennetun jatku-vatoimisen ioninvaihtimen, Simuloidun liikkuvapedin, käyttö arvometallia sisäl-tävän liuoksen puhdistamiseksi kahdenarvoisista metalli-ioneista. Kokeissa käy-tettiin hopeaa sisältävää NaCl-liuosta, josta pyrittiin puhdistamaan Mg2+, Ca2+, Pb2+ ja Zn2+-ionit ekstraktina. Laitteistolla suoritettiin kolme ajoa, joista kaksi edusti vastavirtasysteemiä ja yksi ristivirtasysteemiä. Ensimmäisessä vastavirta-ajossa sekä ekstrakti että raffinaattin erottuva hopealiuos tulivat puhtaina. Toisessa vastavirta-ajossa pyrittiin parantamaan tuottavuutta nostamalla syötön virtausnopeutta, jolloin raffinaatin puhtaus kärsi Pb2+ ja Mg2+-ionien kulkeutuessa liuosfaasin mukana raffinaattiin. Ristivirta-ajossa vain yksi kolmesta raffinaatista saavutti 100 % puhtauden. Kokeet osoittivat, että Mg2+, Ca2+, Pb2+ ja Zn2+-ionien erottaminen hopeaionista on mahdollista käyttämällämme SMB-laitteistolla. Tuottavuuden parantaminen syötön virtausnopeutta nostamalla kuitenkin heikentää puhtautta. Cross-flow-systeemin erilleenkytkettyjen kolonnien ansioista painehäviö on pienempi, mikä mahdollistaa korkeammat virtausnopeudet, mikäli ei vaadita 100 % puhtautta.

Influence of depectinization in the ultrafiltration of West Indian cherry (Malpighia glabra L.) and pineapple (Ananas comosus (L.) Meer) juices

West Indian cherry (Malpighia glabra L.) and pineapple (Ananas comosus (L.) Meer)juice clarification by cross-flow UF, using polysulphone hollow fiber and ceramic tubular membranes with, respectively, nominal molecular weight cut off values of 100kDaltons and average pore diameters of 0.01mm, were studied. The influence of enzymatic treatment using enzyme concentrations of 20, 100 and 300mg/L, a time of 90min and a temperature of 40ºC for depectinization was verified. The juices were then clarified in a laboratory scale filtration unit, with an effective filtration area of 0.12m² for the polysulphone hollow fiber membrane and of 0.005m² for the ceramic tubular membranes. The influence of enzymatic treatment on viscosity, turbidity and total pectin of the juice, before ultrafiltration, is reported. Membrane performance was evaluated in terms of flow rate and clarity of the permeate. The permeate flow rate of depectinized pineapple juice was higher (30 - 60%) for both membranes. Depectinized West Indian cherry juice presented a lower permeate flow rate for the polysulphone hollow fiber membrane. The increase in permeate flow rate, with the use of the 300mg/L and 100mg/L enzyme concentration was not significant, so it is economically advantageous to ultrafilter depectinized juice, treated with an enzyme concentration of 20mg/L.

Effects of Fin Parameters on Gas-Side Heat Transfer Performance of H-Type Finned Tube Bundle in a Waste Heat Recovery Boiler

Alfa Laval Aalborg Oy designs and manufactures waste heat recovery systems utilizing extended surfaces. The waste heat recovery boiler considered in this thesis is a water-tube boiler where exhaust gas is used as the convective heat transfer medium and water or steam flowing inside the tubes is subject to cross-flow. This thesis aims to contribute to the design of waste heat recovery boiler unit by developing a numerical model of the H-type finned tube bundle currently used by Alfa Laval Aalborg Oy to evaluate the gas-side heat transfer performance. The main objective is to identify weaknesses and potential areas of development in the current H-type finned tube design. In addition, numerical simulations for a total of 15 cases with varying geometric parameters are conducted to investigate the heat transfer and pressure drop performance dependent on H-type fin geometry. The investigated geometric parameters include fin width and height, fin spacing, and fin thickness. Comparison between single and double tube type configuration is also conducted. Based on the simulation results, the local heat transfer and flow behaviour of the H-type finned tube is presented including boundary layer development between the fins, the formation of recirculation zone behind the tubes, and the local variations of flow velocity and temperature within the tube bundle and on the fin surface. Moreover, an evaluation of the effects of various fin parameters on heat transfer and pressure drop performance of H-type finned tube bundle has been provided. It was concluded that from the studied parameters fin spacing and fin width had the most significant effect on tube bundle performance and the effect of fin thickness was the least important. Furthermore, the results suggested that the heat transfer performance would increase due to enhanced turbulence if the current double tube configuration is replaced with single tube configuration, but further investigation and experimental measurements are required in order to validate the results.

