Use of nanoparticles in Swiss industry: a targeted survey

A large number of applications using manufactured nanoparticles of less than 100 nm are currently being introduced into industrial processes. There is an urgent need to evaluate the risks of these novel particles to ensure their safe production, handling, use, and disposal. However, today we lack even rudimentary knowledge about type and quantity of industrially used manufactured nanoparticles and the level of exposure in Swiss industry. The goal of this study was to evaluate the use of nanoparticles, the currently implemented safety measures, and the number of potentially exposed workers in all types of industry. To evaluate this, a targeted telephone survey was conducted among health and safety representatives from 197 Swiss companies. The survey showed that nanoparticles are already used in many industrial sectors; not only in companies in the new field of nanotechnology, but also in more traditional sectors, such as paints. Forty-three companies declared to use or produce nanoparticles, and 11 imported and traded with prepackaged goods that contain nanoparticles. The following nanoparticles were found to be used in considerable quantities (> 1000 kg/year per company): Ag, Al-Ox, Fe-Ox, SiO2, TiO2, and ZnO. The median reported quantity of handled nanoparticles was 100 kg/year. The production of cosmetics, food, paints, powders, and the treatment of surfaces used the largest quantities of these nanoparticles. Generally, the safety measures were found to be higher in powder-based than in liquid-based applications. However, the respondents had many open questions about best practices, which points to the need for rapid development of guidelines and protection strategies

Juxtaposition of melt impregnation and high-temperature shear zones in the upper mantle; field and petrological constraints from the Lanzo peridotite (Northern Italy)

Results of a field and microstructural study between the northern and the central bodies of the Lanzo plagioclase peridotite massif (NW Italy) indicate that the spatial distribution of deformation is asymmetric across kilometre-scale mantle shear zones. The southwestern part of the shear zone (footwall) shows a gradually increasing degree of deformation from porphyroclastic peridotites to mylonite, whereas the northeastern part (hanging wall) quickly grades into weakly deformed peridotites. Discordant gabbroic and basaltic dykes are asymmetrically distributed and far more abundant in the footwall of the shear zone. The porphyroclastic peridotite displays porphyroclastic zones and domains of igneous crystallization whereas mylonites are characterized by elongated porphyroclasts, embedded between fine-grained, polycrystalline bands of olivine, plagioclase, clinopyroxene, orthopyroxene, spinel, rare titanian pargasite, and domains of recrystallized olivine. Two types of melt impregnation textures have been found: (1) clinopyroxene porphyroclasts incongruently reacted with migrating melt to form orthopyroxene plagioclase; (2) olivine porphyroclasts are partially replaced by interstitial orthopyroxene. The meltrock reaction textures tend to disappear in the mylonites, indicating that deformation in the mylonite continued under subsolidus conditions. The pyroxene chemistry is correlated with grain size. High-Al pyroxene cores indicate high temperatures (11001030C), whereas low-Al neoblasts display lower final equilibration temperatures (860C). The spinel Cr-number [molar Cr/(Cr Al)] and TiO2 concentrations show extreme variability covering almost the entire range known from abyssal peridotites. The spinel compositions of porphyroclastic peridotites from the central body are more variable than spinel from mylonite, mylonite with ultra-mylonite bands, and porphyroclastic rocks of the northern body. The spinel compositions probably indicate disequilibrium and would favour rapid cooling, and a faster exhumation of the central peridotite body, relative to the northern one. Our results indicate that melt migration and high-temperature deformation are juxtaposed both in time and space. Meltrock reaction may have caused grain-size reduction, which in turn led to localization of deformation. It is likely that melt-lubricated, actively deforming peridotites acted as melt focusing zones, with permeabilities higher than the surrounding, less deformed peridotites. Later, under subsolidus conditions, pinning in polycrystalline bands in the mylonites inhibited substantial grain growth and led to permanent weak zones in the upper mantle peridotite, with a permeability that is lower than in the weakly deformed peridotites. Such an inversion in permeability might explain why actively deforming, fine-grained peridotite mylonite acted as a permeability barrier and why ascending mafic melts might terminate and crystallize as gabbros along actively deforming shear zones. Melt-lubricated mantle shear zones provide a mechanism for explaining the discontinuous distribution of gabbros in oceancontinent transition zones, oceanic core complexes and ultraslow-spreading ridges.

