Size dependence of refractive index of Si nanoclusters embedded in SiO2

he complex refractive index of SiO2 layers containing Si nanoclusters (Si-nc) has been measured by spectroscopic ellipsometry in the range from 1.5 to 5.0 eV. It has been correlated with the amount of Si excess accurately measured by x-ray photoelectron spectroscopy and the nanocluster size determined by energy-filtered transmission electron microscopy. The Si-nc embedded in SiO2 have been produced by a fourfold Si+ ion implantation, providing uniform Si excess aimed at a reliable ellipsometric modeling. The complex refractive index of the Si-nc phase has been calculated by the application of the Bruggeman effective-medium approximation to the composite media. The characteristic resonances of the refractive index and extinction coefficient of bulk Si vanish out in Si-nc. In agreement with theoretical simulations, a significant reduction of the refractive index of Si-nc is observed, in comparison with bulk and amorphous silicon. The knowledge of the optical properties of these composite layers is crucial for the realization of Si-based waveguides and light-emitting devices.

Bipolar pulsed excitation of erbium-doped nanosilicon light emitting diodes

High quantum efficiency erbium doped silicon nanocluster (Si-NC:Er) light emitting diodes (LEDs) were grown by low-pressure chemical vapor deposition (LPCVD) in a complementary metal-oxide-semiconductor (CMOS) line. Erbium (Er) excitation mechanisms under direct current (DC) and bipolar pulsed electrical injection were studied in a broad range of excitation voltages and frequencies. Under DC excitation, Fowler-Nordheim tunneling of electrons is mediated by Er-related trap states and electroluminescence originates from impact excitation of Er ions. When the bipolar pulsed electrical injection is used, the electron transport and Er excitation mechanism change. Sequential injection of electrons and holes into silicon nanoclusters takes place and nonradiative energy transfer to Er ions is observed. This mechanism occurs in a range of lower driving voltages than those observed in DC and injection frequencies higher than the Er emission rate.

Exposure to solute stress affects genome-wide expression but not the polycyclic aromatic hydrocarbon-degrading activity of Sphingomonas sp. strain LH128 in biofilms.

Members of the genus Sphingomonas are important catalysts for removal of polycyclic aromatic hydrocarbons (PAHs) in soil, but their activity can be affected by various stress factors. This study examines the physiological and genome-wide transcription response of the phenanthrene-degrading Sphingomonas sp. strain LH128 in biofilms to solute stress (invoked by 450 mM NaCl solution), either as an acute (4-h) or a chronic (3-day) exposure. The degree of membrane fatty acid saturation was increased as a response to chronic stress. Oxygen consumption in the biofilms and phenanthrene mineralization activities of biofilm cells were, however, not significantly affected after imposing either acute or chronic stress. This finding was in agreement with the transcriptomic data, since genes involved in PAH degradation were not differentially expressed in stressed conditions compared to nonstressed conditions. The transcriptomic data suggest that LH128 adapts to NaCl stress by (i) increasing the expression of genes coping with osmolytic and ionic stress such as biosynthesis of compatible solutes and regulation of ion homeostasis, (ii) increasing the expression of genes involved in general stress response, (iii) changing the expression of general and specific regulatory functions, and (iv) decreasing the expression of protein synthesis such as proteins involved in motility. Differences in gene expression between cells under acute and chronic stress suggest that LH128 goes through changes in genome-wide expression to fully adapt to NaCl stress, without significantly changing phenanthrene degrading activity.

Iowa Power Fund Board Project Report Update, November 12, 2008

ISU’s proposed research will (1) develop methods for designing clean and efficient burners for low‐Btu producer gas and medium‐Btu syngas, (2) develop catalysts and flow reactors to produce ethanol from medium‐Btu synthesis gas, and (3) upgrade the BECON gasifier system to enable medium‐Btu syngas production and greatly enhanced capabilities for detailed gas analysis needed by both (1) and (2). This project addresses core development needs to enable grain ethanol industry reduce its natural gas demand and ultimately transition to cellulosic ethanol production.

