934 resultados para Pore-size Distributions
Resumo:
Waste has been incinerated for energy utilization for more than a hundred years, but the harmful emissions emitted from the incineration plants did not begin to cause concern until the 1980s. Many plants were shutdown and the waste incineration plant in Kyläsaari Helsinki was one of them. In later years, new landfill regulations have increased the interest in waste incineration. During the last year, four new plants were taken into operation in Finland, Westenergy in Vaasa among them. The presence of dust has been observed indoors at Westenergy waste incineration plant. Dust is defined as particles with a diameter above 10 μm, while fine particles have a diameter smaller than 2.5 μm, ultrafine under 0.1 μm and nanoparticles under 0.05 μm. In recent years, the focus of particle health research has been changed to investigate smaller particles. Ultrafine particles have been found to be more detrimental to health than larger particles. Limit values regulating the concentrations of ultrafine particles have not been determined yet. The objective of this thesis was to investigate dust and particles present inside the Westenergy waste incineration facility. The task was to investigate the potential pollutant sources and to give recommendations of how to minimize the presence of dust and particles in the power plant. The total particle number concentrations and size distributions where measured at 15 points inside the plant with an Engine Exhaust Particle Sizer (EEPS) Spectrometer. The measured particles were mainly in the ultrafine size range. Dust was only visually investigated, since the main purpose was to follow the dust accumulation. The measurement points inside the incineration plant were chosen according to investigate exposure to visitors and workers. At some points probable leakage of emissions were investigated. The measurements were carried out during approximately one month in March–April 2013. The results of the measurements showed that elevated levels of dust and particles are present in the indoor air at the waste incineration plant. The cleanest air was found in the control room, warehouse and office. The most polluted air was near the sources that were investigated due to possible leakage and in the bottom ash hall. However, the concentrations were near measured background concentrations in European cities and no leakage could be detected. The high concentrations were assumed to be a result of a lot of dust and particles present on surfaces that had not been cleaned in a while. The main source of the dust and particles present inside the waste incineration plant was thought to be particles and dust from the outside air. Other activities in the area around the waste incineration facility are ground work activities, stone crushing and traffic, which probably are sources of particle formation. Filtration of the outside air prior entering the facility would probably save personnel and visitors from nuisance and save in cleaning and maintenance costs.
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Mikrohuokoisia membraaneja käytetään monissa suodatussovelluksissa kuten vedenpuhdistuksessa. Tämän työn tavoite oli pinnoittaa suodatinkankaita mikrohuokoisella membraanilla. Membraanimateriaalin ja suodatuskankaan yhdistelmällä tavoiteltiin komposiittimateriaalia, jolla on membraanin selektiivinen erotuskyky ja kankaan mekaaniset ominaisuudet. Tämän työn kirjallisuusosa käsittelee membraanin valmistusta faasi-inversiomenetelmällä, pinnoitteeksi soveltuvia membraanimateriaaleja sekä pinnoitteen lujittamista. Kokeellisessa osassa suodatuskankaalle kehitettiin sopivaa pinnoitusmenetelmää. Pinnoitemateriaaleina käytettiin akryylidispersioainetta, polyamidia ja polysulfonia. Tuloksista huomattiin, ettei akryylidispersioaine soveltunut pinnoitemateriaaliksi. Kangasta onnistuttiin pinnoittamaan polyamidilla ja pinnoitusolosuhteita kontrolloimalla saatiin aikaiseksi pinnoite, joka pysyi kankaassa kiinni ja jonka rakenne koostui noin 12 μm huokosista. Polymeeriliuoksen pitoisuuden huomattiin vaikuttavan pinnoitteen rakenteeseen, mutta siihen jäi edelleen suuria avoimia huokosia. Suuret yksittäiset huokoset laskivat kuplapistepainetta ja tekivät huokoskokojakaumasta leveämmän. Polyamidipitoisuudella 14 ja 16 m–% pinnoite oli tunkeutunut kankaan sisään ja sen rakenne oli huokoinen, mutta pintakerrokseen muodostunut tiivis ihokerros tukki materiaalia. Tulosten perusteella kankaiden pinnoittaminen membraanikerroksella on mahdollista mutta pinnoitusprosessia täytyy edelleen kehittää, jotta päästään pienempään huokoskokoon ja kapeampaan huokoskokojakaumaan pinnoitteessa.