Low environmental impact bleaching sequences for attaining high brightness level with eucalyptus SPP pulp

The alternatives used for minimizing the usage of chlorine dioxide in bleaching sequences included a hot acid hydrolysis (Ahot) stage, the use of hot chlorine dioxide (Dhot) and ozone stages at medium consistency and high consistency (Zmc and Zhc), in addition to stages with atmospheric hydrogen peroxide (P) and pressurized hydrogen peroxide (PO). The results were interpreted based on the cost of the chemical products, bleaching process yields and on minimizing the environmental impact of the bleaching process. In spite of some process restrictions, high ISO brightness levels were kept around 90 % brightness. Additionally, the inclusion of stages like acid hydrolysis, pressurized peroxide and ozone in the bleaching sequences provided an increase in operating flexibility, aimed at reducing environmental impact (ECF Light). The Dhot(EOP)D(PO) sequence presented lower operating cost for ISO brightness above 92 %. However, this kind of sequence was not allowed for closing the wastewater circuit, even partially. For ISO brightness level around 91%, the AhotZhcDP sequence presented a lower operating cost than the others

Authentication of vegetable oils by bulk and molecular carbon isotope analyses with emphasis on olive oil and pumpkin seed oil

The authenticity of vegetable oils consumed in Slovenia and Croatia was investigated by carbon isotope analysis of the individual fatty acids by the use of gas chromatography-combustion-isotope ratio mass spectrometry (GC/C/IRMS), and through carbon isotope analysis of the bulk oil. The fatty acids from samples of olive, pumpkin, sunflower, maize, rape, soybean, and sesame oils were separated by alkaline hydrolysis and derivatized to methyl esters for chemical characterization by capillary gas chromatography/mass spectrometry (GC/MS) prior to isotopic analysis. Enrichment in heavy carbon isotope (C-13) of th, bulk oil and of the individual fatty acids are related to (1) a thermally induced degradation during processing (deodorization, steam washing, or bleaching), (2) hydrolytic rancidity (lipolysis) and oxidative rancidity of the vegetable oils during storage, and (3) the potential blend with refined oil or other vegetable oils. The impurity or admixture of different oils may be assessed from the delta C-13(16:0) VS. delta C-13(18:1) covariations. The fatty acid compositions of Slovenian and Croatian olive oils are compared with those from the most important Mediterranean producer countries (Spain, Italy, Greece, and France).

