PDM system functions and utilizations analysis to improve efficiency of sheet metal product design and manufacturing

This study will concentrate on Product Data Management (PDM) systems, and sheet metal design features and classification. In this thesis, PDM is seen as an individual system which handles all product-related data and information. The meaning of relevant data is to take the manufacturing process further with fewer errors. The features of sheet metals are giving more information and value to the designed models. The possibility of implementing PDM and sheet metal features recognition are the core of this study. Their integration should make the design process faster and manufacturing-friendly products easier to design. The triangulation method is the basis for this research. The sections of this triangle are: scientific literature review, interview using the Delphi method and the author’s experience and observations. The main key findings of this study are: (1) the area of focus in triangle (the triangle of three different point of views: business, information exchange and technical) depends on the person’s background and their role in the company, (2) the classification in the PDM system (and also in the CAD system) should be done using the materials, tools and machines that are in use in the company and (3) the design process has to be more effective because of the increase of industrial production, sheet metal blank production and the designer’s time spent on actual design and (4) because Design For Manufacture (DFM) integration can be done with CAD-programs, DFM integration with the PDM system should also be possible.

How can we agree on some product agnostic repository function fundamentals?

Presentation at Open Repositories 2014, Helsinki, Finland, June 9-13, 2014

Software product line for power converters

Työn tilaajana toimi Visedo Oy. Työn tavoitteina oli tutkia Visedo Oy:n ohjelmistokehityksen nykytila, tunnistaa seuraavat parannuskohteet ja antaa ohjeita havaittujen parannuskohteiden korjaamiseksi. Visedo Oy:n tehonmuokkain ohjelmistokehityksen nykytilaa käsiteltiin neljän valitun osa-alueen näkökulmasta: ohjelmistoarkkitehtuurityyli, komponenttipohjainen ohjelmistokehitys, ohjelmistotuotelinjojen kehitysmenetelmät ja ohjelmistovariaatioiden hallinta. Valituilla osa-alueilla havaittujen parannuskohteiden perusteella annettiin korjausehdotuksia: ohjelmistoarkkitehtuurin rakenteeseen, komponenttien jakautumiselle, komponenttien koostamiselle ja komponenttien versioinnille. Lisäksi ehdotettiin uudenlaista ohjelmistotuotelinja rakennetta, joka yhdistää kerros- ja komponenttipohjaiset arkkitehtuurityylit mahdollistaen ominaisuuksiltaan eroavien tehonmuokkain ohjelmistojen hallinnan.

Service paradox in a product oriented company: A service business development case

The master´s thesis had three aims; to develop a service portfolio, to support the management of services through the developed portfolio, and evaluate effects of service differentiation strategy on the future selection of services. The product oriented case company in service paradox is Hilti (Suomi) Oy, which is entering systematic service management era, supported by the late strategic change. Low return on service business investments is referred as service paradox. The project was carried out as a case study, where the primary information source was twenty-one conducted interviews. The theory part focuses on marketing logics, service strategies, and categorization of services. The empirical part contributes in solving the aim related research questions. As a result of the case study a service portfolio was created, next further steps in service management were suggested, and the effect on selection of services by service differentiation strategy was evaluated. The main goal of creating service portfolio contributes to systematic management of services, which required revising at the case company.

Jätteen kaasutus ja energiakäyttö

Kiinteiden polttoaineiden muuntaminen kaasumaiseen muotoon eli kaasuttaminen herätti jo vuosia sitten tutkijoiden kiinnostusta. Suomessa yleinen mielenkiinto on viimeaikoina keskittynyt edullisempien polttoaineiden kaasuttamiseen ja saatavan tuotekaasun polttamiseen. Lahti Energian uudessa Kymijärvi 2 voimalaitoksessa kaasutetaan puuta ja kierrätyspolttoainetta (REF). Saatava tuotekaasu jäähdytetään ja suodatetaan, jotta epäpuhtaudet saadaan pois tuotekaasusta. Puhdistettu tuotekaasu poltetaan kaasukattilassa korkeilla höyrynarvoilla. Tuotekaasun jäähdyttämistä ei ole paljoa tehty eikä siitä ole juurikaan tieteellistä tutkimusta eikä kokemusta. Tuotekaasun jäähtyessä partikkelit tarttuvat lämpöpinnoille aiheuttaen kerrostumia. Kerrostumat heikentävät lämmönsiirtoa olennaisesti. Tämän työn tarkoitus on tutkia kaasutusprosessia, tuotekaasun jäähdyttimen likaantumista sekä antaa lisätietoja likaantumiseen vaikuttavista tekijöistä.

