Odor emission control and reduce in betaine manufacture

This thesis was made in Naantali plant of Finnfeeds Finland Oy. In this thesis the main study was in reducing, controlling, measuring and processing odour effluents in various methods. Also are considered legislation, marketing issues and environmental requirements of reducing of odour effluents. The literature review introduces odours complications, legislations and various methods of odour removal. There is also a review of volatile organic compounds detection and measuring methods. The experimental section consists TD-GC-MS-measurements and expansive measurements with electronic nose. Electronic nose is a new solution for recognition and measuring industrial odours. In this thesis the electronic nose was adapted into reliable recognition and measuring method. Measurements with electronic nose was made in betaine factory and main targets were odour removal process and other odours from factory. As a result of experimental work with TD-GC-MS-measurements becomes odour compound of 2-and 3- methylbutanal and dimethyldisulfide, which odour is sweet and fug. Extensive study with electronic nose found many developmental subjects. Odour balance measurements of factory and after calculation made adjustment of odour removal process, over all odour effluent to environment will reduce 25 %.

Improvement of pyrolysis oil quality by scrubbing

Diplomityössä tutkittiin kuuman pyrolyysihöyryn puhdistamista haisevista ja kevyistä haihtuvista yhdisteistä. Työn kirjallisuusosassa selvitettiin pyrolyysiöljyn kannattavuutta uusiutuvana energialähteenä. Lisäksi eri pesurityyppejä tarkasteltiin ja ja vertailtiin. Työn kokeellisessa osassa käytettiin kahta erilaista koelaitteistoa. Tuotteen talteenotossa vertailtiin reaktorilämpötilan ja raaka-aineen kosteuden vaikutusta pyrolyysisaantoihin. Komponenttien talteenotossa tutkittiin epästabiilien ja pistävän hajuisten yhdisteiden poistamista kuumasta pyrolyysihöyrystä. Raaka-aineena käytettiin kuusen metsätäh-dehaketta, joka sisältää runsaasti neulasia ja kaarnaa. Kokeet toteutettiin lämpötila-alueella 460 - 520 °C. Koelaitteistot koostuivat kaasun (N2) syöttöjärjestelmään kytketystä kuumasta ja kyl-mästä puolesta. Tuotteen talteenotossa kuuma pyrolyysihöyry jäähdytettiin ja otettiin talteen. Komponenttien talteenotossa tuote kerättiin suodattimelle ja metyleeniklo-ridiloukkuun. Tuotteiden koostumukset analysoitiin kaasukromatokrafilla. Korkeimmat orgaaniset saannot saatiin 480 °C reaktorilämpötilalla ja 8-9 p-% raaka-ainekosteudella. Pyrolyysiveden määrä putosi raaka-aineen kosteutta nostettaessa. Eri reaktorilämpötiloilla ja raaka-ainekosteuksilla ei ollut vaikutusta hiiltosaantoihin. Kaasusaannot (pääosin CO2, CO ja hiilivedyt) olivat noin 10 p-%. Komponenttien talteenotossa suodatin tukkeutui matalissa (< 250 °C) lämpötiloissa. Suodattimelle jäänyt materiaali oli pääosin neulasista ja kaarnasta peräisin olevia uuteaineita (pääosin hartsi- rasvahappoja) ja sokereita. Korkeimmissa lämpötiloissa (> 250 °C) uuteaineet läpäisivät suodattimen paremmin. 250 ja 300 °C:n lämpötiloissa suuri määrä lyhytketjuisia helposti haihtuvia epästabiileja ja haisevia yhdisteitä (ketoneja, furaani- ja furfuraalijohdannaisia jne.) jäi metyleenikloridi- ja metanoliloukkuihin.

