Ultrafiltration of pulp mill bleaching effluents

Main objective of this research was to find suitable polymeric ultrafiltration membranes with high retentions, good capacities and low fouling tendencies for the E2- and EP-effluent ultrafiltration. Purpose was to treat alkaline bleaching effluents with ultrafiltration in a way that permeates of the filtrations could be recycled back to process and the consumption of fresh water in the pulp mill could be reduced significantly. In the theoretical part of this work the challenges set by the pulp and paper indus-try processes for membranes were examined. An overview of the membrane tech-nology in the pulp industry was also provided. In addition process conditions in the chemical pulp bleaching and properties of bleaching effluents were discussed in literature study. In experimental part the E2- and EP-stage bleaching effluents from Stora Enso Imatra kraft pulp mill were ultrafiltered with CR250- and CR200-filters. Suitable membranes for ultrafiltration were chosen after screening experiments. Concentra-tion experiment was made for the E2-effluent in order to estimate water saving potential. The E2-effluent was finally ultrafiltered in the pulp mill in order to test the feasibility of ultrafiltration in a real industrial environment. Good membrane for the EP-effluent ultrafiltration based on the EP-screening ex-periments was polyethersulfone membrane UP020 with cut-off value of 20 000 Da. Polysulfone membrane UFX05 with cut-off value of 5 000 Da was promising membrane for the ultrafiltration of the E2-effluent. Based on the concentration filtration of the E2-effluent with UFX05 membrane the water saving potential could be 2.2 m3/Adt for the industrial scale ultrafiltration process. Retention re-sults, such as average COD retention of 60 %, from the trial filtration at the pulp mill with UFX05 membrane were modest compared to the screening experiments, where average COD retention was 75 %. Therefore tighter ultrafiltration mem-branes should be tested for the ultrafiltration of the E2-effluent. The UP020 mem-brane seemed to be suitable for the ultrafiltration of the EP-effluent however con-centration and pilot scale ultrafiltration experiments are needed to verify this.

Transoperative refusion: a simple and safe method in emergency surgery

The objective is to reinforce the importance of blood reinfusion as a cheap, safe and simple method, which can be used in small hospitals, especially those in which there is no blood bank. Moreover, even with the use of devices that perform the collection and filtration of blood, more recent studies show that the cost-benefit ratio is much better when autologous transfusion is compared with blood transfusions, even when there is injury to hollow viscera and blood contamination. It is known that the allogeneic blood transfusion carries a number of risks to patients, among them are the coagulation disorders mediated by excess enzymes in the conserved blood, and deficiency in clotting factors, mainly the Factor V, the proacelerin. Another factor would be the risk of contamination with still unknown pathogens or that are not investigated during screening for selection of donors, such as the West Nile Fever and Creutzfeldt-Jacob, better known as "Mad Cow" disease. Comparing both methods, we conclude that blood autotransfusion has numerous advantages over heterologous transfusion, even in large hospitals. We are not against blood transfusions, just do not agree that the patient's own blood is discarded without making sure there will be enough blood in stock to get him out of the hemorrhagic shock.

Application of capillary electrophoretic methods for determining carbohydrates and aliphatic carboxylic acids formed during wood processing

Knowledge of the behaviour of cellulose, hemicelluloses, and lignin during wood and pulp processing is essential for understanding and controlling the processes. Determination of monosaccharide composition gives information about the structural polysaccharide composition of wood material and helps when determining the quality of fibrous products. In addition, monitoring of the acidic degradation products gives information of the extent of degradation of lignin and polysaccharides. This work describes two capillary electrophoretic methods developed for the analysis of monosaccharides and for the determination of aliphatic carboxylic acids from alkaline oxidation solutions of lignin and wood. Capillary electrophoresis (CE), in its many variants is an alternative separation technique to chromatographic methods. In capillary zone electrophoresis (CZE) the fused silica capillary is filled with an electrolyte solution. An applied voltage generates a field across the capillary. The movement of the ions under electric field is based on the charge and hydrodynamic radius of ions. Carbohydrates contain hydroxyl groups that are ionised only in strongly alkaline conditions. After ionisation, the structures are suitable for electrophoretic analysis and identification through either indirect UV detection or electrochemical detection. The current work presents a new capillary zone electrophoretic method, relying on in-capillary reaction and direct UV detection at the wavelength of 270 nm. The method has been used for the simultaneous separation of neutral carbohydrates, including mono- and disaccharides and sugar alcohols. The in-capillary reaction produces negatively charged and UV-absorbing compounds. The optimised method was applied to real samples. The methodology is fast since no other sample preparation, except dilution, is required. A new method for aliphatic carboxylic acids in highly alkaline process liquids was developed. The goal was to develop a method for the simultaneous analysis of the dicarboxylic acids, hydroxy acids and volatile acids that are oxidation and degradation products of lignin and wood polysaccharides. The CZE method was applied to three process cases. First, the fate of lignin under alkaline oxidation conditions was monitored by determining the level of carboxylic acids from process solutions. In the second application, the degradation of spruce wood using alkaline and catalysed alkaline oxidation were compared by determining carboxylic acids from the process solutions. In addition, the effectiveness of membrane filtration and preparative liquid chromatography in the enrichment of hydroxy acids from black liquor was evaluated, by analysing the effluents with capillary electrophoresis.