Siiderin ja long drink -juomien sekoitusprosessin kehittäminen

Diplomityössä perehdytään Hartwall Lahden tuotantolaitoksen juomanvalmistuksen osaston siiderin ja long drink –juomien valmistusprosessin kehittämiseen. Diplomityön tavoitteena oli löytää prosessin ongelma- ja poikkeamakohtia, tutkia mahdollisia hävikkikohteita ja suorittaa laadun osalta ajoseurantamittauksia. Ongelmakohtien pohjalta laadittiin parannusehdotuksia ja niitä toteutettiin jo tämän projektin aikana. Ongelma- ja poikkeamakohtia tutkittiin ajoprosessin aikana. Hävikkitutkimus kohdennettiin aromiliuoksen annostelulinjaan, nestesokerin an-nostelulinjaan ja tuotteiden alku- ja lopputyönnöille painetankkeihin. Painetankkien osalta mahdollisia hävikkikohteita tutkittiin kokeellisen toiminnan avulla ajo-prosessin aikana. Ajoprosessin käynnistyksen jälkeen selvitettiin milloin valmis tuote on painetankkien venttiilimatriisilla. Uudet parametrit alku- ja lopputyönnöille määritettiin tuoteputken, painetankkien pohjaputkien ja venttiilimatriisin tilavuuksien avulla. Hävikkitutkimuksen tuloksena saatiin pienennettyä hävikkiä ja näin ollen syntyi kustannussäästöjä. Hiilidioksidin sitoutuvuutta tutkittiin mittauksien avulla valmistusprosessin aikana. Mittauksien perusteella havaittiin, että hiilidioksidipitoisuus laskee painetankissa. Tämä johtuu valmiin tuotteen lämpötilamuutoksista. Tuotteen lämpötilaa voidaan tasata esimerkiksi levylämmönvaihtimen avulla.

UHPLC-epäpuhtausmenetelmän kehittäminen ja validointi inhalaatiovalmisteelle

Tämän diplomityön tarkoituksena on kehittää menetelmä, jolla voidaan seurata inhalaatiovalmisteen sisältämiä epäpuhtauksia. Menetelmä kehitetään erittäin korkean suorituskyvyn kromatografialaitteistolle (Ultra High Performance Liquid Chromatography, UHPLC) jo olemassa olevan HPLC-epäpuhtausmenetelmän pohjalta. Uusi menetelmä kehitetään analyysiajan lyhentämiseksi ja erotuksen resoluution parantamiseksi. Työn kirjallisuusosa esittelee lyhyesti inhalaatiovalmisteet sekä nestekromatografian perusteet. Korkean erotuskyvyn nestekromatografia ja analysoinnin apuna käytettävät parametrit selvitetään laskukaavoineen. Kirjallisuusosa keskittyy epäpuhtausmenetelmän kehittämisen kulkuun ja menetelmän validoinnissa suoritettaviin kokeisiin. Soveltavassa osassa Orion Oyj:n kehitteillä olevalle kahden vaikuttavan aineen inhalaatiovalmisteelle kehitetään UHPLC-epäpuhtausmenetelmä kirjallisuusosiossa esitellyn menetelmäkehitysrungon pohjalta. Menetelmäkehityksen kulku ja analyysin olosuhteiden valinta esitellään pääpiirteittäin, jonka jälkeen kehitetty menetelmä validoidaan sille tehdyn validointisuunnitelman mukaisesti. Kehitetystä UHPLC-epäpuhtausmenetelmästä saatiin 16 minuuttia lyhyempi kuin vastaava HPLC-epäpuhtausmenetelmä. Myös analyysin resoluutio parantui merkittävästi. Toistuvien injektioiden jälkeen kromatogrammissa esiintyi kuitenkin häntimistä, joka johti merkittävään resoluution heikkenemiseen. Häntimisen syyksi epäiltiin toisen vaikuttavan aineen kiinnittymistä kolonnimateriaaliin, mutta sen estämiseksi ehdotetut toimenpiteet eivät sopineet kehitettyyn menetelmään.