Development and characterization of concentric capillary nebulizer used in inductively coupled plasma analysis /

A simple, low-cost concentric capillary nebulizer (CCN) was developed and evaluated for ICP spectrometry. The CCN could be operated at sample uptake rates of 0.050-1.00 ml min'^ and under oscillating and non-oscillating conditions. Aerosol characteristics for the CCN were studied using a laser Fraunhofter diffraction analyzer. Solvent transport efficiencies and transport rates, detection limits, and short- and long-term stabilities were evaluated for the CCN with a modified cyclonic spray chamber at different sample uptake rates. The Mg II (280.2nm)/l\/lg 1(285.2nm) ratio was used for matrix effect studies. Results were compared to those with conventional nebulizers, a cross-flow nebulizer with a Scott-type spray chamber, a GemCone nebulizer with a cyclonic spray chamber, and a Meinhard TR-30-K3 concentric nebulizer with a cyclonic spray chamber. Transport efficiencies of up to 57% were obtained for the CCN. For the elements tested, short- and long-term precisions and detection limits obtained with the CCN at 0.050-0.500 ml min'^ are similar to, or better than, those obtained on the same instrument using the conventional nebulizers (at 1.0 ml min'^). The depressive and enhancement effects of easily ionizable element Na, sulfuric acid, and dodecylamine surfactant on analyte signals with the CCN are similar to, or better than, those obtained with the conventional nebulizers. However, capillary clog was observed when the sample solution with high dissolved solids was nebulized for more than 40 min. The effects of data acquisition and data processing on detection limits were studied using inductively coupled plasma-atomic emission spectrometry. The study examined the effects of different detection limit approaches, the effects of data integration modes, the effects of regression modes, the effects of the standard concentration range and the number of standards, the effects of sample uptake rate, and the effect of Integration time. All the experiments followed the same protocols. Three detection limit approaches were examined, lUPAC method, the residual standard deviation (RSD), and the signal-to-background ratio and relative standard deviation of the background (SBR-RSDB). The study demonstrated that the different approaches, the integration modes, the regression methods, and the sample uptake rates can have an effect on detection limits. The study also showed that the different approaches give different detection limits and some methods (for example, RSD) are susceptible to the quality of calibration curves. Multicomponents spectral fitting (MSF) gave the best results among these three integration modes, peak height, peak area, and MSF. Weighted least squares method showed the ability to obtain better quality calibration curves. Although an effect of the number of standards on detection limits was not observed, multiple standards are recommended because they provide more reliable calibration curves. An increase of sample uptake rate and integration time could improve detection limits. However, an improvement with increased integration time on detection limits was not observed because the auto integration mode was used.

The triggering of orographic rainbands by small-scale topography

The triggering of convective orographic rainbands by small-scale topographic features is investigated through observations of a banded precipitation event over the Oregon Coastal Range and simulations using a cloud-resolving numerical model. A quasi-idealized simulation of the observed event reproduces the bands in the radar observations, indicating the model’s ability to capture the physics of the band-formation process. Additional idealized simulations reinforce that the bands are triggered by lee waves past small-scale topographic obstacles just upstream of the nominal leading edge of the orographic cloud. Whether a topographic obstacle in this region is able to trigger a strong rainband depends on the phase of its lee wave at cloud entry. Convective growth only occurs downstream of obstacles that give rise to lee-wave-induced displacements that create positive vertical velocity anomalies w_c and nearly zero buoyancy anomalies b_c as air parcels undergo saturation. This relationship is quantified through a simple analytic condition involving w_c, b_c, and the static stability N_m^2 of the cloud mass. Once convection is triggered, horizontal buoyancy gradients in the cross-flow direction generate circulations that align the bands parallel to the flow direction.