Real-time monitoring of the silicidation process of tungsten filaments at high temperature used as catalysers for silane decomposition

The scope of this work is the systematic study of the silicidation process affecting tungsten filaments at high temperature (1900ºC) used for silane decomposition in the hot-wire chemical vapour deposition technique (HWCVD). The correlation between the electrical resistance evolution of the filaments, Rfil(t), and the different stages of the their silicidation process is exposed. Said stages correspond to: the rapid formation of two WSi2 fronts at the cold ends of the filaments and their further propagation towards the middle of the filaments; and, regarding the hot central portion of the filaments: a initial stage of silicon dissolution into the tungsten bulk, with a random duration for as-manufactured filaments, followed by the inhomogeneous nucleation of W5Si3 (which is later replaced by WSi2) and its further growth towards the filaments core. An electrical model is used to obtain real-time information about the current status of the filaments silicidation process by simply monitoring their Rfil(t) evolution during the HWCVD process. It is shown that implementing an annealing pre-treatment to the filaments leads to a clearly repetitive trend in the monitored Rfil(t) signatures. The influence of hydrogen dilution of silane on the filaments silicidation process is also discussed.

Lipase Improvement: Goals and strategies

Lipases have received great attention as industrial biocatalysts in areas like oils and fats processing, detergents, baking, cheese making, surface cleaning, or fine chemistry . They can catalyse reactions of insoluble substrates at the lipid-water interface, preserving their catalytic activity in organic solvents. This makes of lipases powerful tools for catalysing not only hydrolysis, but also various reverse reactions such as esterification, transesterification, aminolysis, or thiotransesterifications in anhydrous organic solvents. Moreover, lipases catalyse reactions with high specificity, regio and enantioselectivity, becoming the most used enzymes in synthetic organic chemistry. Therefore, they display important advantages over classical catalysts, as they can catalyse reactions with reduced side products, lowered waste treatment costs, and under mild temperature and pressure conditions. Accordingly, the use of lipases holds a great promise for green and economical process chemistry.

Iowa Department of Cultural Affairs; Culture Connects Iowa, FY13-FY15

Iowa Department of Cultural Affairs’ FY13-FY15 Annual Report. The department recently developed a new mission and vision to focus our efforts and ensure everything we do is in the best interest of Iowans. As we move forward, we will empower Iowa to build and sustain culturally vibrant communities by connecting Iowans to the people, places and points of pride that define our state. The department will accomplish this mission through the collective efforts of the various entities under our umbrella, including the Iowa Arts Council, State Historical Society of Iowa and Produce Iowa: State Office of Media Production. The impact of the Iowa Department of Cultural Affairs on our state can be measured through quality of life initiatives that are catalysts for attracting, recruiting and retaining jobs, companies, and talent to Iowa.

Nucleophile-Catalyzed Additions to Activated Triple Bonds. Protection of Lactams, Imides, and Nucleosides with MocVinyl and Related Groups

Additions of lactams, imides, (S)-4-benzyl-1,3-oxazolidin-2-one, 2-pyridone, pyrimidine-2,4-diones (AZT derivatives), or inosines to the electron-deficient triple bonds of methyl propynoate, tert-butyl propynoate, 3-butyn-2-one, N-propynoylmorpholine, or N-methoxy-N-methylpropynamide in the presence of many potential catalysts were examined. DABCO and, second, DMAP appeared to be the best (highest reaction rates and E/Z ratios), while RuCl3, RuClCp*(PPh3)2, AuCl, AuCl(PPh3), CuI, and Cu2(OTf)2 were incapable of catalyzing such additions. The groups incorporated (for example, the 2-(methoxycarbonyl)ethenyl group that we name MocVinyl) serve as protecting groups for the above-mentioned heterocyclic CONH or CONHCO moieties. Deprotections were accomplished via exchange with good nucleophiles: the 1-dodecanethiolate anion turned out to be the most general and efficient reagent, but in some particular cases other nucleophiles also worked (e.g., MocVinyl-inosines can be cleaved with succinimide anion). Some structural and mechanistic details have been accounted for with the help of DFT and MP2 calculations.

Role of peroxynitrite in the cardiovascular dysfunction of septic shock.