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Enzymatic hydrolysis of lignocellulosic polymers is likely to become one of the key technologies enabling industrial production of liquid biofuels and chemicals from lignocellulosic biomass. Certain types of enzymes are able to hydrolyze cellulose and hemicellulose polymers to shorter units and finally to sugar monomers. These monomeric sugars are environmentally acceptable carbon sources for the production of liquid biofuels, such as bioethanol, and other chemicals, such as organic acids. Liquid biofuels in particular have been shown to contribute to the reduction of net emissions of greenhouse gases. The solid residue of enzymatic hydrolysis is composed mainly of lignin and partially degraded fibers, while the liquid phase contains the produced sugars. It is usually necessary to separate these two phases at some point after the hydrolysis stage. Pressure filtration is an efficient technique for this separation. Solid-liquid separation of biomass suspensions is difficult, because biomass solids are able to retain high amounts of water, which cannot be readily liberated by mechanical separation techniques. Most importantly, the filter cakes formed from biomaterials are compressible, which ultimately means that the separation may not be much improved by increasing the filtration pressure. The use of filter aids can therefore facilitate the filtration significantly. On the other hand, the upstream process conditions have a major influence on the filtration process. This thesis investigates how enzymatic hydrolysis and related process conditions affect the filtration properties of a cardboard suspension. The experimental work consists of pressure filtration and characterization of hydrolysates. The study provides novel information about both issues, as the relationship between enzymatic hydrolysis conditions and subsequent filtration properties has so far not been considered in academic studies. The results of the work reveal that the final degree of hydrolysis is an important factor in the filtration stage. High hydrolysis yield generally increases the average specific cake resistance. Mixing during the hydrolysis stage resulted in undefined changes in the physical properties of the solid residue, causing a high filtration resistance when the mixing intensity was high. Theoretical processing of the mixing data led to an interesting observation: the average specific cake resistance was observed to be linearly proportional to the mixer shear stress. Another finding worth attention is that the size distributions of the solids did not change very dramatically during enzymatic hydrolysis. There was an observable size reduction during the first couple of hours, but after that the size reduction was minimal. Similarly, the size distribution of the suspended solids remained almost constant when the hydrolyzed suspension was subjected to intensive mixing. It was also found that the average specific cake resistance was successfully reduced by the use of filter aids. This reduction depended on the method of how the filter aids were applied. In order to obtain high filtration capacity, it is recommended to use the body feed mode, i.e. to mix the filter aid with the slurry prior to filtration. Regarding the quality of the filtrate, precoat filtration was observed to produce a clear filtrate with negligible suspended solids content, while the body feed filtrates were turbid, irrespective of which type of filter aid was used.
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The dynamics of the tree community and 30 tree populations were examined in an area of tropical semideciduous forest located on the margin of the Rio Grande, SE Brazil, based on surveys done in 1990 and 1997 in three 0.18 ha plots. The main purpose was to assess whether variations in dynamics were related to topography and the effects of a catastrophic flood in 1992. Rates of mortality and recruitment of trees and gain and loss of basal area in two topographic sites, lower (flooded) and upper (non-flooded), were obtained. Projected trajectories of mean and accelerated growth in diameter were obtained for each species. In both topographic sites, mortality rates surpassed recruitment rates, gain rates of basal area surpassed loss rates, and size distributions changed, with declining proportions of smaller trees. These overall changes were possibly related to increased underground water supply after the 1992 flood as well as to a c. 250-year-old process of primary succession on abandoned gold mines. Possible effects of the 1992 flood showed up in the higher proportions of dead trees in the flooded sites and faster growth rates in the flood-free sites. Species of different regeneration guilds showed particular trends with respect to their demographic changes and diameter growth patterns. Nevertheless, patterns of population dynamics differed between topographic sites for only two species.
