Computational Analysis and Optimization of Real Gas Flow In Small Centrifugal Compressors

Small centrifugal compressors are more and more widely used in many industrialsystems because of their higher efficiency and better off-design performance comparing to piston and scroll compressors as while as higher work coefficient perstage than in axial compressors. Higher efficiency is always the aim of the designer of compressors. In the present work, the influence of four partsof a small centrifugal compressor that compresses heavy molecular weight real gas has been investigated in order to achieve higher efficiency. Two parts concern the impeller: tip clearance and the circumferential position of the splitter blade. The other two parts concern the diffuser: the pinch shape and vane shape. Computational fluid dynamics is applied in this study. The Reynolds averaged Navier-Stokes flow solver Finflo is used. The quasi-steady approach is utilized. Chien's k-e turbulence model is used to model the turbulence. A new practical real gas model is presented in this study. The real gas model is easily generated, accuracy controllable and fairly fast. The numerical results and measurements show good agreement. The influence of tip clearance on the performance of a small compressor is obvious. The pressure ratio and efficiency are decreased as the size of tip clearance is increased, while the total enthalpy rise keeps almost constant. The decrement of the pressure ratio and efficiency is larger at higher mass flow rates and smaller at lower mass flow rates. The flow angles at the inlet and outlet of the impeller are increased as the size of tip clearance is increased. The results of the detailed flow field show that leakingflow is the main reason for the performance drop. The secondary flow region becomes larger as the size of tip clearance is increased and the area of the main flow is compressed. The flow uniformity is then decreased. A detailed study shows that the leaking flow rate is higher near the exit of the impeller than that near the inlet of the impeller. Based on this phenomenon, a new partiallyshrouded impeller is used. The impeller is shrouded near the exit of the impeller. The results show that the flow field near the exit of the impeller is greatly changed by the partially shrouded impeller, and better performance is achievedthan with the unshrouded impeller. The loading distribution on the impeller blade and the flow fields in the impeller is changed by moving the splitter of the impeller in circumferential direction. Moving the splitter slightly to the suction side of the long blade can improve the performance of the compressor. The total enthalpy rise is reduced if only the leading edge of the splitter ismoved to the suction side of the long blade. The performance of the compressor is decreased if the blade is bended from the radius direction at the leading edge of the splitter. The total pressure rise and the enthalpy rise of thecompressor are increased if pinch is used at the diffuser inlet. Among the fivedifferent pinch shape configurations, at design and lower mass flow rates the efficiency of a straight line pinch is the highest, while at higher mass flow rate, the efficiency of a concave pinch is the highest. The sharp corner of the pinch is the main reason for the decrease of efficiency and should be avoided. The variation of the flow angles entering the diffuser in spanwise direction is decreased if pinch is applied. A three-dimensional low solidity twisted vaned diffuser is designed to match the flow angles entering the diffuser. The numerical results show that the pressure recovery in the twisted diffuser is higher than in a conventional low solidity vaned diffuser, which also leads to higher efficiency of the twisted diffuser. Investigation of the detailed flow fields shows that the separation at lower mass flow rate in the twisted diffuser is later than in the conventional low solidity vaned diffuser, which leads to a possible wider flow range of the twisted diffuser.