Critical flux in ultrafiltration of skimmed milk

he best operating conditions, using the critical flux concept during ultrafiltration of skimmed milk, were evaluated for tubular membranes. It was found that irreversible fouling was greatly reduced by operating at or below the critical flux, but was not totally eliminated. The critical flux of skimmed milk was found to be the weak form. The critical flux at cross flow velocity 3.4 in s(-1) for MWCO 200 kDa membrane was 56.9 kg m(-2) h(-1) while for MWCO 25 kDa membranes it was 45 kg m(2) h(-1) suggesting that membrane pore size influenced the flux. The critical flux increased with increasing wall shear stress and decreased with increasing protein concentration. Empirical equations, for predicting the critical flux (J(crit)) for skimmed milk with a protein concentration (c(b)) in the range 3-7% w/w and wall shear stress (tau(w)) in the range 7-60 Pa for MWCO 200 kDa and 25 kDa membranes were J(crit) = 5.1 (tau(w)/c(b)) and J(crit) = 4.0 (tau(w)/c(b)) respectively. In general, the rejections of protein and lactose at the critical flux were not affected by protein concentration, wall shear stress and membrane used, and they were similar to those found when operating at the limiting flux.

Synthesis of galacto-oligosaccharide from lactose using beta-galactosidase from Kluyveromyces lactis: studies on batch and continuous UF membrane-fitted bioreactors

A study of galacto-oligosaccharides (GOS) synthesis from lactose with beta-galactosidase from Kluyveromyces lactis (Maxilact(R) L2000) was carried out. The synthesis was performed using various initial lactose concentrations ranging from 220 to 400 mg/mL and enzyme concentrations ranging from 3 to 9 U/mL, and was investigated at 40degreesC and pH 7, in a stirred-tank reactor. In the experimental range examined, the results showed the amount of GOS formed depended on lactose concentration but not on enzyme concentration. Galactose was a competitive inhibitor, while glucose was a non-competitive inhibitor. In a further study, a laboratory-scale reactor system, fitted with a 10-kDa NMWCO composite regenerated cellulose membrane, was used in a continuous process. The reactor was operated in cross-flow mode. The effect of operating pressures on flux and productivity was investigated by applying different transmembrane pressures to the system. The continuous process showed better production performance compared to the batch synthesis with the same lactose and enzyme concentrations at 40degreesC, pH 7. Comparison of product structures from batch and continuous processes, analyzed by HPAEPAD and methylation analysis, showed similarities but differed from the structures found in a commercial GOS product (Vivinal(R)GOS). (C) 2004 Wiley Periodicals, Inc.