Influence of surface functionalization on the behavior of silica nanoparticles in biological systems
Resumo:
Personalized nanomedicine has been shown to provide advantages over traditional clinical imaging, diagnosis, and conventional medical treatment. Using nanoparticles can enhance and clarify the clinical targeting and imaging, and lead them exactly to the place in the body that is the goal of treatment. At the same time, one can reduce the side effects that usually occur in the parts of the body that are not targets for treatment. Nanoparticles are of a size that can penetrate into cells. Their surface functionalization offers a way to increase their sensitivity when detecting target molecules. In addition, it increases the potential for flexibility in particle design, their therapeutic function, and variation possibilities in diagnostics. Mesoporous nanoparticles of amorphous silica have attractive physical and chemical characteristics such as particle morphology, controllable pore size, and high surface area and pore volume. Additionally, the surface functionalization of silica nanoparticles is relatively straightforward, which enables optimization of the interaction between the particles and the biological system. The main goal of this study was to prepare traceable and targetable silica nanoparticles for medical applications with a special focus on particle dispersion stability, biocompatibility, and targeting capabilities. Nanoparticle properties are highly particle-size dependent and a good dispersion stability is a prerequisite for active therapeutic and diagnostic agents. In the study it was shown that traceable streptavidin-conjugated silica nanoparticles which exhibit a good dispersibility could be obtained by the suitable choice of a proper surface functionalization route. Theranostic nanoparticles should exhibit sufficient hydrolytic stability to effectively carry the medicine to the target cells after which they should disintegrate and dissolve. Furthermore, the surface groups should stay at the particle surface until the particle has been internalized by the cell in order to optimize cell specificity. Model particles with fluorescently-labeled regions were tested in vitro using light microscopy and image processing technology, which allowed a detailed study of the disintegration and dissolution process. The study showed that nanoparticles degrade more slowly outside, as compared to inside the cell. The main advantage of theranostic agents is their successful targeting in vitro and in vivo. Non-porous nanoparticles using monoclonal antibodies as guiding ligands were tested in vitro in order to follow their targeting ability and internalization. In addition to the targeting that was found successful, a specific internalization route for the particles could be detected. In the last part of the study, the objective was to clarify the feasibility of traceable mesoporous silica nanoparticles, loaded with a hydrophobic cancer drug, being applied for targeted drug delivery in vitro and in vivo. Particles were provided with a small molecular targeting ligand. In the study a significantly higher therapeutic effect could be achieved with nanoparticles compared to free drug. The nanoparticles were biocompatible and stayed in the tumor for a longer time than a free medicine did, before being eliminated by renal excretion. Overall, the results showed that mesoporous silica nanoparticles are biocompatible, biodegradable drug carriers and that cell specificity can be achieved both in vitro and in vivo.
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In this thesis, stepwise titration with hydrochloric acid was used to obtain chemical reactivities and dissolution rates of ground limestones and dolostones of varying geological backgrounds (sedimentary, metamorphic or magmatic). Two different ways of conducting the calculations were used: 1) a first order mathematical model was used to calculate extrapolated initial reactivities (and dissolution rates) at pH 4, and 2) a second order mathematical model was used to acquire integrated mean specific chemical reaction constants (and dissolution rates) at pH 5. The calculations of the reactivities and dissolution rates were based on rate of change of pH and particle size distributions of the sample powders obtained by laser diffraction. The initial dissolution rates at pH 4 were repeatedly higher than previously reported literature values, whereas the dissolution rates at pH 5 