Mechanisms of interaction of therapeutic nanoparticles with cells

Nanoparticles (NPs) have gained a lot of interest in recent years due to their huge potential for applications in industry and medicine. Their unique properties offer a large number of attractive possibilities in the biomedical field, providing innovative tools for diagnosis of diseases and for novel therapies. Nevertheless, a deep understanding of their interactions with living tissues and the knowledge about their possible effects in the human body are necessary for the safe use of nanoparticulate formulations. The aim of this PhD project was to study in detail the interactions of therapeutic NPs with living cells, including cellular uptake and release, cellular localization and transport across the cell layers. Moreover, the effects of NPs on the cellular metabolic processes were determined using adapted in vitro assays. We evaluated the biological effect of several NPs potentially used in the biomedical field, including titanium dioxide (Ti02) NPs, 2-sized fluorescent silica NPs, ultrasmall superparamagnetic iron oxide (USPIO) NPs, either uncoated or coated with oleic acid or with polyvinylamine (aminoPVA) and poly(lactic-co-glycolic acid) - polyethylene-oxide (PLGA-PEO) NPs. We have found that the NPs were internalized by the cells, depending on their size, chemical composition, surface coating and also depending on the cell line considered. The uptake of aminoPVA-coated USPIO NPs by endothelial cells was enhanced in the presence of an external magnetic field. None of the tested USPIO NPs and silica NPs was transported across confluent kidney cell layers or brain endothelial cell layers, even in the presence of a magnetic field. However, in an original endothelium-glioblastoma barrier model which was developed, uncoated USPIO NPs were directly transferred from endothelial cells to glioblastoma cells. Following uptake, Ti02 NPs and uncoated USPIO NPs were released by the kidney cells, but not by the endothelial cells. Furthermore, these NPs induced an oxidative stress and autophagy in brain endothelial cells, possibly associated with their enhanced agglomeration in cell medium. A significant DNA damage was found in brain endothelial cells after their exposure to TiO2NPs. Altogether these results extend the existing knowledge about the effects of NPs on living cells with regard to their physicochemical characteristics and provide interesting tools for further investigation. The development of the in vitro toxicological assays with a special consideration for risk evaluation aims to reduce the use of animal experiments. -Les nanoparticules (NPs) présentent beaucoup d'intérêt dans le domaine biomédical et industriel. Leurs propriétés uniques offrent un grand nombre de possibilités de solutions innovantes pour le diagnostique et la thérapie. Cependant, pour un usage sûr des NPs il est nécessaire d'acquérir une connaissance approfondie des mécanismes d'interactions des NPs avec les tissus vivants et de leur effets sur le corps humain. Le but de ce projet de thèse était d'étudier en détail les mécanismes d'interactions de NPs thérapeutiques avec des cellules vivantes, en particulier les mécanismes d'internalisation cellulaire et leur subséquente sécrétion par les cellules, leur localisation cellulaire, leur transport à travers des couches cellulaires, et l'évaluation des effets de NPs sur le métabolisme cellulaire, en adaptant les méthodes existante d'évaluation cyto-toxico logique s in vitro. Pour ces expériences, les effets biologiques de nanoparticules d'intérêt thérapeutique, telles que des NPs d'oxyde de titane (TiO2), des NPs fluorescents de silicate de 2 tailles différentes, des NPs, d'oxyde de fer super-para-magnétiques ultra-petites (USPIO), soit non- enrobées soit enrobées d'acide oléique ou de polyvinylamine (aminoPVA), et des NPs d'acide poly(lactique-co-glycolique)-polyethylene-oxide (PLGA-PEO) ont été évalués. Les résultats ont démontré que les NPs sont internalisées par les cellules en fonction de leur taille, composition chimique, enrobage de surface, et également du type de cellules utilisées. L'internalisation cellulaire des USPIO NPs a été augmentée en présence d'un aimant externe. Aucune des NPs de fer et de silicate n'a été transportée à travers des couches de cellules épithéliales du rein ou endothéliales du cerveau, même en présence d'un aimant. Cependant, en développant un modèle original de barrière endothélium-glioblastome, un transfert direct de NPs d'oxyde de fer de cellule endothéliale à cellule de glioblastome a été démontré. A la suite de leur internalisation les NPs d'oxyde de fer et de titane sont relâchées par des cellules épithéliales du rein, mais pas des cellules endothéliales du cerveau. Dans les cellules endothéliales du cerveau ces NPs induisent en fonction de leur état d'agglomération un stress oxydatif et des mécanismes d'autophagie, ainsi que des dommages à l'ADN des cellules exposées aux NPs d'oxyde de titane. En conclusion, les résultats obtenus élargissent les connaissances sur les effets exercés par des NPs sur des cellules vivantes et ont permis de développer les outils expérimentaux pour étudier ces effets in vitro, réduisant ainsi le recours à des expériences sur animaux.

Aqueous photocatalytic oxidation of steroid estrogens

Concerns have increased regarding the detection of endocrine-disrupting compounds in the effluents of sewage treatment plants (STPs). These compounds are able to disrupt normal function of the endocrine system of living organisms even at trace concentrations. Natural and synthetic steroid estrogens (SEs) are believed to be responsible for the majority of the endocrine-disrupting effects. Municipal sewage, the main source of SEs in the environment, is a complex mixture of a wide range of pollutants at concentrations much higher than those of SEs. Low concentrations of SEs in the presence of copollutants thus make their removal problematic. The main objectives of the present work were to study the potential of photocatalytic oxidation (PCO) to effectively treat SE-containing aqueous solutions and to identify the optimum conditions for such treatment. The results showed that SEs can be effectively degraded photocatalytically. Due to the adsorption properties of SEs on the TiO2 photocatalyst surface alkaline medium was found to be beneficial for SE oxidation despite the presence of co-pollutants in concentrations characteristic for the sanitary fraction of municipal sewage. The potential of PCO to selectively oxidise SEs was examined in the presence of copollutants of the sanitary fraction of sewage - urea, saccharose and human urine. The impact of ethanol, often used as a solvent in the preparation of SE stock solutions, was also studied and the results indicated the need to use organic solvent-free solutions for the study of SE behaviour. Photocatalytic oxidation of SEs appeared to be indifferent towards the presence of urea in concentrations commonly found in domestic sewage. The effect of other co-pollutants under consideration was far weaker than could be expected from their concentrations, which are from one hundred to a few thousands times higher than those of the SEs. Although higher concentrations can dramatically slow down the PCO of SEs, realistic concentrations of co-pollutants characteristic for the sanitary fraction of domestic sewage allowed selective removal of SEs. This indicates the potential of PCO to be a selective oxidation method for SE removal from the separate sanitary fraction of municipal sewage.