Determinação de elementos traço em amostras ambientais por ICP OES

Neste trabalho é avaliada a aplicação da técnica de ICP OES (Espectrometria de Emissão com Plasma Indutivamente Acoplado) para a determinação de elementos traço em amostras ambientais. Foram investigados os comportamentos de As, Ba, Cd, Co, Cu, Cr, Mn, Ni, Pb, V e Zn, utilizando-se espectrômetro com vista de observação axial/radial do plasma e sistema de detecção baseado em dispositivos de carga acoplada (CCD). No presente estudo, foi avaliado o desempenho dos nebulizadores pneumáticos do tipo concêntrico (Meinhard), “cross flow” e GemCone® acoplados às câmaras de nebulização de duplo passo (Scott) e ciclônica, bem como do nebulizador ultra-sônico para a introdução de amostras no plasma. Investigou-se a robustez do plasma, potência de radiofreqüência (RF), vazão dos gases de nebulização e auxiliar, bem como a altura de observação, para ambas as vistas de observação do plasma. Sob condições otimizadas os limites de detecção (LD), em ng mL-1, para os elementos As, Ba, Cd, Co, Cr, Cu, Mn, Ni, Pb, V e Zn, em solução aquosa de HNO3 5% (v/v), utilizando-se a configuração axial do plasma, foram: 1,1 - 16; 0,002 - 0,32; 0,03 - 1,2; 0,02 - 0,72; 0,03 - 0,82; 0,04 - 3,0; 0,003 - 0,76; 0,08 - 3,8; 0,22 - 8,9; 0,04 - 2,6; e 0,02 - 1,2 respectivamente. Utilizando-se a configuração radial, os LDs (ng mL-1) dos mesmos elementos foram: 10 - 87; 0,01 - 0,91; 0,07 - 3,8; 0,16 - 4,3; 0,13 - 8,1; 0,16 - 4,3; 0,01 - 0,81; 0,43 - 7,6; 1,4 - 37; 0,28 - 6,0 e 0,77 - 9,5 respectivamente. Com relação à nebulização pneumática, os LDs são relativamente mais baixos quando é utilizado o nebulizador concêntrico acoplado à câmara de nebulização ciclônica. LDs ainda melhores são obtidos mediante o uso de nebulização ultra-sônica mas, neste caso, foi observado que o plasma é menos robusto. As metodologias foram desenvolvidas mediante o uso de materiais de referência certificados sendo analisados os seguintes materiais: sedimento marinho (PACS-2/NRCC), folhas de maçã (apple leaves – 1515/NIST) e água (natural water – 1640/NIST), obtendo-se concentrações concordantes com as certificadas, com exceção do Ni em folha de maçã, que não foi detectado utilizando-se a nebulização pneumática e também não pôde ser determinado com exatidão mediante o uso de nebulizador ultra-sônico. Interferências não espectrais observadas na análise de sedimento marinho foram contornadas através da diluição da amostra, ou através da lavagem da câmara de nebulização com solução de HNO3 5% (v/v), por 60 s entre cada ciclo de leitura. Estas interferências não puderam ser contornadas com o uso de padrão interno (PI). A interferência espectral do As sobre o Cd não foi observada fazendo-se a medição do sinal em área de pico, demarcado com somente 3 pontos/pico. Após serem estabelecidas as metodologias de análise, foram analisadas as seguintes amostras não certificadas: água de rio, água subterrânea (poço artesiano), água tratada e de chuva, folhas de eucalipto e bambu, acículas de pinus e infusão de chá preto, sendo possível quantificar baixas concentrações dos elementos investigados, utilizando-se a calibração externa.

Development of a micro-heat exchanger with stacked plates using LTCC technology

A green ceramic tape micro-heat exchanger was developed using Low Temperature Co-fired Ceramics technology (LTCC). The device was designed by using Computational Aided Design software and simulations were made using a Computational Fluid Dynamics package (COMSOL Multiphysics) to evaluate the homogeneity of fluid distribution in the microchannels. Four geometries were proposed and simulated in two and three dimensions to show that geometric details directly affect the distribution of velocity in the micro-heat exchanger channels. The simulation results were quite useful for the design of the microfluidic device. The micro-heat exchanger was then constructed using the LTCC technology and is composed of five thermal exchange plates in cross-flow arrangement and two connecting plates, with all plates stacked to form a device with external dimensions of 26 x 26 x 6 mm(3).

Simulação numérica de trocadores de calor multitubulares equipados com fitas helicoidais externamente aos tubos

Classical shell-and-tube heat exchangers are usually equipped with segmental baffles. These baffles serve two basic functions: (a) they provide tube supports, thereby preventing or reducing mechanical problems, such as sagging or vibration; (b) they direct the fluid flow over the tubes so as to introduce a cross-flow component, thereby increasing the heat transfer. Segmented baffles have several sources of performance loss, some due to various leakage flows and others caused by stagnation zones. A new concept of longitudinal flow heat exchanger - based on placing twisted tapes along the tube bundle subchannels - was developed to mitigate drawbacks of other types of tubular heat exchangers. In this paper, a numerical model has been implemented in order to simulate the thermal-hydraulic feature of tubular heat exchangers equipped either with segmental baffles or with subchannel twisted tapes. The tube bundle has been described by means of an equivalent porous medium type model, allowing a macroscopic description of the shell-side flow. The basic equations - continuity, momentum and energy - have been solved by using the finite volume method. Typical numerical results have been compared with experimental data, reaching a very good agreement. A comparative analysis of different types of heat exchangers has been carried out, revealing the satisfactory thermal-hydraulic efficiency level of the twisted tapes heat exchangers.