were consistent with former observations. Reactivities and dissolution rates varied substantially for dolostones, whereas for limestones and calcareous rocks, the variation can be primarily explained by relatively large sample standard deviations. A list of the dolostone samples in a decreasing order of initial reactivity at pH 4 is: 1) metamorphic dolostones with calcite/dolomite ratio higher than about 6% 2) sedimentary dolostones without calcite 3) metamorphic dolostones with calcite/dolomite ratio lower than about 6% The reactivities and dissolution rates were accompanied by a wide range of experimental techniques to characterise the samples, to reveal how different rocks changed during the dissolution process, and to find out which factors had an influence on their chemical reactivities. An emphasis was put on chemical and morphological changes taking place at the surfaces of the particles via X-ray Photoelectron Spectroscopy (XPS) and Scanning Electron Microscopy (SEM). Supporting chemical information was obtained with X-Ray Fluorescence (XRF) measurements of the samples, and Inductively Coupled Plasma-Mass Spectrometry (ICP-MS) and Inductively Coupled Plasma-Optical Emission Spectrometry (ICP-OES) measurements of the solutions used in the reactivity experiments. Information on mineral (modal) compositions and their occurrence was provided by X-Ray Diffraction (XRD), Energy Dispersive X-ray analysis (EDX) and studying thin sections with a petrographic microscope. BET (Brunauer, Emmet, Teller) surface areas were determined from nitrogen physisorption data. Factors increasing chemical reactivity of dolostones and calcareous rocks were found to be sedimentary origin, higher calcite concentration and smaller quartz concentration. Also, it is assumed that finer grain size and larger BET surface areas increase the reactivity although no certain correlation was found in this thesis. Atomic concentrations did not correlate with the reactivities. Sedimentary dolostones, unlike metamorphic ones, were found to have porous surface structures after dissolution. In addition, conventional (XPS) and synchrotron based (HRXPS) X-ray Photoelectron Spectroscopy were used to study bonding environments on calcite and dolomite surfaces. Both samples are insulators, which is why neutralisation measures such as electron flood gun and a conductive mask were used. Surface core level shifts of 0.7 ± 0.1 eV for Ca 2p spectrum of calcite and 0.75 ± 0.05 eV for Mg 2p and Ca 3s spectra of dolomite were obtained. Some satellite features of Ca 2p, C 1s and O 1s spectra have been suggested to be bulk plasmons. The origin of carbide bonds was suggested to be beam assisted interaction with hydrocarbons found on the surface. The results presented in this thesis are of particular importance for choosing raw materials for wet Flue Gas Desulphurisation (FGD) and construction industry. Wet FGD benefits from high reactivity, whereas construction industry can take advantage of slow reactivity of carbonate rocks often used in the facades of fine buildings. Information on chemical bonding environments may help to create more accurate models for water-rock interactions of carbonates.
Resumo:
Laskeutus ja suodatus ovat paljon tutkittuja ja laajassa käytössä olevia mekaanisia erotusmenetelmiä. Laskeutumisen vaikutusta suodatuksen yhteydessä ei kuitenkaan ole tutkittu juurikaan. Tämän työn tavoitteena on selvittää suodattimessa ennen vakiopaine suodatusta tapahtuvan kiintoaineen laskeutumisen vaikutusta suodatuksen tuloksiin. Työn kirjallisuusosuudessa käsitellään työhön liittyvää teoriaa partikkelikokojakaumista, laskeutumisesta, suodatuksesta ja flokkulanttien käytöstä sekä tehdään yhteenvetoa aiemmasta laskeutumista ja suodatusta yhdistävästä tutkimuksesta. Koska käsitellyt aiheet ovat laajoja ja niitä on useita, joudutaan teorian esittämisessä tekemään rajauksia. Työn kokeellisessa osassa tutkitaan suodattimessa tapahtuvan laskeutuksen vaikutusta suodatukseen. Kokeet suoritetaan 20 m-% kalsiumkarbonaattilietteellä. Kokeissa tutkitaan laskeutumisen vaikutusta antamalla lietteen laskeutua suodattimessa tietyn ajan ennen suodatuksen aloitusta. Lisäksi tutkitaan flokkulanttien lisäämisen vaikutusta mahdollisiin ilmiöihin. Koetuloksista nähdään pidemmän laskeutusajan ennen suodatusta alentavan kakun keskimääräistä ominaisvastusta ja vaikutus kasvaa merkittävästi kun lietteeseen on lisätty flokkulanttia. Suodatusta edeltävä laskeutus siis helpottaa varsinaista suodatusta.