Challenges in packaging waste management: A case study in the fast food industry

The main research problem of this thesis is to find out the means of promoting the recovery of packaging waste generated in thefast food industry. The recovery of packaging waste generated in the fast food industry is demanded by the packaging waste legislation and expected by the public. The means are revealed by the general factors influencing the recovery of packaging waste, analysed by a multidisciplinary literature review and a case study focusing on the packaging waste managementof McDonald's Oy operating in Finland. The existing solid waste infrastructure does not promote the recovery ofpackaging waste generated in the fast food industry. The theoretical recovery rate of the packaging waste is high, 93 %, while the actual recovery rate is only 29 % consisting of secondary packaging manufactured from cardboard. The total recovery potential of packaging waste is 64 %, resulting in 1 230 tonnes ofrecoverable packaging waste. The achievable recovery potential of 33 %, equalling 647 tonnes of packaging waste could be recovered, but is not recovered mainly because of non-working waste management practises. The theoretical recovery potential of 31 %, equalling 583 tonnes of packaging waste can not be recovered by the existing solid waste infrastructure because of the obscure status of commecial waste, the improper operation ofproducer organisations, and the municipal autonomy. The sorting experiment indicated that it is possible to reach the achievable recovery potential inthe existing solid waste infrastructure. The achievement is promoted by waste producer -oriented waste management practises. The theoretical recovery potential can be reached by increasing the consistency of the solid waste infrastructure through governmental action.

Numerical and ExperimentalModelling of Gas Flow and Heat Transfer in the Air Gap of An Electric Machine

This work deals with the cooling of high-speed electric machines, such as motors and generators, through an air gap. It consists of numerical and experimental modelling of gas flow and heat transfer in an annular channel. Velocity and temperature profiles are modelled in the air gap of a high-speed testmachine. Local and mean heat transfer coefficients and total friction coefficients are attained for a smooth rotor-stator combination at a large velocity range. The aim is to solve the heat transfer numerically and experimentally. The FINFLO software, developed at Helsinki University of Technology, has been used in the flow solution, and the commercial IGG and Field view programs for the grid generation and post processing. The annular channel is discretized as a sector mesh. Calculation is performed with constant mass flow rate on six rotational speeds. The effect of turbulence is calculated using three turbulence models. The friction coefficient and velocity factor are attained via total friction power. The first part of experimental section consists of finding the proper sensors and calibrating them in a straight pipe. After preliminary tests, a RdF-sensor is glued on the walls of stator and rotor surfaces. Telemetry is needed to be able to measure the heat transfer coefficients at the rotor. The mean heat transfer coefficients are measured in a test machine on four cooling air mass flow rates at a wide Couette Reynolds number range. The calculated values concerning the friction and heat transfer coefficients are compared with measured and semi-empirical data. Heat is transferred from the hotter stator and rotor surfaces to the coolerair flow in the air gap, not from the rotor to the stator via the air gap, althought the stator temperature is lower than the rotor temperature. The calculatedfriction coefficients fits well with the semi-empirical equations and precedingmeasurements. On constant mass flow rate the rotor heat transfer coefficient attains a saturation point at a higher rotational speed, while the heat transfer coefficient of the stator grows uniformly. The magnitudes of the heat transfer coefficients are almost constant with different turbulence models. The calibrationof sensors in a straight pipe is only an advisory step in the selection process. Telemetry is tested in the pipe conditions and compared to the same measurements with a plain sensor. The magnitudes of the measured data and the data from the semi-empirical equation are higher for the heat transfer coefficients than thenumerical data considered on the velocity range. Friction and heat transfer coefficients are presented in a large velocity range in the report. The goals are reached acceptably using numerical and experimental research. The next challenge is to achieve results for grooved stator-rotor combinations. The work contains also results for an air gap with a grooved stator with 36 slots. The velocity field by the numerical method does not match in every respect the estimated flow mode. The absence of secondary Taylor vortices is evident when using time averagednumerical simulation.

Formation and Control of Trace Metal Emissions in Co-Firing of Biomass, Peat, and Wastes in Fluidised Bed Combustors