The fog of cyber defence

The Fog of Cyber Defence is a book about cyberspace, cyber security and cyberwar. The book is untangling the ties of the Nordic states with the important, yet complex and foggy phenomenon of cyber. It is adding important perspectives into the ongoing discussion about cyber security and creating room for the deepening of co-operation amongst the Nordic states. The articles in the book contribute to the debate over the implications of cyber for national security and the armed forces. The authors, who come from various professional backgrounds, appreciate and welcome further discussion and comments on the very important themes that impact our everyday lives.

Kosteuden ja neliömassan mittaaminen kartonkikoneen viiraosalla

Diplomityön tavoitteena oli selvittää spraytärkkelyksen ja eri kerrosten liitossakeuksien vaikutusta kartongin palstautumislujuuteen ja formaatioon. Työn teon aikana viiraosille hankittiin gammasäteilyllä toimivat kosteusmittarit. Työssä haettiin keinoja varmentaa mit-tausten luotettavuus kartonkikoneella, jonka nopeudet ja tuotteiden neliömassat vaihtelevat suuresti. Työn loppuvaiheessa aloitettiin mittareiden toiminnan parantaminen. Spraytärk-kelyksen annostelua parannettiin ja annostelulle rakennettiin suhdesäätö. Tärkkisumun aiheuttamia haittoja vähennettiin lisäämällä spraytärkkelysputkien yhteyteen tärkkelys-tippoja poistavia imupalkkeja. Tämän diplomityön kirjallisuusosan tavoitteena oli tarkastella taivekartonkia tuotteena ja sen kilpailukyvyn kannalta tärkeitä ominaisuuksia. Kilpailukyvyn kannalta tärkeään palstautumislujuuteen sekä taivutusjäykkyyteen kiinnitettiin huomiota niiden toisistaan riippuvuuksien vuoksi. Spraytärkkelyksen käyttö riittävän palstautumislujuuden varmistajana ja spraytärkkelyksen määrän hallinta olivat kirjallisuusosassa mukana. Liitossakeuksien hallinta gammasäteilyä hyödyntävien NDC-mittareiden avulla oli toinenpääalue. Kirjallisuusosassa on viitattu myös tehtaalta saatuihin kokemusperäisiin tietoihin. Tämän työn kokeellisessa osassa selvitettiin InkeroistenKartonkitehtaan Kartonkikone 4:a. ja sillä suoritettuja spraytärkkelyskokeita. Liitoskosteuksia selvitettiin pääosin aiempien mittausten ja kokemusten perusteella.