The intense systemic inflammatory response characterizing septic shock is associated with an increased generation of free radicals by multiple cell types in cardiovascular and non cardiovascular tissues. The oxygen-centered radical superoxide anion (O2 .-) rapidly reacts with the nitrogen-centered radical nitric oxide (NO.) to form the potent oxidant species peroxynitrite. Peroxynitrite oxidizes multiple targets molecules, either directly or via the secondary generation of highly reactive radicals, resulting in significant alterations in lipids, proteins and nucleic acids, with significant cytotoxic consequences. The formation of peroxynitrite is a key pathophysiological mechanism contributing to the cardiovascular collapse of septic shock, promoting vascular contractile failure, endothelial and myocardial dysfunction, and is also implicated in the occurrence of multiple organ dysfunction in this setting. The recent development of various porphyrin-based pharmacological compounds accelerating the degradation of peroxynitrite has allowed to specifically address these pathophysiological roles of peroxynitrite in experimental septic shock. Such agents, including 5,10,15,20-tetrakis(4- sulfonatophenyl)porphyrinato iron III chloride (FeTTPs), manganese tetrakis(4-N-methylpyridyl)porphyrin (MnTMPyP), Fe(III) tetrakis-2-(N-triethylene glycol monomethyl ether)pyridyl porphyrin) (FP-15) and WW-85, have been shown to improve the cardiovascular and multiple organ failure in small and large animal models of septic shock. Therefore, these findings support the development of peroxynitrite decomposition catalysts as potentially useful novel therapeutic agents to restore cardiovascular function in sepsis.

Nucleophile-Catalyzed Additions to Activated Triple Bonds. Protection of Lactams, Imides, and Nucleosides with MocVinyl and Related Groups

Additions of lactams, imides, (S)-4-benzyl-1,3-oxazolidin-2-one, 2-pyridone, pyrimidine-2,4-diones (AZT derivatives), or inosines to the electron-deficient triple bonds of methyl propynoate, tert-butyl propynoate, 3-butyn-2-one, N-propynoylmorpholine, or N-methoxy-N-methylpropynamide in the presence of many potential catalysts were examined. DABCO and, second, DMAP appeared to be the best (highest reaction rates and E/Z ratios), while RuCl3, RuClCp*(PPh3)2, AuCl, AuCl(PPh3), CuI, and Cu2(OTf)2 were incapable of catalyzing such additions. The groups incorporated (for example, the 2-(methoxycarbonyl)ethenyl group that we name MocVinyl) serve as protecting groups for the above-mentioned heterocyclic CONH or CONHCO moieties. Deprotections were accomplished via exchange with good nucleophiles: the 1-dodecanethiolate anion turned out to be the most general and efficient reagent, but in some particular cases other nucleophiles also worked (e.g., MocVinyl-inosines can be cleaved with succinimide anion). Some structural and mechanistic details have been accounted for with the help of DFT and MP2 calculations.