Environmentally harmful consequences of fossil fuel utilisation andthe landfilling of wastes have increased the interest among the energy producers to consider the use of alternative fuels like wood fuels and Refuse-Derived Fuels, RDFs. The fluidised bed technology that allows the flexible use of a variety of different fuels is commonly used at small- and medium-sized power plants ofmunicipalities and industry in Finland. Since there is only one mass-burn plantcurrently in operation in the country and no intention to build new ones, the co-firing of pre-processed wastes in fluidised bed boilers has become the most generally applied waste-to-energy concept in Finland. The recently validated EU Directive on Incineration of Wastes aims to mitigate environmentally harmful pollutants of waste incineration and co-incineration of wastes with conventional fuels. Apart from gaseous flue gas pollutants and dust, the emissions of toxic tracemetals are limited. The implementation of the Directive's restrictions in the Finnish legislation is assumed to limit the co-firing of waste fuels, due to the insufficient reduction of the regulated air pollutants in the existing flue gas cleaning devices. Trace metals emission formation and reduction in the ESP, the condensing wet scrubber, the fabric filter, and the humidification reactor were studied, experimentally, in full- and pilot-scale combustors utilising the bubbling fluidised bed technology, and, theoretically, by means of reactor model calculations. The core of the model is a thermodynamic equilibrium analysis. The experiments were carried out with wood chips, sawdust, and peat, and their refuse-derived fuel, RDF, blends. In all, ten different fuels or fuel blends were tested. Relatively high concentrations of trace metals in RDFs compared to the concentrations of these metals in wood fuels increased the trace metal concentrations in the flue gas after the boiler ten- to hundred-folds, when RDF was co-fired with sawdust in a full-scale BFB boiler. In the case of peat, lesser increase in trace metal concentrations was observed, due to the higher initial trace metal concentrations of peat compared to sawdust. Despite the high removal rate of most of the trace metals in the ESP, the Directive emission limits for trace metals were exceeded in each of the RDF co-firing tests. The dominat trace metals in fluegas after the ESP were Cu, Pb and Mn. In the condensing wet scrubber, the flue gas trace metal emissions were reduced below the Directive emission limits, whenRDF pellet was used as a co-firing fuel together with sawdust and peat. High chlorine content of the RDFs enhanced the mercuric chloride formation and hence the mercury removal in the ESP and scrubber. Mercury emissions were lower than theDirective emission limit for total Hg, 0.05 mg/Nm3, in all full-scale co-firingtests already in the flue gas after the ESP. The pilot-scale experiments with aBFB combustor equipped with a fabric filter revealed that the fabric filter alone is able to reduce the trace metal concentrations, including mercury, in the flue gas during the RDF co-firing approximately to the same level as they are during the wood chip firing. Lower trace metal emissions than the Directive limits were easily reached even with a 40% thermal share of RDF co-firing with sawdust.Enrichment of trace metals in the submicron fly ash particle fraction because of RDF co-firing was not observed in the test runs where sawdust was used as the main fuel. The combustion of RDF pellets with peat caused an enrichment of As, Cd, Co, Pb, Sb, and V in the submicron particle mode. Accumulation and release oftrace metals in the bed material was examined by means of a bed material analysis, mass balance calculations and a reactor model. Lead, zinc and copper were found to have a tendency to be accumulated in the bed material but also to have a tendency to be released from the bed material into the combustion gases, if the combustion conditions were changed. The concentration of the trace metal in the combustion gases of the bubbling fluidised bed boiler was found to be a summary of trace metal fluxes from three main sources. They were (1) the trace metal flux from the burning fuel particle (2) the trace metal flux from the ash in the bed, and (3) the trace metal flux from the active alkali metal layer on the sand (and ash) particles in the bed. The amount of chlorine in the system, the combustion temperature, the fuel ash composition and the saturation state of the bed material in regard to trace metals were discovered to be key factors affecting therelease process. During the co-firing of waste fuels with variable amounts of e.g. ash and chlorine, it is extremely important to consider the possible ongoingaccumulation and/or release of the trace metals in the bed, when determining the flue gas trace metal emissions. If the state of the combustion process in regard to trace metals accumulation and/or release in the bed material is not known,it may happen that emissions from the bed material rather than the combustion of the fuel in question are measured and reported.