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Litiumioniakkujen kehityksen myötä litiumin tarve ja kysyntä ovat kasvaneet viime vuodet tasaisesti noin 10 % vuosivauhdilla. Kasvun on myös ennustettu jatkuvan samanlaisena tulevaisuudessa, jonka takia erilaiset litiumin erotusprosessit ovat nousseet tutkimuksen kohteeksi. Tärkeimmät litiumlähteet sijaitsevat suola-aavikoilla ja -järvillä, joihin litiumia on kerääntynyt suuria määriä maanpinnan läheisyyteen. Litiumia erotetaan suolatasangoilla aikaa vievissä haihdutus- ja saostusvaiheissa. Suolaliuokset sisältävät litiumin lisäksi muita metalleja, kuten magnesiumia, kalsiumia ja natriumia, joista etenkin magnesium häiritsee litiumin erotusta. Aikaisemmissa tutkimuksissa ei ole löydetty litiumille riittävän selektiivistä ioninvaihtohartsia. Tehdyissä tutkimuksissa muut metallit on usein erotettu selektiivisesti ennen litiumia ja litium on erotettu lopuksi. Litiumin erotusta voitaisiin parantaa, mikäli se onnistuisi selektiivisesti suoraan suolaliuoksesta. Tässä työssä tutkittiin litiumin selektiivistä erotusta magnesium- ja kalsiumpitoisesta väkevästä kloridiliuoksesta ioninvaihtohartseilla sekä molekyyliseulalla. Käytetyt neljä ioninvaihtohartsia olivat kaupallisia Puroliten hartseja: MN200, S940, CT151 ja A170. Molekyyliseula oli Sigman huokoskoon 4 Å zeoliittia. Kromatografisilla kolonnikokeilla saadut näytteet analysoitiin ICP-AES:lla. Tulosten perusteella ei yksikään tutkituista hartseista ja molekyyliseulasta ollut selektiivinen litiumille.
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Työn kirjallisuusosassa selvitettiin neste-nestedispersioiden ja emulsioiden pisarakokojakauman määrittämiseen soveltuvia menetelmiä. Kirjallisuusosa painottuu emulsioiden stabiliteettiin liittyvään teoriaan ja menetelmiin, joilla voidaan tutkia pisarakokojakaumia suoraan prosessista. Erillisnäytteiden analysointiin perustuvista menetelmistä on esitettynä mikroskooppianalyysi sekä lasersäteen sirontaan perustuva mittaus, joita molempia käytettiin tämän työn kokeellisessa osassa. Kokeellisessa osassa pyrittiin selvittämään, vaikuttavatko kaksi erimuotoista ruuvi-kapaletta eri tavalla öljy-vesiemulsion pisarakokojakaumaan, kun emulsio virtasi ruuvin vuorovaikutusalueen läpi. Tätä tutkittiin määrittämällä ennen vuorovaikutusaluetta ja vuorovaikutusalueen jälkeen kerättyjen emulsionäytteiden pisarakokojakaumat lasersäteen sirontamittauksilla. Mitattujen pisarakokojakaumien perusteella ei voitu tehdä varmaa johtopäätöstä, vaikuttivatko ruuvit pisarakokojakaumaan vai eivät. Syynä tähän on pisarakokojakaumien vaihtelu rinnakkaisnäytteissä. Rinnakkaismittauksissa havaittu vaihtelu johtui arvaamattomasti muuttuneista virtausolosuhteista, mikä aiheutti edelleen öljypitoisuuden muutoksia. Muita mahdollisia syitä ovat veden ionivahvuuden, pH:n ja lämpötilan vaihtelu.
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Microscopic visualization, especially in transparent micromodels, can provide valuable information to understand the transport phenomena at pore scale in different process occurring in porous materials (food, timber, soils, etc.). Micromodels studies focus mainly on the observation of multi-phase flow, which presents a greater proximity to reality. The aim of this study was to study the process of flexography and its application in the manufacture of polyester resin transparent micromodels and its application to carrots. Materials used to implement a flexo station for micromodels construction were thermoregulated water bath, exposure chamber to UV light, photosensitive substance (photopolymer), RTV silicone polyester resin, and glass plates. In this paper, data on size distribution of a particular kind of carrot we used, and a transparent micromodel with square cross-section as well as a Log-normal pore size distribution with pore radii ranging from 10 to 110 µm (average of 22 µm and micromodel size of 10 × 10 cm) were built. Finally, it stresses that it has successfully implemented the protocol processing 2D polyester resin transparent micromodels.