Epäpuhtaudet sinkin uutossa

Työssä tutkittiin metalli- ja anioniepäpuhtauksien myötäuuttautumista sinkin mukana di(2-etyyliheksyyli)fosforihappoalla (D2EHPA). Laboratoriokokeissa selvitettiin pH:n vaikutusta metalliepäpuhtauksien uuttautumiseen pH-alueella -O, l... 3 sekä pesujen vaikutusta sinkillä ladatun orgaanisen faasin metallipitoisuuksiin. Kokeita tehtiin sekä synteettisillä että autenttisilla prosessiliuoksilla. Anionikokeissa tutkittiin raudan ja sinkin vaikutusta kloridin ja fluoridin uuttautumiseen. Synteettisillä liuoksilla tehdyissä kokeissa tutkittiin kadmiumin, koboltin, nikkelin, kuparin sekä antimonin uuttautumista sinkkisulfaattiliuoksesta. Kokeissa havaittiin D2EHPA:n uuttavan sinkkiä selvästi em. metalleja paremmin. Sinkki uuttautui sulfaattiliuoksesta lähes täydellisesti tasapaino-pH:n ollessa yli 2,3. Sinkin jälkeen muista metalleista uuttautui eniten kadmium ja järjestyksessä sitten kupari, koboltti ja nikkeli. Epäpuhtausmetallien myötäuuttautumista lisääntyi uuton tasapaino-pH:n kasvaessa ja väheni sinkkilatauksen kasvaessa. Kahdella peräkkäisellä pesuaskeleella, joissa ensimmäinen pesuliuos sisälsi 5 g/L rikkihappoa ja toinen sekä 15 g/L rikkihappoa että 5 g/L sinkkiä saatiin kaikkien epäpuhtausmetallien pitoisuudet jäämään alle 3 mg/L. Antimonin uuttokokeissa huomattiin antimonin uuttautuvan täydellisesti D2EHPA:lla pH:sta riippumatta pH-alueella0...3. Prosessiliuoksilla tehdyissä kokeissa todettiin D2EHPA:n pystyvän tehokkaasti erottamaan sinkin magnesiumista ßzn,Mg ˜107 ja kadmiumista ßzn,cd ˜106. Havaittiin myös, että mitä suurempi sinkki- ja rautalataus orgaanisessa faasissa on sitä vähemmän magnesiumia ja kadmiumia uuttautuu. Ensimmäisessä pesussa saatiin sekä kadmiumin että magnesiumin pitoisuudet putoamaan keskimäärin 0,1 mg/L eli 30 alkuperäisestä pitoisuudesta. Toisella pesuaskeleella ei enää ollut vaikutusta kadmiumin ja magnesiumin pitoisuuksiin orgaanisessa faasissa. Kokeissa havaittiin myös, että D2EHPA:n latausasteen ylittäessä 0,7 alkaa sinkki-D2EHPA-kompleksit polymeroitua ja faasit eivät enää selkeytyneet helposti. Anionikokeissa huomattiin, ettei D2EHPA uuttanut kloridi tai fluoridi sinkin tai raudan mukana. D2EHPA:n havaittiin myös itsessään sisältävän hieman kloridia.

Aluminium fouling and its impact on activated carbon based dioxin and furan removal in a wet scrubber at a co-incineration plant

Dioxins and furans, PCDD/Fs, are highly toxic substances formed in post combustion zones in furnaces. PCDD/F emissions are regulated by a waste incineration directive which relates also to co-incineration plants. Several observations of dioxin and furan enhancements in wet scrub- bers have been reported previously. This is thought to be due to the so-called "memory effect" which occurs when dioxins and furans absorb into plastic material in scrubbers and desorb when ambient circumstances alter significantly. At the co-incineration plant involved, dioxins and furans are controlled with a wet scrubber, the tower packing of which is made of plastic in which activated carbon particles are dispersed. This should avoid the memory effect and act as a dioxin and furan sink since dioxins and furans are absorbed irreversibly into the packing ma- terial. In this case, the tower packing in the scrubber is covered with a white layer that has been found to be mainly aluminium. The aim of this thesis was to determine the aluminium balance and the dioxin and furan behaviour in the scrubber and, thus, the impacts that the foul- ing has on dioxin and furan removal. The source of aluminium, reasons for fouling and further actions to minimize its impacts on dioxin and furan removal were also to be discovered. Measurements in various media around the scrubber and in fuels were made and a profile analysis of PCDD/F and mass balance calculations were carried out. PCDD/F content de- creased in the scrubber. The reduced PCDD/F was not discharged into scrubbing water. The removal mechanism seems to work in spite of the fouling, at least with low PCDD/F loads. Most of the PCDD/F in excess water originates from the Kymijoki River which is used as feeding water in the scrubber. Fouling turned out to consist mainly of aluminium hydroxides. Sludge combusted in the furnace was found to be a significant source of aluminium. Ways to minimize the fouling would be adjustment of pH to a proper lever, installation of a mechanical filter to catch the loose material from the scrubbing water and affecting the aluminium content of the sludge.