The effects of potentiallydisruptive technology on business model - a case study of new technologies in ICT industry

This study examines how firms interpret new, potentially disruptive technologies in their own strategic context. The work presents a cross-case analysis of four potentially disruptive technologies or technical operating models: Bluetooth, WLAN, Grid computing and Mobile Peer-to-peer paradigm. The technologies were investigated from the perspective of three mobile operators, a device manufacturer and a software company in the ICT industry. The theoretical background for the study consists of the resource-based view of the firm with dynamic perspective, the theories on the nature of technology and innovations, and the concept of business model. The literature review builds up a propositional framework for estimating the amount of radical change in the companies' business model with two middle variables, the disruptiveness potential of a new technology, and the strategic importance of a new technology to a firm. The data was gathered in group discussion sessions in each company. The results of each case analysis were brought together to evaluate, how firms interpret the potential disruptiveness in terms of changes in product characteristics and added value, technology and market uncertainty, changes in product-market positions, possible competence disruption and changes in value network positions. The results indicate that the perceived disruptiveness in terms ofproduct characteristics does not necessarily translate into strategic importance. In addition, firms did not see the new technologies as a threat in terms of potential competence disruption.

Modeling dynamic behavior in tilting pad gas journal bearings

Thisresearch deals with the dynamic modeling of gas lubricated tilting pad journal bearings provided with spring supported pads, including experimental verification of the computation. On the basis of a mathematical model of a film bearing, a computer program has been developed, which can be used for the simulation of a special type of tilting pad gas journal bearing supported by a rotary spring under different loading conditions time dependently (transient running conditions due to geometry variations in time externally imposed). On the basis of literature, different transformations have been used in the model to achieve simpler calculation. The numerical simulation is used to solve a non-stationary case of a gasfilm. The simulation results were compared with literature results in a stationary case (steady running conditions) and they were found to be equal. In addition to this, comparisons were made with a number of stationary and non-stationary bearing tests, which were performed at Lappeenranta University of Technology using bearings designed with the simulation program. A study was also made using numerical simulation and literature to establish the influence of the different bearing parameters on the stability of the bearing. Comparison work was done with literature on tilting pad gas bearings. This bearing type is rarely used. One literature reference has studied the same bearing type as that used in LUT. A new design of tilting pad gas bearing is introduced. It is based on a stainless steel body and electron beam welding of the bearing parts. It has good operation characteristics and is easier to tune and faster to manufacture than traditional constructions. It is also suitable for large serial production.

Gas-liquid mass transfer in bubbly flow: Estimation of mass transfer, bubble size and reactor performance in various applications

Gas-liquid mass transfer is an important issue in the design and operation of many chemical unit operations. Despite its importance, the evaluation of gas-liquid mass transfer is not straightforward due to the complex nature of the phenomena involved. In this thesis gas-liquid mass transfer was evaluated in three different gas-liquid reactors in a traditional way by measuring the volumetric mass transfer coefficient (kLa). The studied reactors were a bubble column with a T-junction two-phase nozzle for gas dispersion, an industrial scale bubble column reactor for the oxidation of tetrahydroanthrahydroquinone and a concurrent downflow structured bed.The main drawback of this approach is that the obtained correlations give only the average volumetric mass transfer coefficient, which is dependent on average conditions. Moreover, the obtained correlations are valid only for the studied geometry and for the chemical system used in the measurements. In principle, a more fundamental approach is to estimate the interfacial area available for mass transfer from bubble size distributions obtained by solution of population balance equations. This approach has been used in this thesis by developing a population balance model for a bubble column together with phenomenological models for bubble breakage and coalescence. The parameters of the bubble breakage rate and coalescence rate models were estimated by comparing the measured and calculated bubble sizes. The coalescence models always have at least one experimental parameter. This is because the bubble coalescence depends on liquid composition in a way which is difficult to evaluate using known physical properties. The coalescence properties of some model solutions were evaluated by measuring the time that a bubble rests at the free liquid-gas interface before coalescing (the so-calledpersistence time or rest time). The measured persistence times range from 10 msup to 15 s depending on the solution. The coalescence was never found to be instantaneous. The bubble oscillates up and down at the interface at least a coupleof times before coalescence takes place. The measured persistence times were compared to coalescence times obtained by parameter fitting using measured bubble size distributions in a bubble column and a bubble column population balance model. For short persistence times, the persistence and coalescence times are in good agreement. For longer persistence times, however, the persistence times are at least an order of magnitude longer than the corresponding coalescence times from parameter fitting. This discrepancy may be attributed to the uncertainties concerning the estimation of energy dissipation rates, collision rates and mechanisms and contact times of the bubbles.