Unsaturated Polyester Resins from Recycled Polyethyleneterephthalate

Tämän diplomityön tarkoituksena oli tutkia miten kuluttajien kierrättämästä polyeteenitereftalaatista ( PET ) voi valmistaa tyydyttymättömiä polyesterihartseja. Työssä valmistettiin yleiskäyttöön soveltuva laminointihartsi sekä 'gel coat' -hartsi jota käytetään esim. veneiden pintamaalina. Yleishartsin depolymerointiin käytettiin propyleeniglykolia ja 'gel coat' -hartsin valmistamiseen neopentyyliglykolia. Polykondensaatiovaiheessa reaktioon lisättiin maleiinihappoa ja lopuksi hartsit liuotettiin styreeniin. Kirjallisuusosassa esitetään eri menetelmiä PET:n depolymeroimiseksi. Lisäksi esitetään eri vaihtoehtoja glykolien, happojen, katalyyttien ja vinyylimonomeerien valitsemiseksi tyydyttymättömien polyesterihartsien valmistuksessa. Analyysimenetelmiä nestemäisten ja kovetettujen hartsien tutkimiseen ja vertailuun käydään läpi kuten myös erilaisia sovelluksia polyesterihartsien käyttämiseksi. Kokeellinen osa todisti että PET-pullojäte voidaan prosessoida hartsiksiilman uusia investointeja prosessilaitteistoon. PET:n glykolyysi kesti viidestäseitsemään tuntia ja polykondensaatiovaihe kahdesta ja puolesta viiteen tuntiin. Hartsien molekyylipainot ja mekaanisten testien tulokset olivat vertailukelpoisia kaupallisten hartsien antamien tulosten kanssa. Glykolyysivaiheen momomeeri- ja oligomeeripitoisuudet mitattiin geelipermeaatiokromatografialla, jotta nähtiin miten pitkälle depolymerisaatio oli edennyt. Tätä tietoa voidaan hyödyntää uusien hartsireseptin suunnittelussa. Polymeeriketjussa jäljellä olevien C=C kaksoissidosten määrä ja niiden isomeraatioaste maleaattimuodosta fumaraattimuotoon mitattiin 1H-NMR -menetelmällä. Tislevesien koostumus määritettiin kaasukromatografialla, ja tulokset kertoivat katalyytin sisältämän kloorin reagoineen glykolien kanssa, johtaen suureen glykolikulutukseen ja muihin ei-toivottuihin sivureaktioihin. Hartsien sietokykyä auringon valolle mitattiin niiden UV-absorption avulla. Kummastakin hartsista valmistettiin 'gel coat' -maalit jotkalaitettiin sääkoneeseen, joka simuloi auringonpaistetta ja vesisadetta vuorotellen. Näistä 'gel coateista' mitattiin niiden kellastumista. Kummastakin hartsista tehdyt valut asetettiin myös sääkoneeseen ja IR-spektreistä ennen jajälkeen koetta nähtiin että C=O ja C-O esterisidoksia oli hajonnut.

Selective catalytic reduction of nitrogen oxides with ammonia in forced unsteady state reactors - Case based reasoning and mathematical model simulation reasoning