Combustibility of Paper Mill Rejects

Tämän työn tarkoituksena oli selvittää mekaanisen massan valmistuksen käsittävän paperitehtaan rejektija jätevirtojen poltettavuutta, jos paperitehtaan vesikiertojen sulkemisastetta lisätään. Jotta prosessin tilannetta sulkemisen jälkeen saatiin arvioitua, Anjalan paperitehtaan nykypäivän PK3:n prosessia tutkittiin kuorimolta jätevesilaitokselle. Kirjallisuusosassa käsiteltiin rejekti- ja jätevirtojen alkuperää mekaanista massaa käyttävässä paperitehtaassa. Myös tämän päivän jätevedenkäsittelyprosessit sekä sulkemisessa mahdolliset prosessiveden puhdistustekniikat esiteltiin lyhyesti. Lisäksikäytiin läpi nykypäivänä metsäteollisuudessa käytössä olevat polttotekniikat sekä polttoaineiden karakterisointi kattilan käytettävyyden ja päästöjen kannalta. Anjalan PK3:lla käytetään sekä peroksidi- että ditioniittivalkaistua tai pelkästään ditioniittivalkaistua hioketta riippuen tuotannossa olevasta lajista. PK3-prosessissa syntyneet jätevesi-, liete- ja muut jätevirrat selvitettiin molemmissa valkaisuolosuhteissa. Prosessin eniten liuennutta orgaanista ainesta sisältävät jätevesijakeet, 3-hiomon kuumankierron ja kirkassuodoksen ulosajot sekä kuoripuristimen suodos, valittiin puhdistettaviksi virroiksi prosessin sulkemista arvioitaessa. Kun peroksidivalkaisua käytettiin 3-hiomolla, TOC-kuorma jokeen oli 30 % suurempi kuin pelkällä ditioniittivalkaisulla. Jos prosessin sulkemisastetta lisättäisiin, TOC-kuorma olisi 30 %pienempi kuin tänäpäivänä peroksidivalkaisua käytettäessä (80 % puhdistustehokkuudella). Prosessin sulkemisastetta lisättäessä biolietettä muodostuisi n. 30 % vähemmän verrattuna nykytilanteeseen, sillä mikrobien ravintona käyttämää orgaanista ainesta päätyisi vähemmän jäteveteen. 3-hiomon peroksidivalkaisun vaikutus kattilan käytettävyyteen ja päästöihin oli pieni, sillä biolietteen osuus polttoaineen syötöstä oli vain 4 %. Vain osa biolietteestä muodostui 3-hiomolta peräisin olevaa orgaanista ainesta poistettaessa. Jos nykyisen pääpolttoaineen, PDF:n,osuuden jättää huomioimatta, SO2- ja NOx-päästöt sekä leijupedin sintrautuvuus ovat hiukan suuremmat käytettäessä peroksidivalkaisua 3-hiomolla kuin pelkästään ditioniittivalkaisulla. Jos kuoripuristimen ja hiomon suodosten puhdistuksen konsentraatit johdetaan poltettaviksi BFB-tyyppiseen kattilaan, leijupedin sintrautuminen tulisi olemaan suurin ongelma. Myös raskasmetalli-, SO2- ja NOx-päästöt lisääntyisivät merkittävästi verrattuna nykyiseen tilanteeseen. Sen sijaan kattilan korroosioriski tuskin lisääntyisi. Lisäksi konsentraattien kosteuspitoisuus olisi korkea, mikä tekisi poltosta kannattamatonta veden haihdutuksen vaatiessa paljon energiaa. Yksityiskohtaisempaa tutkimusta tarvitaan vielä prosessin sulkemisen vaikutuksista päästöihin ja kattilan käytettävyyteen. Myös muita konsentraattien hävittämismahdollisuuksia tulisi tutkia lisää.