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The aim of this thesis research work focused on the carbonate precipitation of magnesium using magnesium hydroxide Mg(OH)2 and carbon dioxide (CO2) gas at ambient temperature and pressure. The rate of dissolution of Mg(OH)2 and precipitation kinetics were investigated under different operating conditions. The conductivity and pH of the solution were inline monitored by a Consort meter and the solid samples gotten from the precipitation reaction were analysed by a laser diffraction analyzer Malvern Mastersizer to obtain particle size distributions (PSD) of crystal samples. Also the Mg2+ concentration profiles were determined from the liquid phase of the precipitate by ion chromatography (IC) analysis. Crystal morphology of the obtained precipitates were also investigated and discussed in this work. For the carbonation reaction of magnesium hydroxide in the present work, it was found that magnesium carbonate trihydrate (nesquehonite) was the main product and its formation occurred at a pH of around 7-8. The stirrer speed has a significant effect on the dissolution rate of Mg(OH)2. The highest obtained Mg2+ concentration level was 0.424 mol L-l for the 470 rpm and 0.387 mol L-1 for the 560 rpm which corresponded to the processing time of 45 mins and 40 mins respectively. The particle size distribution shows that the average particle size keeps increasing during the reaction as the CO2 is been fed to the system. The carbonation process is kinetically favored and simple as nesquehonite formation occurs in a very short time. It is a thermodynamically and chemically stable solid product, which allows for a long-term storage of CO2. Since the carbonation reaction is a complex system which includes dissolution of magnesium hydroxide particles, absorption of CO2, chemical reaction and crystallization, the dissolution of magnesium hydroxide was studied in hydrochloric acid (HCl) solvent with and without nitrogen (N2) inert gas. It was found on the dissolution part that the impeller speed had effect on the dissolution rate. The higher the impeller speed the higher the pH of the solution, although for the highest speed of 650rpm it was not the case. Therefore, it was concluded that the optimum speed of the stirrer was 560rpm. The influence of inert gas N2 on the dissolution rate of Mg(OH)2 particles could be seen based on measured pH, electric conductivity and Mg2+ concentration curves.
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Tässä työssä testattiin partikkelikokojakaumien analysoinnissa käytettävää kuvankäsittelyohjelmaa INCA Feature. Partikkelikokojakaumat määritettiin elektronimikroskooppikuvista INCA Feature ohjelmaa käyttäen partikkeleiden projektiokuvista päällystyspigmenttinä käytettävälle talkille ja kahdelle eri karbonaattilaadulle. Lisäksi määritettiin partikkelikokojakaumat suodatuksessa ja puhdistuksessa apuaineina käytettäville piidioksidi- ja alumiinioksidihiukkasille. Kuvankäsittelyohjelmalla määritettyjä partikkelikokojakaumia verrattiin partikkelin laskeutumisnopeuteen eli sedimentaatioon perustuvalla SediGraph 5100 analysaattorilla ja laserdiffraktioon perustuvalla Coulter LS 230 menetelmällä analysoituihin partikkelikokojakaumiin. SediGraph 5100 ja kuva-analyysiohjelma antoivat talkkipartikkelien kokojakaumalle hyvin samankaltaisen keskiarvon. Sen sijaan Coulter LS 230 laitteen antama kokojakauman keskiarvo poikkesi edellisistä. Kaikki vertailussa olleet partikkelikokojakaumamenetelmät asettivat eri näytteiden partikkelit samaan kokojärjestykseen. Kuitenkaan menetelmien tuloksia ei voida numeerisesti verrata toisiinsa, sillä kaikissa käytetyissä analyysimenetelmissä partikkelikoon mittaus perustuu partikkelin eri ominaisuuteen. Työn perusteella kaikki testatut analyysimenetelmät soveltuvat paperipigmenttien partikkelikokojakaumien määrittämiseen. Tässä työssä selvitettiin myös kuva-analyysiin tarvittava partikkelien lukumäärä, jolla analyysitulos on luotettava. Työssä todettiin, että analysoitavien partikkelien lukumäärän tulee olla vähintään 300 partikkelia. Liian suuri näytemäärä lisää kokojakauman hajontaa ja pidentää analyysiin käytettyä aikaa useaan tuntiin. Näytteenkäsittely vaatii vielä lisää tutkimuksia, sillä se on tärkein ja kriittisin vaihe SEM ja kuva-analyysiohjelmalla tehtävää partikkelikokoanalyysiä. Automaattisten mikroskooppien yleistyminen helpottaa ja nopeuttaa analyysien tekoa, jolloin menetelmän suosio tulee kasvamaan myös paperipigmenttien tutkimuksessa. Laitteiden korkea hinta ja käyttäjältä vaadittava eritysosaaminen tulevat rajaamaan käytön ainakin toistaiseksi tutkimuslaitoksiin.