Langattoman tietoliikenneverkon toteuttaminen satama-alueelle

Tässä työssä toteutetaan IEEE 802.16-2004 standardiin perustuva langaton WiMAX tietoliikenneverkko, sekä tutkitaan etenemismallien soveltuvuutta satama-alueelle. Myös muiden verkkoratkaisujen soveltuvuutta pohditaan. Lisäksi tutkitaan sääolosuhteiden sekä päätelaitteen liikkumisnopeuden vaikutuksia yhteyteen. Satama-alueella on teräksestä valmistettuja merikontteja pinottuina päällekkäin, ja ne vaikeuttavat langattomien signaalien etenemistä. Merikonttien pinot säilyttävät tietyn maksimikorkeuden johtuen työkoneiden rajallisesta kyvystä pinota niitä. Langattomien signaalien etenemiselle erilaisissa ympäristöissä on kehitetty etenemismalleja. Etenemisallien avulla voidaan pyrkiä ennustamaan signaalin vahvuutta eri etäisyyksillä tukiasemasta. Etenemismallit kuvaavat ympäristön aiheuttamaa signaalin vaimenemista erilaisten muuttujien avulla. Langattoman tietoliikenneverkon toteutus ongelmatilanteineen dokumentoitiin ja alueella tehtiin kuuluvuusmittauksia. Löydettiin etenemismalli ja muuttujat, joiden avulla lasketut tulokset vastasivat mitattuja tuloksia hyvin. Myös sääolosuhteiden sekä päätelaitteen liikkumisnopeuden vaikutusta signaalin vahvuuteen tutkittiin. Vesi- ja lumisateen sekä sumun vaikutuksen todettiin olevan merkityksetön verkon käyttämällä 3.5 GHz taajuusalueella. Myöskään päätelaitteen liikkumisnopeuden ei todettu vaikuttavan toiminnallisuuteen 20-30 kilometrin tuntinopeudella, jolla työkoneet alueella liikkuvat.

Epäpuhtausmetallien talteenotto sinkkiprosessissa

There are small amounts of valuable metals, such as indium, gallium and germanium, in zinc process solutions. Their solvent extraction was studied in this work in sulphate solutions containing zinc and other metals present in industrial solutions. It was discovered, that a commercial bis(2-ethylhexyl)phosphate (D2EHPA) extractant can be used to extract indium and gallium. Indium was extracted separately at a higher acid concentration than gallium. Zinc was co-extracted faster than gallium and almost as much as gallium at the same pH. However, the scrubbing of zinc was possible using a dilute sulphuric acid and a short contact time while gallium losses were small. Both indium and gallium were stripped with sulphuric acid. Germanium was extracted with 5,8-diethyl-7-hydroxydodecane-6-oxime with the commercial name of LIX 63. Unlike other metals in the solution the extraction of germanium increased with different extractants as the acidity increased. Germanium extraction isotherm was measured for a 125 g/L sulfuric acid solution. The loaded organic phase was washed with pure water. It removed the co-extracted acid and part of the germanium and extracted impurities such as iron and copper. Germanium was stripped using a NaOH solution. A process model utilizing own experimentally determined extraction, scrubbing and stripping isotherms was made with HSC Sim software developed by Outotec Oyj. The model based on McCabe–Thiele diagrams was used in sizing the necessary amount of stages and phase ratios in a recovery process. It was concluded, that indium, gallium and germanium can be recovered in the process from a feed where their concentrations are low (<300 ppm). In an example case the feed contained also more than 20 g/L zinc and 2–8 g/L iron, aluminium and copper. The recoveries of indium, gallium and germanium were more than 90 % when 1–3 stages were used in each extraction, scrubbing and stripping section. Since the number of stages is small mixer-settlers would be well suited for this purpose.