The Influence of Process Conditions on the Deresination Efficiency in Mechanical Pulp Washing

The aim of this thesis was to produce information for the estimation of the flow balance of wood resin in mechanical pulping and to demonstrate the possibilities for improving the efficiency of deresination in practice. It was observed that chemical changes in wood resin take place only during peroxide bleaching, a significant amount of water dispersed wood resin is retained in the pulp mat during dewatering and the amount of wood resin in the solid phase of the process filtrates is very small. On the basis of this information there exist three parameters related to behaviour of wood resin that determine the flow balance in the process: 1. The liberation of wood resin to the pulp water phase 2. Theretention of water dispersed wood resin in dewatering 3. The proportion of wood resin degraded in the peroxide bleaching The effect of different factors on these parameters was evaluated with the help of laboratory studies and a literature survey. Also, information related to the values of these parameters in existing processes was obtained in mill measurements. With the help of this information, it was possible to evaluate the deresination efficiency and the effect of different factors on this efficiency in a pulping plant that produced low-freeness mechanical pulp. This evaluation showed that the wood resin content of mechanical pulp can be significantly decreased if there exists, in the process, a peroxide bleaching and subsequent washing stage. In the case of an optimal process configuration, as high as a 85 percent deresination efficiency seems to be possible with a water usage level of 8 m3/o.d.t.

Practical applications of a systematic approach to the chemical abatement of pollutants in water and air

The present dissertation is devoted to the systematic approach to the development of organic toxic and refractory pollutants abatement by chemical decomposition methods in aqueous and gaseous phases. The systematic approach outlines the basic scenario of chemical decomposition process applications with a step-by-step approximation to the most effective result with a predictable outcome for the full-scale application, confirmed by successful experience. The strategy includes the following steps: chemistry studies, reaction kinetic studies in interaction with the mass transfer processes under conditions of different control parameters, contact equipment design and studies, mathematical description of the process for its modelling and simulation, processes integration into treatment technology and its optimisation, and the treatment plant design. The main idea of the systematic approach for oxidation process introduction consists of a search for the most effective combination between the chemical reaction and the treatment device, in which the reaction is supposed to take place. Under this strategy,a knowledge of the reaction pathways, its products, stoichiometry and kinetics is fundamental and, unfortunately, often unavailable from the preliminary knowledge. Therefore, research made in chemistry on novel treatment methods, comprisesnowadays a substantial part of the efforts. Chemical decomposition methods in the aqueous phase include oxidation by ozonation, ozone-associated methods (O3/H2O2, O3/UV, O3/TiO2), Fenton reagent (H2O2/Fe2+/3+) and photocatalytic oxidation (PCO). In the gaseous phase, PCO and catalytic hydrolysis over zero valent ironsare developed. The experimental studies within the described methodology involve aqueous phase oxidation of natural organic matter (NOM) of potable water, phenolic and aromatic amino compounds, ethylene glycol and its derivatives as de-icing agents, and oxygenated motor fuel additives ¿ methyl tert-butyl ether (MTBE) ¿ in leachates and polluted groundwater. Gas-phase chemical decomposition includes PCO of volatile organic compounds and dechlorination of chlorinated methane derivatives. The results of the research summarised here are presented in fifteenattachments (publications and papers submitted for publication and under preparation).

Studies on the characterization of dental whitening process by using both hyperspectral imaging and colorimeter techniques

A beautiful smile is directly related with white teeth. Nowadays oral care has increased and developed processes for beautiful smiles. Dental bleaching is frequently used in odontology, not just for health care also for aesthetic treatment. With the possibility of teeth bleaching, now the importance is in, how white the tooth is? Because color is relate to an individual perception. In order to assets teeth correct color identification has been developed many color guides, models, spaces and analytical methods. Spite all of these useful tools the color interpretation depends on environmental factors, position of the sample in the data acquisition and most importantly the instrument sensitivity. The commons methods have proved to be useful. They are easy to handle, some are portable but they do not have a high sensitivity. The present work is based on the integration of a new analytical technique for color acquisition. High spectral Image (HSI) is able to performed image analysis with high quality and efficiency. HSI is used in many fields and we used it for color image analysis within the bleaching process. The main comparison was done with the HSI and the colorimeter through the processes of two different bleaching protocols. The results showed that HSI has higher sensitivity than the colorimeter. During the analysis the dental surface with the HSI we were able to notice surface changes. These changes were analyzed by roughness studies.