Tuotetietoprosessin kehittäminen päivittäistavarakaupan toimitusketjussa

Diplomityö toteutettiin Yritys X:n toimeksiantona. Työ sai alkunsa Yritys X:n tarpeesta kehittää yrityksen ja sen asiakasomistajien yhteistä tuotetietoprosessia. Tavoitteena oli saada kuvaus tuotetietoprosessin nykytilasta sekä sen pohjalta luoda kehitysehdotukset, joilla prosessia voitaisiin tehostaa. Työssä käytettiin kvalitatiivista eli laadullista tutkimusmenetelmää. Tietoa tuotetietoprosessin nykytilasta etsittiin pääsääntöisesti lukuisten Yritys X:n ja sen asiakasomistajien henkilöstön haastattelujen avulla. Lisäksi työtä tehdessä tutustuttiin laajasti toimitusketjuyhteistyöstä, tiedon läpinäkyvyyden merkityksestä, tiedonhallinnasta ja tuotetietoprosessista kertovaan kirjallisuuteen. Työn tuloksena saatiin kuvaus siitä, miten Yritys X ja sen asiakasomistajat käsittelevät tuotetietoja sekä mitkä ovat tuotetietoprosessin suurimmat haasteet. Tämän pohjalta luotiin kehitysehdotukset, joilla prosessia voitaisiin tehostaa. Tuotetietoprosessin suurimpana haasteena nähtiin olevan se, että koko ryhmittymän yhteistä etua ei ole huomioitu prosessia luodessa sekä se, että prosessissa tehdään päällekkäistä ja manuaalista työtä, joka olisi mahdollista välttää tiedon jakamisen ja sähköisen tiedonsiirron avulla. Tärkeimmiksi kehitysehdotuksiksi muodostui tuotetietoprosessin tarkastelu ja kehittäminen jatkossa kokonaisuutena, yhteistyön ja tiedon jakamisen lisääminen, Yritys X:ltä saatavien tuotetietojen laajempi hyödyntäminen asiakasomistajilla, sähköisen tiedonsiirron merkittävä lisääminen sekä yhtenäisen tuotetietojen laadunhallintajärjestelmän luominen ja sitä myötä tuotetietoprosessin ja sen tehokkuuden mittaaminen.

Utilization of steelmaking waste materials for production of calcium carbonate (CaCO3)

The steel industry produces, besides steel, also solid mineral by-products or slags, while it emits large quantities of carbon dioxide (CO2). Slags consist of various silicates and oxides which are formed in chemical reactions between the iron ore and the fluxing agents during the high temperature processing at the steel plant. Currently, these materials are recycled in the ironmaking processes, used as aggregates in construction, or landfilled as waste. The utilization rate of the steel slags can be increased by selectively extracting components from the mineral matrix. As an example, aqueous solutions of ammonium salts such as ammonium acetate, chloride and nitrate extract calcium quite selectively already at ambient temperature and pressure conditions. After the residual solids have been separated from the solution, calcium carbonate can be precipitated by feeding a CO2 flow through the solution. Precipitated calcium carbonate (PCC) is used in different applications as a filler material. Its largest consumer is the papermaking industry, which utilizes PCC because it enhances the optical properties of paper at a relatively low cost. Traditionally, PCC is manufactured from limestone, which is first calcined to calcium oxide, then slaked with water to calcium hydroxide and finally carbonated to PCC. This process emits large amounts of CO2, mainly because of the energy-intensive calcination step. This thesis presents research work on the scale-up of the above-mentioned ammonium salt based calcium extraction and carbonation method, named Slag2PCC. Extending the scope of the earlier studies, it is now shown that the parameters which mainly affect the calcium utilization efficiency are the solid-to-liquid ratio of steel slag and the ammonium salt solvent solution during extraction, the mean diameter of the slag particles, and the slag composition, especially the fractions of total calcium, silicon, vanadium and iron as well as the fraction of free calcium oxide. Regarding extraction kinetics, slag particle size, solid-to-liquid ratio and molar concentration of the solvent solution have the largest effect on the reaction rate. Solvent solution concentrations above 1 mol/L NH4Cl cause leaching of other elements besides calcium. Some of these such as iron and manganese result in solution coloring, which can be disadvantageous for the quality of the PCC product. Based on chemical composition analysis of the produced PCC samples, however, the product quality is mainly similar as in commercial products. Increasing the novelty of the work, other important parameters related to assessment of the PCC quality, such as particle size distribution and crystal morphology are studied as well. As in traditional PCC precipitation process, the ratio of calcium and carbonate ions controls the particle shape; a higher value for [Ca2+]/[CO32-] prefers precipitation of calcite polymorph, while vaterite forms when carbon species are present in excess. The third main polymorph, aragonite, is only formed at elevated temperatures, above 40-50 °C. In general, longer precipitation times cause transformation of vaterite to calcite or aragonite, but also result in particle agglomeration. The chemical equilibrium of ammonium and calcium ions and dissolved ammonia controlling the solution pH affects the particle sizes, too. Initial pH of 12-13 during the carbonation favors nonagglomerated particles with a diameter of 1 μm and smaller, while pH values of 9-10 generate more agglomerates of 10-20 μm. As a part of the research work, these findings are implemented in demonstrationscale experimental process setups. For the first time, the Slag2PCC technology is tested in scale of ~70 liters instead of laboratory scale only. Additionally, design of a setup of several hundreds of liters is discussed. For these purposes various process units such as inclined settlers and filters for solids separation, pumps and stirrers for material transfer and mixing as well as gas feeding equipment are dimensioned and developed. Overall emissions reduction of the current industrial processes and good product quality as the main targets, based on the performed partial life cycle assessment (LCA), it is most beneficial to utilize low concentration ammonium salt solutions for the Slag2PCC process. In this manner the post-treatment of the products does not require extensive use of washing and drying equipment, otherwise increasing the CO2 emissions of the process. The low solvent concentration Slag2PCC process causes negative CO2 emissions; thus, it can be seen as a carbon capture and utilization (CCU) method, which actually reduces the anthropogenic CO2 emissions compared to the alternative of not using the technology. Even if the amount of steel slag is too small for any substantial mitigation of global warming, the process can have both financial and environmental significance for individual steel manufacturers as a means to reduce the amounts of emitted CO2 and landfilled steel slag. Alternatively, it is possible to introduce the carbon dioxide directly into the mixture of steel slag and ammonium salt solution. The process would generate a 60-75% pure calcium carbonate mixture, the remaining 25-40% consisting of the residual steel slag. This calcium-rich material could be re-used in ironmaking as a fluxing agent instead of natural limestone. Even though this process option would require less process equipment compared to the Slag2PCC process, it still needs further studies regarding the practical usefulness of the products. Nevertheless, compared to several other CO2 emission reduction methods studied around the world, the within this thesis developed and studied processes have the advantage of existing markets for the produced materials, thus giving also a financial incentive for applying the technology in practice.