Origins of production errors and significance of employee empowerment in reducing production error amount in sheet metal fabricating industry

The market place of the twenty-first century will demand that manufacturing assumes a crucial role in a new competitive field. Two potential resources in the area of manufacturing are advanced manufacturing technology (AMT) and empowered employees. Surveys in Finland have shown the need to invest in the new AMT in the Finnish sheet metal industry in the 1990's. In this run the focus has been on hard technology and less attention is paid to the utilization of human resources. In manymanufacturing companies an appreciable portion of the profit within reach is wasted due to poor quality of planning and workmanship. The production flow production error distribution of the sheet metal part based constructions is inspectedin this thesis. The objective of the thesis is to analyze the origins of production errors in the production flow of sheet metal based constructions. Also the employee empowerment is investigated in theory and the meaning of the employee empowerment in reducing the overall production error amount is discussed in this thesis. This study is most relevant to the sheet metal part fabricating industrywhich produces sheet metal part based constructions for electronics and telecommunication industry. This study concentrates on the manufacturing function of a company and is based on a field study carried out in five Finnish case factories. In each studied case factory the most delicate work phases for production errors were detected. It can be assumed that most of the production errors are caused in manually operated work phases and in mass production work phases. However, no common theme in collected production error data for production error distribution in the production flow can be found. Most important finding was still that most of the production errors in each case factory studied belong to the 'human activity based errors-category'. This result indicates that most of the problemsin the production flow are related to employees or work organization. Development activities must therefore be focused to the development of employee skills orto the development of work organization. Employee empowerment gives the right tools and methods to achieve this.

Metsäteollisuuden sivutuotepolttoaineiden hyödyntäminen Etelä-Karjalassa

Tässä diplomityössä on selvitetty merkittävimpien kotimaisten polttoaineiden määrät Etelä-Karjalassa vuonna 1999. Pääpaino työssä on metsäteollisuuden sivutuotepolttoaineiden tarkastelussa. Metsähakkeelle ja kierrätyspolttoaineille on määritetty tuotantopotentiaalit. Myös turpeen tuotantomäärät on selvitetty. Lisäksi työssä on tarkasteltu alueella sijaitsevien teollisuuslaitosten ja kuntien energialaitosten polttoaineiden käyttöä. Työn tuloksia käytetään tutkimuksen seuraavassa vaiheessa, jolloin pyritään kehittämään teollisuusyritysten ja yhdyskuntien välistä energiaintegraatiota. Etelä-Karjalan kemiallisen metsäteollisuuden oman käytön ylijäävä sivutuotepolttoaineiden määrä oli vuonna 1999 yli 230 000 k-m3 (370 GWh). Mekaanisen metsäteollisuuden vastaava luku oli noin 210 000 k-m3 (330 GWh). Puunkäyttömäärien, energiankäyttötietojen ja kirjallisuudesta saatavien osuuksien perusteella mekaanisen metsäteollisuuden sivutuotepolttoaineiden oman käytön ylijäävä määrä olisi noin 350 000 k-m3 (580 GWh). Eroa selittävät lähinnä tilastolliset virheet, sivutuoteliiketoiminnan vähyys ja vaihtoehtoiset käyttökohteet. Metsähakkeen tuotantopotentiaali oli vuoden 1999 hakkuutietoihin perustuen yli 640 000 k-m3, josta tekniset, taloudelliset ja ympäristölliset seikat huomioiden noin 210 000 k-m3 (410 GWh) olisi voitu hyödyntää energiantuotannossa. Etelä-Karjalassa vuonna 1999 syntyneistä jätemääristä olisi arvioiden mukaan voitu valmistaa noin 25 000 tonnia (100 GWh) kierrätyspolttoaineita. Kierrätyspolttoaineiden valmistus alkaa Joutsenossa vuosien 2003 - 2004 välillä. Turpeen tuotantomäärä oli vuonna 1999 noin 1 200 000 tonnia (1020 GWh). Etelä-Karjalan teollisuus ja kuntien energialaitokset käyttivät vuonna 1999 yli 17400 GWh polttoaineita. Ostopolttoaineiden tarve oli noin 4700 GWh, josta lähes 85 % täytettiin maakaasulla. Alueen kunnista kaikki, joissa ei ole kemiallista metsäteollisuutta, pystyisivät teoriassa täyttämään teollisuuden ja energialaitostensa ostopolttoaineiden tarpeen oman kunnan alueelta saatavilla kotimaisilla polttoaineilla.