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The objectives of this master’s thesis were to understand the importance of bubbling fluidized bed (BFB) conditions and to find out how digital image processing and acoustic emission technology can help in monitoring the bed quality. An acoustic emission (AE) measurement system and a bottom ash camera system were evaluated in acquiring information about the bed conditions. The theory part of the study describes the fundamentals of BFB boiler and evaluates the characteristics of bubbling bed. Causes and effects of bed material coarsening are explained. The ways and methods to monitor the behaviour of BFB are determined. The study introduces the operating principles of AE technology and digital image processing. The empirical part of the study describes an experimental arrangement and results of a case study at an industrial BFB boiler. Sand consumption of the boiler was reduced by optimization of bottom ash handling and sand feeding. Furthermore, data from the AE measurement system and the bottom ash camera system was collected. The feasibility of these two systems was evaluated. The particle size of bottom ash and the changes in particle size distribution were monitored during the test period. Neither of the systems evaluated was ready to serve in bed quality control accurately or fast enough. Particle size distributions according to the bottom ash camera did not correspond to the results of manual sieving. Comprehensive interpretation of the collected AE data requires much experience. Both technologies do have potential and with more research and development they may enable acquiring reliable and real-time information about the bed conditions. This information could help to maintain disturbance-free combustion process and to optimize bottom ash handling system.
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The relationships among chick feeding, size and type of prey item, and foraging time away from the brood have not been well studied in seabirds. This study investigated spatial and temporal patterns of foraging and chick-provisioning among 23 radio-tagged male common terns nesting at Hamilton Harbour, Lake Ontario during 1991 and 1992. Telemetry data were collected concurrently with behavioural observations from an elevated blind. Terns fitted with transmitters did not differ from controls with respect to either brood attendance, patterns of chick mortality, species and size distributions of prey delivered to offspring, or chick-provisioning rates. There was a clear separation of parental roles: males were primarily responsible for feeding chicks while females allocated more time to brood attendance. The prey species most commonly delivered to chicks by adults were rainbow smelt (Osmerus mordax) and alewife (A/osa pseudoharengus), followed in importance by larval fish, emerald shiner (Notropis antherinoides), salmonids, and fathead minnows (Pimepha/es prome/as). The relative proportions of various fish speCies delivered to chicks by males differed over the course of each breeding season, and there was also much variability in species composition of prey between years. Sizes of prey delivered to chicks also differed between sampling periods. The modal size of fish brought to chicks during Peak 1991 was 1.5 bill lengths, while the majority of prey in Late 1991 were small larval fish. The reverse trend occurred in 1992 when small fish were delivered to chicks predominantly during the Peak nesting period. During periods when predominantly small fish were delivered to chicks, the foraging activity of radio-tagged males was concentrated within a two kilometer radius of the colony. The observed variation in prey composition and foraging locations during the study likely reflects temporal variation in the availability of prey in the vicinity of the colony. Males delivered fish to chicks at a constant rate, while females 4 increased their feeding frequency over the first six to ten brood days. The mean length of fish delivered to chicks by adults increased significantly with increasing chick age. As a group, within each nesting period, transmittered males either foraged predominantly in the same directional bearing (north during Peak 1991, south during Late 1992), or concentrated foraging activity in the immediate vicinity of the colony (Late 1991, Peak 1992). However, individual radio-tagged males exhibited unique and predictable foraging patterns, often favouring specific locations within these areas and differing in their secondary foraging patterns. Overall, the Lake Ontario shoreline between NCB Bay" (3.5 km south of colony) and the lift bridge canal (4 km north of colony) was the foraging area used most frequently by radiotagged males during the chick-rearing period. Foraging patterns of transmittered males at Windermere Basin are similar to patterns of peak-nesting common terns, but differ from those of late-nesters, at a nearby colony (Port Colborne, Lake Erie). Differences between the foraging patterns of late-nesting terns at these colonies likely reflect differences in annual patterns of fish availability between the two locations. No relationship was found between foraging proficiency of adults and survival of offspring. Stochastic factors, such as predation by black-crowned nightherons (Nycticorax nycticorax) and adverse weather conditions during the early stages of chick rearing, may be more important determinants of common tern breeding success than parental quality or fish availability.