Heterogeneous mass transfer in fluidized beds by computational fluid dynamics

The main objective of this research is to estimate and characterize heterogeneous mass transfer coefficients in bench- and pilot-scale fluidized bed processes by the means of computational fluid dynamics (CFD). A further objective is to benchmark the heterogeneous mass transfer coefficients predicted by fine-grid Eulerian CFD simulations against empirical data presented in the scientific literature. First, a fine-grid two-dimensional Eulerian CFD model with a solid and gas phase has been designed. The model is applied for transient two-dimensional simulations of char combustion in small-scale bubbling and turbulent fluidized beds. The same approach is used to simulate a novel fluidized bed energy conversion process developed for the carbon capture, chemical looping combustion operated with a gaseous fuel. In order to analyze the results of the CFD simulations, two one-dimensional fluidized bed models have been formulated. The single-phase and bubble-emulsion models were applied to derive the average gas-bed and interphase mass transfer coefficients, respectively. In the analysis, the effects of various fluidized bed operation parameters, such as fluidization, velocity, particle and bubble diameter, reactor size, and chemical kinetics, on the heterogeneous mass transfer coefficients in the lower fluidized bed are evaluated extensively. The analysis shows that the fine-grid Eulerian CFD model can predict the heterogeneous mass transfer coefficients quantitatively with acceptable accuracy. Qualitatively, the CFD-based research of fluidized bed process revealed several new scientific results, such as parametrical relationships. The huge variance of seven orders of magnitude within the bed Sherwood numbers presented in the literature could be explained by the change of controlling mechanisms in the overall heterogeneous mass transfer process with the varied process conditions. The research opens new process-specific insights into the reactive fluidized bed processes, such as a strong mass transfer control over heterogeneous reaction rate, a dominance of interphase mass transfer in the fine-particle fluidized beds and a strong chemical kinetic dependence of the average gas-bed mass transfer. The obtained mass transfer coefficients can be applied in fluidized bed models used for various engineering design, reactor scale-up and process research tasks, and they consequently provide an enhanced prediction accuracy of the performance of fluidized bed processes.

Advanced analysis and design methods for preparative chromatographic separation processes