Travelling in a Palimpsest : Finnish nineteenth-century painters' encounters with Spanish art and culture

Utgångspunkten för avhandlingen är finländska konstnärsresor till Spanien under 1800-talet, och kontakterna med spansk konst och kultur. Endast ett fåtal finländare reste till Spanien, och inledningsvis utrycktes intresset för spansk konst i form av kopior efter gamla mästare, utförda både efter original utanför Spanien, och reproduktioner. Denna föga imponerande start efterföljdes av ett litet antal målare som verkligen reste till Spanien under 1800-talets senare hälft: Adolf von Becker (1831–1909), Albert Edelfelt (1854–1905) och Venny Soldan (1863–1945). Jag undersöker hur deras syn på landet manifesterades i deras resebilder i förhållande till den växande turistindustrin. Syftet med avhandlingen är att visa hur den resande målaren, likt en turist, föreställde sig, upplevde och tolkade den främmande kulturen, och hur detta avbildades och uttrycktes i deras resebilder. Vid sidan av ikonografisk analys och stilkritik utnyttjas forskningsmetoder från turismteorin. Resultatet av undersökningen visar att de flesta konstnärerna dyrkade konsten på Prado-museet, beundrade flamenco, Andalusiens vackra kvinnor, tjurfäktningar och zigenarna. De längtade efter en förgången och exotisk tid, samtidigt som de följde de vältrampade turiststigarna och hänfördes av de sedvanliga sevärdheterna; de reste i ett delvis mytiskt och delvis verkligt land. Likt turister (i allmänhet), såg de det de ville se, och sökte sig till på förhand inpräntade mentala (före)bilder. Resebilderna kan med fog tolkas som medvetet konstruerade minnen från resan, souvenirs d’Espagne. Samtidigt förstärkte och upprätthöll valen av motiv uppfattningen att Spaniens äldre konst och samtida kultur var mer ”äkta” (autentiska) än den kultur man själv tillhörde. Spanien uppfattades som en kvarleva från en förgången tid som hölls levande i nuet

Recovery and refining of manganese as by-product from hydrometallurgical processes

The consumption of manganese is increasing, but huge amounts of manganese still end up in waste in hydrometallurgical processes. The recovery of manganese from multi-metal solutions at low concentrations may not be economical. In addition, poor iron control typically prevents the production of high purity manganese. Separation of iron from manganese can be done with chemical precipitation or solvent extraction methods. Combined carbonate precipitation with air oxidation is a feasible method to separate iron and manganese due to the fast kinetics, good controllability and economical reagents. In addition the leaching of manganese carbonate is easier and less acid consuming than that of hydroxide or sulfide precipitates. Selective iron removal with great efficiency from MnSO4 solution is achieved by combined oxygen or air oxidation and CaCO3 precipitation at pH > 5.8 and at a redox potential of > 200 mV. In order to avoid gypsum formation, soda ash should be used instead of limestone. In such case, however, extra attention needs to be paid on the reagents mole ratios in order to avoid manganese coprecipitation. After iron removal, pure MnSO4 solution was obtained by solvent extraction using organophosphorus reagents, di-(2-ethylhexyl)phosphoric acid (D2EHPA) and bis(2,4,4- trimethylpentyl)phosphinic acid (CYANEX 272). The Mn/Ca and Mn/Mg selectivities can be increased by decreasing the temperature from the commonly used temperatures (40 –60oC) to 5oC. The extraction order of D2EHPA (Ca before Mn) at low temperature remains unchanged but the lowering of temperature causes an increase in viscosity and slower phase separation. Of these regents, CYANEX 272 is selective for Mn over Ca and, therefore, it would be the better choice if there is Ca present in solution. A three-stage Mn extraction followed by a two-stage scrubbing and two-stage sulfuric acid stripping is an effective method of producing a very pure MnSO4 intermediate solution for further processing. From the intermediate MnSO4 some special Mn- products for ion exchange applications were synthesized and studied. Three types of octahedrally coordinated manganese oxide materials as an alternative final product for manganese were chosen for synthesis: layer structured Nabirnessite, tunnel structured Mg-todorokite and K-kryptomelane. As an alternative source of pure MnSO4 intermediate, kryptomelane was synthesized by using a synthetic hydrometallurgical tailings. The results show that the studied OMS materials adsorb selectively Cu, Ni, Cd and K in the presence of Ca and Mg. It was also found that the exchange rates were reasonably high due to the small particle dimensions. Materials are stable in the studied conditions and their maximum Cu uptake capacity was 1.3 mmol/g. Competitive uptake of metals and acid was studied using equilibrium, batch kinetic and fixed-bed measurements. The experimental data was correlated with a dynamic model, which also accounts for the dissolution of the framework manganese. Manganese oxide micro-crystals were also bound onto silica to prepare a composite material having a particle size large enough to be used in column separation experiments. The MnOx/SiO2 ratio was found to affect significantly the properties of the composite. The higher the ratio, the lower is the specific surface area, the pore volume and the pore size. On the other hand, higher amount of silica binder gives composites better mechanical properties. Birnesite and todorokite can be aggregated successfully with colloidal silica at pH 4 and with MnO2/SiO2 weight ratio of 0.7. The best gelation and drying temperature was 110oC and sufficiently strong composites were obtained by additional heat-treatment at 250oC for 2 h. The results show that silica–supported MnO2 materials can be utilized to separate copper from nickel and cadmium. The behavior of the composites can be explained reasonably well with the presented model and the parameters estimated from the data of the unsupported oxides. The metal uptake capacities of the prepared materials were quite small. For example, the final copper loading was 0.14 mmol/gMnO2. According to the results the special MnO2 materials are potential for a specific environmental application to uptake harmful metal ions.