Uudet DCHP-prosessit

Diplomityön tavoitteena on selvittää viiden uuden yhdistetyn sähkön- ja lämmöntuotantoprosessin taloudellisuus Suomessa ja Keski-Euroopassa. Polttoaineena käytetään maakaasua. Tehoalue on 1 kW – 1 MW. Työn alkuosassa on kerrottu kyseisten prosessien tekniset ominaisuudet ja käyttö tällä hetkellä. Työn loppuosassa on laskettu jokaisen prosessin taloudellisuus viidessä eri maassa (Suomessa, Alankomaassa, Belgiassa, Iso-Britanniassa ja Saksassa) viidessä eri skenaariossa (omakotitalot, rivitalot, kerrostalot, pienteollisuus ja keskisuuri teollisuus). Toisena aihepiirinä diplomityössä on verrattu kompressori- ja absorptiojäähdyttimiä keskenään ja kerrottu kaukokylmän tekemisestä. Työn tuloksena saatiin arvio siitä, miten taloudellisesti kannattavia kyseiset prosessit ovat tällä hetkellä verrattuna perinteisiin sähkön- ja lämmöntuotantotapoihin.

Sellu- ja paperiteollisuuden haitallisimmat ilmapäästöt

Diplomityössä luotiin katsaus sellu- ja paperiteollisuuden haitallisimpiin ilmapäästöihin ja ilmapäästömäärien kehitykseen Suomessa 1990-luvun alusta nykypäivään. Työssä tutustuttiin sellu- ja paperiteollisuuden ilmapäästöjä rajoittavan lainsäädännön ajankohtaisiin asioihin Suomessa ja Euroopan Unionissa, sekä tarkasteltiin nykyisen lainsäädännön perustana olleita ilmastosopimuksia eli kansainvälisen ilmastopolitiikan syntyä ja kehittymistä. Työssä on myös selvitetty ilman osuutta paperinvalmistuksessa, tutustuttu ilmapäästöjen rajoittamismenetelmiin ja eri mittausmenetelmiin ilmapäästöjen toteamiseksi. Työn puitteissa suoritettiin mittalaitetestejä eri paperitehtailla. Haitallisimpia ja määrällisesti suurimpia ilmapäästöjä sellu- ja paperiteollisuudessa ovat typen ja rikin oksidit, pelkistyneet rikkiyhdisteet, hiukkaset, haihtuvat orgaaniset yhdisteet (VOC) ja hiilidioksidi. Ilmapäästömäärät Suomessa ovat typenoksideja lukuun ottamatta olleet laskussa 1990-luvun alusta nykypäivään. Tärkein kasvihuonekaasu on hiilidioksidi, jonka määrää rajoitetaan Kioton sopimuksessa. Vuoden 2002 aikana selvinneekin, mikä on Kioton sopimuksen vaikutus Suomen metsäteollisuuteen. Päästömittauksia tarvitaan lainsäädännön raja-arvojen toteamiseksi, mittauksia suorittavat sertifioidut päästömittauslaboratoriot. Suoritetuissa mittalaitetesteissä havaittiin mittalaitteiden soveltuvuudessa kosteiden paperiprosessin poistokaasujen määrittämiseen suuria eroja.