Preparative liquid chromatography is one of the most selective separation techniques in the fine chemical, pharmaceutical, and food industries. Several process concepts have been developed and applied for improving the performance of classical batch chromatography. The most powerful approaches include various single-column recycling schemes, counter-current and cross-current multi-column setups, and hybrid processes where chromatography is coupled with other unit operations such as crystallization, chemical reactor, and/or solvent removal unit. To fully utilize the potential of stand-alone and integrated chromatographic processes, efficient methods for selecting the best process alternative as well as optimal operating conditions are needed. In this thesis, a unified method is developed for analysis and design of the following singlecolumn fixed bed processes and corresponding cross-current schemes: (1) batch chromatography, (2) batch chromatography with an integrated solvent removal unit, (3) mixed-recycle steady state recycling chromatography (SSR), and (4) mixed-recycle steady state recycling chromatography with solvent removal from fresh feed, recycle fraction, or column feed (SSR–SR). The method is based on the equilibrium theory of chromatography with an assumption of negligible mass transfer resistance and axial dispersion. The design criteria are given in general, dimensionless form that is formally analogous to that applied widely in the so called triangle theory of counter-current multi-column chromatography. Analytical design equations are derived for binary systems that follow competitive Langmuir adsorption isotherm model. For this purpose, the existing analytic solution of the ideal model of chromatography for binary Langmuir mixtures is completed by deriving missing explicit equations for the height and location of the pure first component shock in the case of a small feed pulse. It is thus shown that the entire chromatographic cycle at the column outlet can be expressed in closed-form. The developed design method allows predicting the feasible range of operating parameters that lead to desired product purities. It can be applied for the calculation of first estimates of optimal operating conditions, the analysis of process robustness, and the early-stage evaluation of different process alternatives. The design method is utilized to analyse the possibility to enhance the performance of conventional SSR chromatography by integrating it with a solvent removal unit. It is shown that the amount of fresh feed processed during a chromatographic cycle and thus the productivity of SSR process can be improved by removing solvent. The maximum solvent removal capacity depends on the location of the solvent removal unit and the physical solvent removal constraints, such as solubility, viscosity, and/or osmotic pressure limits. Usually, the most flexible option is to remove solvent from the column feed. Applicability of the equilibrium design for real, non-ideal separation problems is evaluated by means of numerical simulations. Due to assumption of infinite column efficiency, the developed design method is most applicable for high performance systems where thermodynamic effects are predominant, while significant deviations are observed under highly non-ideal conditions. The findings based on the equilibrium theory are applied to develop a shortcut approach for the design of chromatographic separation processes under strongly non-ideal conditions with significant dispersive effects. The method is based on a simple procedure applied to a single conventional chromatogram. Applicability of the approach for the design of batch and counter-current simulated moving bed processes is evaluated with case studies. It is shown that the shortcut approach works the better the higher the column efficiency and the lower the purity constraints are.

Conditions and practices in the commercialisation of innovations in wood industry

The report 'Conditions and practices in the commercialisation of innovation in wood industry' has been written as a part of the Wood Academy project. The report analyses the commercialisation conditions and practices of wood industry by utilising product categorisation based on a conceptual schema which combines the aspects of the transfer of the procession of utility and the degree of form/service utility (or value-added) created or provided by the company. Open innovation approaches help to perceive the possible new product and service innovations as well as the new business models and earning logics in the industry. The report also contains brief company cases to demonstrate theory-to-practice and showcase company examples from successful Finnish companies.

Customer-driven service product development

This thesis studies customer-driven service product development and how to manage customer involvement in the service product development process. The theory part of this thesis is a literature review of the prior studies and the thesis also includes empirical evidence in the form of a case study about ABB.

From Unspecific Quenching to Specific Signaling: Functional GTPase Assays Utilizing Quenching Resonance Energy Transfer (QRET) Technology

The aim of the work presented in this study was to demonstrate the wide applicability of a single-label quenching resonance energy transfer (QRET) assay based on time-resolved lanthanide luminescence. QRET technology is proximity dependent method utilizing weak and unspecific interaction between soluble quencher molecule and lanthanide chelate. The interaction between quencher and chelate is lost when the ligand binds to its target molecule. The properties of QRET technology are especially useful in high throughput screening (HTS) assays. At the beginning of this study, only end-point type QRET technology was available. To enable efficient study of enzymatic reactions, the QRET technology was further developed to enable measurement of reaction kinetics. This was performed using proteindeoxyribonuclei acid (DNA) interaction as a first tool to monitor reaction kinetics. Later, the QRET was used to study nucleotide exchange reaction kinetics and mutation induced effects to the small GTPase activity. Small GTPases act as a molecular switch shifting between active GTP bound and inactive GDP bound conformation. The possibility of monitoring reaction kinetics using the QRET technology was evaluated using two homogeneous assays: a direct growth factor detection assay and a nucleotide exchange monitoring assay with small GTPases. To complete the list, a heterogeneous assay for monitoring GTP hydrolysis using small GTPases, was developed. All these small GTPase assays could be performed using nanomolar protein concentrations without GTPase pretreatment. The results from these studies demonstrated that QRET technology can be used to monitor reaction kinetics and further enable the possibility to use the same method for screening.