Towards novel biogas upgrading processes

Biogas production has considerable development possibilities not only in Finland but all over the world since it is the easiest way of creating value out of various waste fractions and represents an alternative source of renewable energy. Development of efficient biogas upgrading technology has become an important issue since it improves the quality of biogas and for example facilitating its injection into the natural gas pipelines. Moreover, such upgrading contributes to resolving the issue of increasing CO2 emissions and addresses the increasing climate change concerns. Together with traditional CO2 capturing technologies a new class of recently emerged sorbents such as ionic liquids is claimed as promising media for gas separations. In this thesis, an extensive comparison of the performance of different solvents in terms of CO2 capture has been performed. The focus of the present study was on aqueous amine solutions and their mixtures, traditional ionic liquids, ‘switchable’ ionic liquids and poly(ionic liquid)s in order to reveal the best option for biogas upgrading. The CO2 capturing efficiency for the most promising solvents achieved values around 50 - 60 L CO2 / L absorbent. These values are superior to currently widely applied water wash biogas upgrading system. Regeneration of the solvent mixtures appeared to be challenging since the loss of initial efficiency upon CO2 release was in excess of 20 - 40 vol %, especially in the case of aqueous amine solutions. In contrast, some of the ionic liquids displayed reversible behavior. Thus, for selected “switchable” ionic and poly(ionic liquid)s the CO2 absorption/regeneration cycles were performed 3 - 4 times without any notable efficiency decrease. The viscosity issue, typical for ionic liquids upon CO2 saturation, was addressed and the information obtained was evaluated and related to the ionic interactions. The occurrence of volatile organic compounds (VOCs) before and after biogas upgrading was studied for biogas produced through anaerobic digestion of waste waters sludge. The ionic liquid [C4mim][OAc] demonstrated its feasibility as a promising scrubbing media and exhibited high efficiency in terms of the removal of VOCs. Upon application of this ionic liquid, the amount of identified VOCs was diminished by around 65 wt %, while the samples treated with the aqueous mixture of 15 wt % N-methyldiethanolamine with addition of 5 wt % piperazine resulted in 32 wt % reduction in the amounts of volatile organic compounds only.