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La réduction de la taille des particules jusqu’à l’obtention de nanocristaux est l’une des approches utilisées afin d’améliorer la pénétration cutanée des médicaments à usage topique. Nous proposons que la fabrication d’une formulation semi solide (hydrogel) à base de nanosuspension de docosanol, aboutira à une diffusion du principe actif supérieure à celle du produit commercial Abreva®, à travers des membranes synthétiques de polycarbonates. Le broyage humide est la technique proposée pour la production des nanoparticules de docosanol. Nous proposons aussi la préparation d’une formulation semi-solide (hydrogel) à usage topique à partir de la nanosuspension de docosanol. La nanosuspension de docosanol est obtenue par dispersion du docosanol en solution aqueuse en présence du polymère stabilisant hydroxypropylcellulose (HPC) et du surfactant laurylsulfate de sodium (SDS) suivi d’un broyage humide à faible ou à haute énergie. L’hydrogel de docosanol nanoformulé est préparé à l’aide de la nanosuspension de docosanol qui subit une gélification par le carbopol Ultrez 21 sous agitation mécanique suivie d’une neutralisation au triéthanolamine TEA. La taille des particules de la nanosuspension et de l’hydrogel a été déterminée par diffusion dynamique de la lumière (DLS). Une méthode analytique de chromatographie liquide à haute performance (HPLC) munie d’un détecteur évaporatif (ELSD) a été développée et validée pour évaluer la teneur de docosanol dans les préparations liquides, dans les différentes nanosuspensions et dans les hydrogels de docosanol. L’état de cristallinité des nanocristaux dans la nanosuspension et dans l’hydrogel a été étudié par calorimétrie différentielle à balayage. La morphologie de la nanosuspension et de l’hydrogel de docosanol a été examinée par microscopie électronique à balayage (MEB). Les propriétés rhéologiques et de stabilité physique à différentes températures ont été aussi étudiées pour la formulation semi-solide (hydrogel). De même, la libération in vitro du docosanol contenu dans l’hydrogel et dans le produit commercial Abreva® a été étudiée à travers deux membranes de polycarbonates de taille de pores 400 et 800 nm. Dans le cas de nanosuspensions, des cristaux de docosanol de taille nanométrique ont été produits avec succès par broyage humide. Les nanoparticules de tailles variant de 197 nm à 312 nm ont été produites pour des pourcentages différents en docosanol, en polymère HPC et en surfactant SDS. Après lyophilisation, une augmentation de la taille dépendant de la composition de la formulation a été observée tout en restant dans la gamme nanométrique pour la totalité presque des formulations étudiées. Dans le cas des hydrogels examinés, la taille moyenne des particules de docosanol est maintenue dans la gamme nanométrique avant et après lyophilisation. L’analyse thermique des mélanges physiques, des nanosuspensions et des hydrogels de docosanol a révélé la conservation de l’état de cristallinité des nanocristaux de docosanol après broyage et aussi après gélification. L’examen par microscopie électronique à balayage (MEB) a montré que la nanosuspension et l’hydrogel ont tous deux une morphologie régulière et les nanoparticules ont une forme sphérique. De plus les nanoparticules de la nanosuspension ont presque la même taille inférieure à 300 nm en accord avec le résultat obtenu par diffusion dynamique de la lumière (DLS). Les nanoparticules de l’hydrogel ont une légère augmentation de taille par rapport à celle de la nanosuspension, ce qui est en accord avec les mesures de DLS. D’après les mesures rhéologiques, l’hydrogel de docosanol a un comportement pseudoplastique et un faible degré de thixotropie. L’étude de stabilité physique a montré que les formulations d’hydrogel sont stables à basse température (5°C) et à température ambiante (21°C) pendant une période d’incubation de 13 semaines et instable au-delà de 30°C après deux semaines. La méthode HPLC-ELSD a révélé des teneurs en docosanol comprises entre 90% et 110% dans le cas des nanosuspensions et aux alentours de 100% dans le cas de l’hydrogel. L’essai de diffusion in vitro a montré qu’il y a diffusion de docosanol de l’hydrogel à travers les membranes de polycarbonates, qui est plus marquée pour celle de pore 800 nm, tandis que celui du produit commercial Abreva® ne diffuse pas. Le broyage humide est une technique bien adaptée pour la préparation des nanosuspensions docosanol. Ces nanosuspensions peuvent être utilisée comme base pour la préparation de l’hydrogel de docosanol nanoformulé.