Toxicity screenings of nanomaterials: challenges due to interference with assay processes and components of classic in vitro tests.

Given the multiplicity of nanoparticles (NPs), there is a requirement to develop screening strategies to evaluate their toxicity. Within the EU-funded FP7 NanoTEST project, a panel of medically relevant NPs has been used to develop alternative testing strategies of NPs used in medical diagnostics. As conventional toxicity tests cannot necessarily be directly applied to NPs in the same manner as for soluble chemicals and drugs, we determined the extent of interference of NPs with each assay process and components. In this study, we fully characterized the panel of NP suspensions used in this project (poly(lactic-co-glycolic acid)-polyethylene oxide [PLGA-PEO], TiO2, SiO2, and uncoated and oleic-acid coated Fe3O4) and showed that many NP characteristics (composition, size, coatings, and agglomeration) interfere with a range of in vitro cytotoxicity assays (WST-1, MTT, lactate dehydrogenase, neutral red, propidium iodide, (3)H-thymidine incorporation, and cell counting), pro-inflammatory response evaluation (ELISA for GM-CSF, IL-6, and IL-8), and oxidative stress detection (monoBromoBimane, dichlorofluorescein, and NO assays). Interferences were assay specific as well as NP specific. We propose how to integrate and avoid interference with testing systems as a first step of a screening strategy for biomedical NPs.

PHOTOCATALYTIC OXIDATION OF AQUEOUS SOLUTIONS OF JET FUEL AND ICING INHIBITORS

The present paper is devoted to the results of experimental research undertaken into photocatalytical oxidation (PCO) of aqueous solutions of de-icing agents and aqueous extract of jet fuel. The report consists of introduction, literature review, description of materials and methods, discussion of results and conclusions. TiO2 was selected as a photocatalyst for the experiments with synthetic solutions of ethylene glycol, 2-ethoxyethanol and aqueous extract of jet fuel. To explain the PCO mechanisms affecting certain behaviour of de-icing agent under distinctive conditions, the following factors were studied: the impact of initial concentration of pollutant, the role of pH, the presence of tert-butanol as OH·-radicals scavenger and mineral admixtures. PCO under solar radiation performed in two ways: catalysed by irradiated TiO2 slurry or by TiO2 attached to buoyant hollow glass micro-spheres. Special attention was paid to the energy-saving PCO with reduced intensity mixing of the slurry. The effect of PCO was assessed by determination of residual chemical oxygen demand of solution (COD) and by measuring of concentration of glycols. The PCO process efficiency was assumed to be dependent on the TiO2 suspension fractional composition. Thus, the following effects of solutions’ media were viewed: presence of organic admixtures, pH influence, mixing mode during the PCO. The effects of mineral admixtures - Ca2+, Fe3+/2+, Mn2+, SO42- - that are often present in natural and wastewater systems or produced during the degradation of organic pollutants and which can affect the rate of PCO of de-icing agents, were also investigated.