The application of forced unsteady-state reactors in case of selective catalytic reduction of nitrogen oxides (NOx) with ammonia (NH3) is sustained by the fact that favorable temperature and composition distributions which cannot be achieved in any steady-state regime can be obtained by means of unsteady-state operations. In a normal way of operation the low exothermicity of the selective catalytic reduction (SCR) reaction (usually carried out in the range of 280-350°C) is not enough to maintain by itself the chemical reaction. A normal mode of operation usually requires supply of supplementary heat increasing in this way the overall process operation cost. Through forced unsteady-state operation, the main advantage that can be obtained when exothermic reactions take place is the possibility of trapping, beside the ammonia, the moving heat wave inside the catalytic bed. The unsteady state-operation enables the exploitation of the thermal storage capacity of the catalyticbed. The catalytic bed acts as a regenerative heat exchanger allowing auto-thermal behaviour when the adiabatic temperature rise is low. Finding the optimum reactor configuration, employing the most suitable operation model and identifying the reactor behavior are highly important steps in order to configure a proper device for industrial applications. The Reverse Flow Reactor (RFR) - a forced unsteady state reactor - corresponds to the above mentioned characteristics and may be employed as an efficient device for the treatment of dilute pollutant mixtures. As a main disadvantage, beside its advantages, the RFR presents the 'wash out' phenomena. This phenomenon represents emissions of unconverted reactants at every switch of the flow direction. As a consequence our attention was focused on finding an alternative reactor configuration for RFR which is not affected by the incontrollable emissions of unconverted reactants. In this respect the Reactor Network (RN) was investigated. Its configuration consists of several reactors connected in a closed sequence, simulating a moving bed by changing the reactants feeding position. In the RN the flow direction is maintained in the same way ensuring uniformcatalyst exploitation and in the same time the 'wash out' phenomena is annulated. The simulated moving bed (SMB) can operate in transient mode giving practically constant exit concentration and high conversion levels. The main advantage of the reactor network operation is emphasizedby the possibility to obtain auto-thermal behavior with nearly uniformcatalyst utilization. However, the reactor network presents only a small range of switching times which allow to reach and to maintain an ignited state. Even so a proper study of the complex behavior of the RN may give the necessary information to overcome all the difficulties that can appear in the RN operation. The unsteady-state reactors complexity arises from the fact that these reactor types are characterized by short contact times and complex interaction between heat and mass transportphenomena. Such complex interactions can give rise to a remarkable complex dynamic behavior characterized by a set of spatial-temporal patterns, chaotic changes in concentration and traveling waves of heat or chemical reactivity. The main efforts of the current research studies concern the improvement of contact modalities between reactants, the possibility of thermal wave storage inside the reactor and the improvement of the kinetic activity of the catalyst used. Paying attention to the above mentioned aspects is important when higher activity even at low feeding temperatures and low emissions of unconverted reactants are the main operation concerns. Also, the prediction of the reactor pseudo or steady-state performance (regarding the conversion, selectivity and thermal behavior) and the dynamicreactor response during exploitation are important aspects in finding the optimal control strategy for the forced unsteady state catalytic tubular reactors. The design of an adapted reactor requires knowledge about the influence of its operating conditions on the overall process performance and a precise evaluation of the operating parameters rage for which a sustained dynamic behavior is obtained. An apriori estimation of the system parameters result in diminution of the computational efforts. Usually the convergence of unsteady state reactor systems requires integration over hundreds of cycles depending on the initial guess of the parameter values. The investigation of various operation models and thermal transfer strategies give reliable means to obtain recuperative and regenerative devices which are capable to maintain an auto-thermal behavior in case of low exothermic reactions. In the present research work a gradual analysis of the SCR of NOx with ammonia process in forced unsteady-state reactors was realized. The investigation covers the presentationof the general problematic related to the effect of noxious emissions in the environment, the analysis of the suitable catalysts types for the process, the mathematical analysis approach for modeling and finding the system solutions and the experimental investigation of the device found to be more suitable for the present process. In order to gain information about the forced unsteady state reactor design, operation, important system parameters and their values, mathematical description, mathematicalmethod for solving systems of partial differential equations and other specific aspects, in a fast and easy way, and a case based reasoning (CBR) approach has been used. This approach, using the experience of past similarproblems and their adapted solutions, may provide a method for gaining informations and solutions for new problems related to the forced unsteady state reactors technology. As a consequence a CBR system was implemented and a corresponding tool was developed. Further on, grooving up the hypothesis of isothermal operation, the investigation by means of numerical simulation of the feasibility of the SCR of NOx with ammonia in the RFRand in the RN with variable feeding position was realized. The hypothesis of non-isothermal operation was taken into account because in our opinion ifa commercial catalyst is considered, is not possible to modify the chemical activity and its adsorptive capacity to improve the operation butis possible to change the operation regime. In order to identify the most suitable device for the unsteady state reduction of NOx with ammonia, considering the perspective of recuperative and regenerative devices, a comparative analysis of the above mentioned two devices performance was realized. The assumption of isothermal conditions in the beginningof the forced unsteadystate investigation allowed the simplification of the analysis enabling to focus on the impact of the conditions and mode of operation on the dynamic features caused by the trapping of one reactant in the reactor, without considering the impact of thermal effect on overall reactor performance. The non-isothermal system approach has been investigated in order to point out the important influence of the thermal effect on overall reactor performance, studying the possibility of RFR and RN utilization as recuperative and regenerative devices and the possibility of achieving a sustained auto-thermal behavior in case of lowexothermic reaction of SCR of NOx with ammonia and low temperature gasfeeding. Beside the influence of the thermal effect, the influence of the principal operating parameters, as switching time, inlet flow rate and initial catalyst temperature have been stressed. This analysis is important not only because it allows a comparison between the two devices and optimisation of the operation, but also the switching time is the main operating parameter. An appropriate choice of this parameter enables the fulfilment of the process constraints. The level of the conversions achieved, the more uniform temperature profiles, the uniformity ofcatalyst exploitation and the much simpler mode of operation imposed the RN as a much more suitable device for SCR of NOx with ammonia, in usual operation and also in the perspective of control strategy implementation. Theoretical simplified models have also been proposed in order to describe the forced unsteady state reactors performance and to estimate their internal temperature and concentration profiles. The general idea was to extend the study of catalytic reactor dynamics taking into account the perspectives that haven't been analyzed yet. The experimental investigation ofRN revealed a good agreement between the data obtained by model simulation and the ones obtained experimentally.