Energiataseen hallinta ja optimointi metsäteollisuusintegraatissa

Diplomityö on tehty UPM-Kymmene Oyj, Kaukaan tehtailla Lappeenrannassa. Integroidussa metsäteollisuudessa energiantuotanto koostuu yleensä sähkön- ja lämmöntuotannosta. Kaukaan tehtailla prosessien lämmöntarve saadaan katettua kokonaisuudessaan omalla tuotannolla, kun taas kulutetusta sähköstä ainoastaan puolet on tuotettu itse. Loput sähköntarpeesta joudutaan ostamaan ulkopuolelta. Tutkimuksen pääpaino on ollut selvittää, miten kustannukset ovat riippuvaisia energiantuotannosta erilaisissa käyttöolosuhteissa. Työn tuloksena on luotu tietokonepohjainen laskentamalli, jonka avulla Kaukaan tehtaiden energiantuotantoa voidaan ohjata taloudellisesti optimaalisimmalla tavalla kulloinkin vallitsevassa käyttötilanteessa. Lisäksi tutkimuksessa on analysoitu tehdasintegraatin lämmönkulutuksen seurannan mahdollisuuksia lämmönsiirtoverkon nykyisten mittausten perusteella. Työssä on kerrottu yleisesti metsäteollisuuden energiankulutuksesta Suomessa. Lisäksi on esitetty arvioita energiankulutuksen kehityksestä tulevaisuudessa sekä keinoja energiatehokkuuden parantamiseksi. Kaukaan tehtailla lämmönkulutuksen seurantaan käytettävät mittausmenetelmät ja -laitteet on esitelty virtausmittausten osalta sekä arvioitu nykyisten mittausten luotettavuutta ja riittävyyttä kokonaisvaltaisen lämpötaseen hallintaan. Kaukaan tehtaiden energiantuotantojärjestelmästä on luotu termodynaaminen malli, johon energiantuotannosta aiheutuneiden kustannusten laskenta perustuu. Energiantuotannon optimoinnilla pyritään määrittelemään tietyn tarkasteluhetken käyttötilanteessa taloudellisesti optimaalisin kattiloiden ajojärjestys. Tarkastelu on rajattu lämmöntuotannon lisäämisen osalta maakaasun käytön lisäämiseen ja höyryturbiinien ohitukseen. Sähkön ja maakaasun hinnan sekä ympäristön lämpötilan vaihtelujen vaikutusta optimaaliseen ajojärjestykseen on havainnollistettu esimerkkien avulla.

SB-lateksitehtaan päästöjen minimointi

Diplomityön tavoitteena oli löytää soveltuvimmat parhaaseen käytettävissä olevaan tekniikkaan perustuvat menetelmät SB-lateksitehtaan päästöjen käsittelemiseksi. Kirjallisuuslähteinä käytettiin Euroopan komission julkaisemia toimialakohtaisia BAT-julkaisuja. Lisäksi hyödynnettiin kemianteollisuudessa jo käytössä olevien menetelmien kokemusperäistä tietoa. Kokeellinen osan pohjaksi kartoitettiin merkittävät päästölähteet: kiinteät, nestemäiset ja kaasumaiset päästöt. Päästömittaukset olivat kvantitatiivisia, mutta mittauksissa kerättiin myös kvalitatiivista tietoa. Kirjallisen ja kokemusperäisen tiedon sekä päästöjen mittaustulosten perusteella valittiin soveltuvimmat päästöjenkäsittelyvaihtoehdot. Kiinteiden päästöjen määrään vaikuttaa eniten lateksin suodatusmenetelmän valinta. Nestemäisten päästöjen uudelleenkäyttö on tehokkain tapa minimoida päästöjä. Tehokkain tapa käsitellä orgaanisia jätevesiä on kolonnistrippaus. Lateksipitoisille jätevesille soveltuvin menetelmä on membraanitekniikka. Kaasuseospäästöille soveltuvin käsittelymenetelmä on terminen kammiopoltto. Yhden kemikaalin kaasupäästöjen käsittelyssä menetelmät perustuvat kondensointiin, paikallisiin suodattimiin ja kaasujen takaisinkierrätykseen riippuen kemikaalin ominaisuuksista.