Cost efficient extractive removal of birch pulp

Tämän diplomityön tarkoituksena oli selvittää kustannustehokkaita keinoja uuteaineiden vähentämiseksi koivusulfaattimassasta. Uuteaineet voivat aiheuttaa ongelmia muodostaessaan saostumia prosessilaitteisiin. Saostumat aiheuttavat tukkeumia ja mittaushäiriöitä, mutta irrotessaan ne myös huonontavat sellun laatua. Lopputuotteeseen joutuessaan ne voivat lisäksi aiheuttaa haju- ja makuhaittoja, joilla on erityistä merkitystä esimerkiksi valmistettaessa elintarvikekartonkeja. Tämä työ tehtiin Stora Enson sellutehtaalla, Enocell Oy:llä, Uimaharjussa. Teoriaosassa käsiteltiin uuteaineiden koostumusta ja niiden aiheuttamia ongelmia sellu– ja paperitehtaissa. Lisäksi koottiin aikaisempien tehdaskokeiden fysikaalisia ja kemiallisia keinoja vähentää koivu-uutetta. Tarkastelualueina olivat puunkäsittely, keitto, pesemö ja valkaisu. Kokeellisessa osassa suoritettiin esikokeita laboratorio- ja tehdasmittakaavassa, jotta saavutettaisiin käytännöllistä tietoa itse lopuksi tehtävää tehdasmittakaavan koetta varten. Laboratoriokokeissa tutkittiin mm. keiton kappaluvun, lisäaineiden ja hartsisaippuan vaikutusta koivu-uutteeseen. Lisäksi suoritettiin myös happo- (A) ja peretikkahappovaiheen (Paa) laboratoriokokeet. Tehdasmittakaavassa tarkasteltiin mm. keiton kappaluvun, pesemön lämpötilan, A-vaiheen, valkaisun peroksidi- ja Paa-vaiheen vaikutusta koivu-uutteeseen. Uutteenpoistotehokkuutta eri menetelmien välillä vertailtiin niin määrällisesti kuin rahallisesti. Uutteenpoistotehokkuudella mitattuna vertailuvaihe oli tehokkain pesemön loppuvaiheessa ja valkaisun alkuvaiheessa. Pesemön loppuvaiheessa uutteenpoistoreduktiot olivat noin 30 % ja valkaisun alkuvaiheessa 40 %. Peroksidivaihe oli tehokkain käytettynä valkaisun loppuvaiheessa noin 40 % reduktiolla. Kustannustehokkuudella mitattuna tehokkaimmaksi osoittautui A-vaihe yhdessä peroksidivaiheen kanssa. Säästöt vertailujaksoon verrattuna olivat noin 0.3 €/ADt. Lisäksi kyseinen yhdistelmä osoittautui hyväksi keinoksi säilyttää uutetaso alle maksimirajan kuitulinja 2:lla, kun kuitulinjalla 1 tuotettiin samanaikaisesti armeeraussellua.

Removal of Lipophilic Wood Extractives from TMP Process Waters by Wet Oxidation

Työssä tutkittiin kokeellisesti rasvaliukoisten uuteaineiden poistamista TMP -prosessin vesikierroista märkähapetuksen avulla. Työn tavoitteena oli tutkia mahdollisuudet hyödyntää TMP -prosessissa vallitsevaa korkeaa lämpötilaa rasvaliukoisten uuteaineiden poistamiseen hapettamalla niitä puhtaalla hapella. Kirjallisuusosassa tarkasteltiin märkähapetuksen teknologiaa, reaktiomekanismia, käytettyjä katalyyttejä, käyttökohteita sekä kustannuksia. Kokeita suoritettiin autoklaavireaktorissa lämpötiloissa 140 °C, 160 °C ja 180 °C. Vetyperoksidia käytettiin katalyyttinä lisätyn vetyperoksidin määrän ollessa 100 - 1800 mg/l ja hapen osapaineen ollessa 0 ( typpiatmosfääri) - 15 baria. Kokeissa tarkasteltiin kemiallisen hapenkulutuksen (COD), rasvaliukoisten uuteaineiden konsentraation, orgaanisen kokonaishiilen (TOC) ja värin muutoksia kokeiden aikana eri lämpötiloilla, hapen osapaineilla ja lisätyn vetyperoksidin määrillä. Kokeissa saavutettiin 30 %:n COD:n vähenemä sekä 90 %:n vähenemä rasvaliukoisissa uuteaineissa lämpötiloissa 160 °C ja 180 °C. Lisäämällä vetyperoksidia katalyyttinä saavutettiin lähes sama tulos lämpötilassa 140 °C. Suurin tässä työssä havaittu ongelma oli lisääntynyt värinmuodostus vedessä olevassa hienojakoisessa kiintoaineessa hapetuksen aikana. Tämän vuoksi lisätutkimukset ovat tarpeellisia sen seikan selvittämiseksi, voidaanko muodostunut väri mahdollisesti poistaa massan valkaisussa.