Sisäisten donorien vaikutus Polypropeeni Ziegler-Natta katalyytissä

Tässä työssä tutkittiin erilaisten sisäisten donorien vaikutusta polypropeenin ominaisuuksiin käytettäessä Ziegler-Natta-katalyyttiä, joka valmistettiin Borealiksen aiemmin kehittämällä kaksifaasimenetelmällä. Tällä uudella menetelmällä katalyytti voidaan valmistaa ilman lisättyä sisäistä donoria ja kantajaa. Katalyyttihiukkaset saadaan kaksifaasisysteemin ansiosta muodoltaan pyöreiksi. Työn kokeellisessa osassa valmistettiin erilaisia Mg-komplekseja, jossa sisäinen donori muodostuu in-situ alkoholin ja karboksyylihappokloridin reagoidessa keskenään. Katalyyttisynteesissä Mg-kompleksi reagoi TiCl4:n kanssa. Saatujen katalyyttien ominaisuuksia testattiin polymeroimalla niillä propeenia 70 °C:ssa tunnin ajan. Polymeerien ominaisuuksia tutkittiin useiden eri karakterisointimenetelmien avulla. Lisäksi tutkittiin mahdollisuutta valmistaa katalyytti, joka ei sisältäisi ftalaattia. Työssä havaittiin, että katalyytin valmistusmenetelmä on käyttökelpoinen myös muilla sisäisillä donoreilla kuin referenssinä käytetyllä DOP:lla. Kaksiliuosfaasi-systeemi saatiin aikaan myös kahdella muulla työssä tutkitulla sisäisellä donorilla. Lisäksi faasitasapainokokeissa kahden liuosfaasin systeemi saatiin aikaan sisäisellä donorilla, joka ei sisältänyt ftalaattia. Kyseisellä katalyytillä havaittiin olevan muista katalyyteistä poikkeavia ominaisuuksia. Esimerkiksi se antoi matalamman isotaktisuuden kuin referenssikatalyytti ja se saattaisikin soveltua matalan isotaktisuuden pehmeille tuotteille. Työssä kokeiltiin yhdellä uudella katalyytillä myös eteenin polymerointia, sillä katalyytin donoripitoisuus oli hyvin matala. Katalyytin aktiivisuus eteenipolymeroinnissa oli varsin hyvä.

Kaasutuskaasun puhdistus

Tässä diplomityössä on selvitetty hiilestä, jätteestä tai biopolttoaineesta kaasutetun kaasun märkä- ja kuivapuhdistusta. Kaasutuskaasun puhdistuksella voidaan likainen ja jopa ongelmallinen aines muuttaa tai puhdistaa sellaiseksi ympäristökelpoiseksi polttoaineeksi, että sitä voidaan käyttää nykyisissä kulutuskohteissa ongelmitta. Lisäkannustusta kaasutuskaasun puhdistus saa uusista EU-direktiiveistä, jotka tulevat rajoittamaan jätteiden läjittämistä kaatopaikoille. Loppusijoitukseen meneviä jätevirtoja voidaan energiakäytöllä pienentää huomattavasti.Työ on tehty PVO-Engineering Oy:n voimalaitostekniikan osastolle kevään 2001 aikana. Työn tavoitteena oli kasvattaa yrityksen tietomäärää kaasutuskaasun puhdistuksen osalta. Lisäksi pyrittiin selvittämään uuden keraamisen pussisuodatinmateriaalin käyttöä kaasutuskaasun kuumakuivasuodatuksessa. Työn ensimmäisessä osassa esitetään kaasutuskaasun koostumuksen ja syntymisen lisäksi tämän työn lähtökohdat ja tavoitteet. Toisessa osassa selvitetään kaasulle asetettavia vaatimuksia eri käyttötapojen mukaan. Kolmannessa ja neljännessä osassa selvitetään puhdistettavien komponenttien käyttäytymistä ja sopivia puhdistusmenetelmiä.Kaasutuskaasun puhdistustekniikka vaihtelee paljonkin riippuen kaasun käyttökohteesta. Eroja syntyy käyttökohteen asetettamista vaatimuksista polttoaineelle, kaasutettavan polttoaineen koostumuksesta ja laadun vaihtelusta. Puhdistuksessa keskitytään kloori -, rikki -, typpi - ja metalliyhdisteiden poistamiseen kaasuvirrasta. Erotuskyvyllä arvioituna eri puhdistusmenetelmistä tehokkaimpia ovat pesurisähkösuodatinyhdistelmät. Niiden suuret jätemäärät ovat kuitenkin iso ongelma. Kuumakuivapuhdistuksessa pyritään kehittämään menetelmä, jossa syntyvät jätemäärät ovat pieniä ja puhdistustulos on riittävä. Puhdistuksen apukeinona käytetään usein erilaisia katalyyttejä. Tunnetuimpia ovat erilaiset kalsiumpohjaiset materiaalit ja mineraalit. Katalyyteillä voidaan tehostaa tarpeellisia kemiallisia reaktioita puhdistusprosessissa. Kaikki puhdistukseen liittyvät ongelmat ovat kooltaan niin suuria, että niiden ratkaisemiseksi on tulevaisuudessa tehtävä lujasti töitä. Markkinanäkymät toimivalle puhdistustekniikalle ovat nykymaailmassa hyvät. Niinpä tuotekehitykseen laitetut panokset voivat tulevaisuudessa olla yritykselle kullan arvoisia.