Supplier Evaluation on the Standard Material and Component Markets in the Electronic Manufacturing Equipment Industry

Työn tavoitteena oli arvioida ja selvittää toimittajasuhteeseen vaikuttavia tekijöitä JOT Automation Group Oyj.n ja sen alihankkijoiden välisessä yhteistyössä ja muodostaa yrityksen kilpailukykyä parantava toimittaja-arviointiprosessi. Työssä keskityttiin tarkastelemaan yleisillä materiaali- ja komponenttimarkkinoilla toimivia toimittajia elektroniikkateollisuuden tuotantojärjestelmien valmistuksessa. Ensin tutustuttiin toimittajasuhdetta ja sen arviointia käsitelleeseen kirjallisuuteen. Teorian tueksi tehtiin haastatteluja ja kartoitettiin ensisijaisia tarpeita ja tavoitteita arviointiprosessille. Valmis prosessi testattiin käytännössä kahden eri case-esimerkin avulla. Prosessista muodostui kahteen eri työkaluun jakautunut kokonaisuus, joista auditointi arvioi toimittajan kyvykkyyttä vastatta sille asetettuihin vaatimuksiin. Toimittajan suorituskyvyn mittaaminen puolestaan testaa ja vertaa jatkuvasti toiminnan todellista tasoa auditoinnissa saatuihin tuloksiin. Työ sisältää selvityksen ja ohjeistuksen toimittaja-arviointiprosessin käytöstä. Prosessin käyttö alentaa toimittajaan kohdistuvaa materiaalien saatavuuteen ja hankintaan liittyviä riskejä. Esimerkeistä saadut kokemukset osoittivat, että prosessin avulla päästään pureutumaan tärkeisiin ydinalueisiin ja kehittämään niitä sekä toimittajalle, että ostajayritykselle edullisella tavalla. Toimittaja-arviointiprosessista kehittyy toimintatapa yrityksen ja sen toimittajan välisen suhteen ylläpitämiseksi.

Entry Strategy Issues in the Ophthalmic Industry: Entry Mode, Pricing and Distribution

Maahantulostrategia asettaa yrityksen kansainvälisiä liiketoimintoja ohjaavat tavoitteet, päämäärät, resurssit ja toiminnan suuntaviivat. Tämä diplomityö käsittelee yrityksen maahantulostrategian elementeistä operaatiomuodon valintaa, hinnoittelua ja jakelua. Työssä rakennetaan teoriakehys elementteihin liittyvien päätösten tutkimiseksi lääketeollisuuden ominaispiirteet huomioiden. Lääketeollisuudella on muihin teollisuudenaloihin verrattuna useita erityispiirteitä, joihin työ perehdyttää. Lisäksi työn olennainen osa on selvittää lääketeollisuuden maakohtaisia säädöksiä ja toimintamalleja. Diplomityö on tehty silmäläkkeitä valmistavalle, kehittävälle ja markkinoivalle Santen Oy:lle, joka suunnittelee toimintansa laajentamista Keski- ja Etelä-Euroopan markkinoille. Tässä laajentumisprosessissa ensimmäisenä kohdemaana on Saksa, jonka markkinoille suuntautuvia toimenpiteitä työ tutkii. Teoriakehyksen, markkinoiden ominaispiirteiden sekä useiden erilaisten analyysien pohjalta työn tavoitteena on antaa operaatiomuotoa, tuotteiden hinnoittelua ja jakelua koskevia suosituksia.