Gas-phase photocatalytic oxidation of volatile organic compounds

Substances emitted into the atmosphere by human activities in urban and industrial areas cause environmental problems such as air quality degradation, respiratory diseases, climate change, global warming, and stratospheric ozone depletion. Volatile organic compounds (VOCs) are major air pollutants, emitted largely by industry, transportation and households. Many VOCs are toxic, and some are considered to be carcinogenic, mutagenic, or teratogenic. A wide spectrum of VOCs is readily oxidized photocatalytically. Photocatalytic oxidation (PCO) over titanium dioxide may present a potential alternative to air treatment strategies currently in use, such as adsorption and thermal treatment, due to its advantageous activity under ambient conditions, although higher but still mild temperatures may also be applied. The objective of the present research was to disclose routes of chemical reactions, estimate the kinetics and the sensitivity of gas-phase PCO to reaction conditions in respect of air pollutants containing heteroatoms in their molecules. Deactivation of the photocatalyst and restoration of its activity was also taken under consideration to assess the practical possibility of the application of PCO to the treatment of air polluted with VOCs. UV-irradiated titanium dioxide was selected as a photocatalyst for its chemical inertness, non-toxic character and low cost. In the present work Degussa P25 TiO2 photocatalyst was mostly used. In transient studies platinized TiO2 was also studied. The experimental research into PCO of following VOCs was undertaken: - methyl tert-butyl ether (MTBE) as the basic oxygenated motor fuel additive and, thus, a major non-biodegradable pollutant of groundwater; - tert-butyl alcohol (TBA) as the primary product of MTBE hydrolysis and PCO; - ethyl mercaptan (ethanethiol) as one of the reduced sulphur pungent air pollutants in the pulp-and-paper industry; - methylamine (MA) and dimethylamine (DMA) as the amino compounds often emitted by various industries. The PCO of VOCs was studied using a continuous-flow mode. The PCO of MTBE and TBA was also studied by transient mode, in which carbon dioxide, water, and acetone were identified as the main gas-phase products. The volatile products of thermal catalytic oxidation (TCO) of MTBE included 2-methyl-1-propene (2-MP), carbon monoxide, carbon dioxide and water; TBA decomposed to 2-MP and water. Continuous PCO of 4 TBA proceeded faster in humid air than dry air. MTBE oxidation, however, was less sensitive to humidity. The TiO2 catalyst was stable during continuous PCO of MTBE and TBA above 373 K, but gradually lost activity below 373 K; the catalyst could be regenerated by UV irradiation in the absence of gas-phase VOCs. Sulphur dioxide, carbon monoxide, carbon dioxide and water were identified as ultimate products of PCO of ethanethiol. Acetic acid was identified as a photocatalytic oxidation by-product. The limits of ethanethiol concentration and temperature, at which the reactor performance was stable for indefinite time, were established. The apparent reaction kinetics appeared to be independent of the reaction temperature within the studied limits, 373 to 453 K. The catalyst was completely and irreversibly deactivated with ethanethiol TCO. Volatile PCO products of MA included ammonia, nitrogen dioxide, nitrous oxide, carbon dioxide and water. Formamide was observed among DMA PCO products together with others similar to the ones of MA. TCO for both substances resulted in the formation of ammonia, hydrogen cyanide, carbon monoxide, carbon dioxide and water. No deactivation of the photocatalyst during the multiple long-run experiments was observed at the concentrations and temperatures used in the study. PCO of MA was also studied in the aqueous phase. Maximum efficiency was achieved in an alkaline media, where MA exhibited high fugitivity. Two mechanisms of aqueous PCO – decomposition to formate and ammonia, and oxidation of organic nitrogen directly to nitrite - lead ultimately to carbon dioxide, water, ammonia and nitrate: formate and nitrite were observed as intermediates. A part of the ammonia formed in the reaction was oxidized to nitrite and nitrate. This finding helped in better understanding of the gasphase PCO pathways. The PCO kinetic data for VOCs fitted well to the monomolecular Langmuir- Hinshelwood (L-H) model, whereas TCO kinetic behaviour matched the first order process for volatile amines and the L-H model for others. It should be noted that both LH and the first order equations were only the data fit, not the real description of the reaction kinetics. The dependence of the kinetic constants on temperature was established in the form of an Arrhenius equation.