Kationinvaihtohartsien hapetuskestävyys

Hyvin puhdasta vettä vaativissa sovelluksissa käytettävät kationinvaihtohartsit eivät saisi vuotaa puhdistettavaan veteen mitään vieraita aineita. Todellisuudessa hartsit kuitenkin vuotavat hyvin pieniä määriä erilaisia yhdisteitä käytön aikana. Aineet, joita kationinvaihtohartsi päästää veteen, ovat osaksi hartsin polymerointireaktion aikana sen rungon sisään jääneitä yhdisteitä. Nämä voidaan suurimmaksi osaksi poistaa pesemällä hartsia. Osittain niitä syntyy myös hartsin polystyreenidivinyylibentseenirungon (PS-DVB) hapettuessa. Hapettumisen seurauksena syntyneet yhdisteet ovat pääosin orgaanisia sulfonaatteja. Tämä työ koskee ydinvoimalaitoksissa käytettäviä pulverihartseja, joita käytetään primääripiirissä kiertävän lauhdeveden puhdistukseen ja jotka joutuvat siellä alttiiksi hapettumiselle. Yleensä hapettuminen on hidasta ja se johtuu veteen liuenneesta hapesta. Hapettuminen nopeutuu huomattavasti, jos vedessä on läsnä hapettimia tai siirtymämetalli-ioneja. Tällaisia hapettimia ovat esimerkiksi vetyperoksidi, otsoni, vapaa kloori, typpihappo ja kromi. Vetyperoksidin vaikutuksesta hartsin runkoon muodostuu hydroperoksidiryhmä, jonka hajoamisesta alkaa reaktioiden sarja, joka lopulta johtaa hartsin polymeerirungon katkeamiseen. Siirtymämetalli-ionit katalysoivat peroksidien hajoamista. Tavallisimpia hapetusta katalysoivia metalli-ioneja ovat rauta ja kupari, joiden katalyyttinen aktiivisuus on suuri. Tässä työssä pyrittiin selvittämään, onko mahdollista valmistaa hartseja, jotka kestävät hapettumista paremmin kuin nykyisin käytössä olevat hartsit. Sen tutkimiseksi tehtiin kiihdytettyjä hapetuskokeita käyttäen hapettimena vetyperoksidia ilman siirtymämetalli-ioni katalyyttejä. Hapetuskokeet tehtiin kaupallisesti saatavilla hartseilla ja uusilla työtä varten syntetisoiduilla koehartseilla. Hapetuskokeiden etenemistä seurattiin mittaamalla veteen liuenneiden orgaanisten aineiden kokonaismäärää (TOC-analyysi) ja liuoksessa esiintyvien orgaanisten sulfonaattien määrää johtokykymittauksin. Saadut tulokset antoivat viitteitä siitä, että hartsin synteesiolosuhteilla voi olla suurempi vaikutus sen hapetuskestävyyteen kuin synteesissä käytetyillä raaka-aineilla.