Reduction of nitrogen oxide emissions in lime kiln

Different nitrogen oxide removal technologies for rotary lime kiln are studied in this thesis, the main focus being in commercial technologies. Post-combustion methods are investigated in more detail as potential possible NOx removal with combustion methods in rotary lime kiln is more limited or primary methods are already in use. However, secondary methods as NOx scrubber, SNCR or SCR technologies are not listed as the Best Available Technologies defined by European Union. BAT technologies for NOx removal in lime kiln are (1) Optimised combustion and combustion control, (2) Good mixing of fuel and air, (3) Low-NOx burner and (4) Fuel selection/low-N fuel. SNCR method is the most suitable technique for NOx removal in lime kiln when NOx removal from 50 % to 70 % is required in case primary methods are already in use or cannot be applied. In higher removal cases ammonia slip is an issue in SNCR. By using SCR better NOx reduction can be achieved but issues with catalyst materials are expected to arise because of the dust and sulphur dioxide which leads to catalyst poison formation in lower flue gas temperatures. NOx scrubbing has potential when simultaneous NOx and SO2 removal is required. The challenge is that NO cannot be scrubbed directly, but once it is oxidized to NO2 or further scrubbing can be performed as the solubility of NO2 is higher. Commercial installations have not been made regarding SNCR, SCR or NOx scrubbing regarding rotary lime kiln. For SNCR and SCR the closest references come from cement industry.

Embedded Service Bus for Internet of Things Interoperability

Internet of Things (IoT) technologies are developing rapidly, and therefore there exist several standards of interconnection protocols and platforms. The existence of heterogeneous protocols and platforms has become a critical challenge for IoT system developers. To mitigate this challenge, few alliances and organizations have taken the initiative to build a framework that helps to integrate application silos. Some of these frameworks focus only on a specific domain like home automation. However, the resource constraints in the large proportion of connected devices make it difficult to build an interoperable system using such frameworks. Therefore, a general purpose, lightweight interoperability framework that can be used for a range of devices is required. To tackle the heterogeneous nature, this work introduces an embedded, distributed and lightweight service bus, Lightweight IoT Service bus Architecture (LISA), which fits inside the network stack of a small real-time operating system for constrained nodes. LISA provides a uniform application programming interface for an IoT system on a range of devices with variable resource constraints. It hides platform and protocol variations underneath it, thus facilitating interoperability in IoT implementations. LISA is inspired by the Network on Terminal Architecture, a service centric open architecture by Nokia Research Center. Unlike many other interoperability frameworks, LISA is designed specifically for resource constrained nodes and it provides essential features of a service bus for easy service oriented architecture implementation. The presented architecture utilizes an intermediate computing layer, a Fog layer, between the small nodes and the cloud, thereby facilitating the federation of constrained nodes into subnetworks. As a result of a modular and distributed design, the part of LISA running in the Fog layer handles the heavy lifting to assist the lightweight portion of LISA inside the resource constrained nodes. Furthermore, LISA introduces a new networking paradigm, Node Centric Networking, to route messages across protocol boundaries to facilitate interoperability. This thesis presents a concept implementation of the architecture and creates a foundation for future extension towards a comprehensive interoperability framework for IoT.

Droplet Deposition in the Last Stage of Steam Turbine

During the expansion of steam in turbine, the steam crosses the saturation line and hence subsequent turbine stages run under wet condition. The stages under wet condition run with low efficiency as compared to stages running with supersaturated steam and the life of the last stage cascade is reduced due to erosion. After the steam crosses the saturation line it does not condense immediately but instead it becomes supersaturated which is a meta-stable state and reversion of equilibrium results in the formation of large number of small droplets in the range of 0.05 - 1 μm. Although these droplets are small enough to follow the stream lines of vapor however some of the fog droplets are deposited on the blade surface. After deposition they coagulate into films and rivulets which are then drawn towards the trailing edge of the blade due to viscous drag of the steam. These large droplets in the range of radius 100 μm are accelerated by steam until they impact on the next blade row causing erosion. The two phenomenon responsible for deposition are inertial impaction and turbulent-diffusion. This work shall discuss the deposition mechanism in steam turbine in detail and numerically model and validate with practical data.