Acidic dissolution of iron oxides and regeneration of a ceramic filter medium

The dewatering of iron ore concentrates requires large capacity in addition to producing a cake with low moisture content. Such large processes are commonly energy intensive and means to lower the specific energy consumption are needed. Ceramic capillary action disc filters incorporate a novel filter medium enabling the harnessing of capillary action, which results in decreased energy consumption in comparison to traditional filtration technologies. As another benefit, the filter medium is mechanically and chemically more durable than, for example, filter cloths and can, thus, withstand harsh operating conditions and possible regeneration better than other types of filter media. In iron ore dewatering, the regeneration of the filter medium is done through a combination of several techniques: (1) backwashing, (2) ultrasonic cleaning, and (3) acid regeneration. Although it is commonly acknowledged that the filter medium is affected by slurry particles and extraneous compounds, published research, especially in the field of dewatering of mineral concentrates, is scarce. Whereas the regenerative effect of backwashing and ultrasound are more or less mechanical, regeneration with acids is based on chemistry. The chemistry behind the acid regeneration is, naturally, dissolution. The dissolution of iron oxide particles has been extensively studied over several decades but those studies may not necessarily be directly applicable in the regeneration of the filter medium which has undergone interactions with the slurry components. The aim of this thesis was to investigate if free particle dissolution indeed correlates with the regeneration of the filter medium. For this purpose, both free particle dissolution and dissolution of surface adhered particles were studied. The focus was on acidic dissolution of iron oxide particles and on the study of the ceramic filter medium used in the dewatering of iron ore concentrates. The free particle dissolution experiments show that the solubility of synthetic fine grained iron oxide particles in oxalic acid could be explained through linear models accounting for the effects of temperature and acid concentration, whereas the dissolution of a natural magnetite is not so easily explained by such models. In addition, the kinetic experiments performed both support and contradict the work of previous authors: the suitable kinetic model here supports previous research suggesting solid state reduction to be the reaction mechanism of hematite dissolution but the formation of a stable iron oxalate is not supported by the results of this research. Several other dissolution mechanisms have also been suggested for iron oxide dissolution in oxalic acid, indicating that the details of oxalate promoted reductive dissolution are not yet agreed and, in this respect, this research offers added value to the community. The results of the regeneration experiments with the ceramic filter media show that oxalic acid is highly effective in removing iron oxide particles from the surface of the filter medium. The dissolution of those particles did not, however, exhibit the expected behaviour, i.e. complete dissolution. The results of this thesis show that although the regeneration of the ceramic filter medium with acids incorporates the dissolution of slurry particles from the surface of the filter medium, the regeneration cannot be assessed purely based upon free particle dissolution. A steady state, dependent on temperature and on the acid concentration, was observed in the dissolution of particles from the surface even though the limit of solubility of free iron oxide particles had not been reached. Both the regeneration capacity and efficiency, with regards to the removal of iron oxide particles, was found to be temperature dependent, but was not affected by the acid concentration. This observation further suggests that the removal of the surface adhered particles does not follow the dissolution of free particles, which do exhibit a dependency on the acid concentration. In addition, changes in the permeability and in the pore structure of the filter medium were still observed after the bulk concentration of dissolved iron had reached a steady state. Consequently, the regeneration of the filter medium continued after the dissolution of particles from the surface had ceased. This observation suggests that internal changes take place at the final stages of regeneration. The regeneration process could, in theory, be divided into two, possibly overlapping, stages: (1) dissolution of surface-adhered particles, and (2) dissolution of extraneous compounds from within the pore structure. In addition to the fundamental knowledge generated during this thesis, tools to assess the effects of parameters on the regeneration of the ceramic filter medium are needed. It has become clear that the same tools used to estimate the dissolution of free particles cannot be used to estimate the regeneration of a filter medium unless only a robust characterisation of the order of regeneration efficiency is needed.

Puuperäisten biomassahydrolysaattien likaamien membraanien pesu

Tässä diplomityössä tutkittiin biomassahydrolysaatilla liattujen ultrasuodatusmembraanien pesua. Työn kirjallisuusosassa käsitellään membraanien likaantumista ja pesua, puuperäistä biomassahydrolysaattia sekä biomassahydrolysaatin suodatusta membraaneilla ja membraanien karakterisointia. Kokeellisessa osassa tutkittiin pesuaineiden vaikutusta koivuhydrolysaatilla liattujen membraanien peseytyvyyteen. Käytetyt ultrasuodatusmembraanit olivat Alfa Lavalin UFX5 ja ETNA01PP. Membraanien pesussa käytettiin Ecolabin entsymaattisia P3-ultrasil 53 ja P3-ultrasil 67 pesuaineita yhdessä emäksisen P3-ultrasil 69 pesuaineen kanssa sekä hapanta P3-ultrasil 75 pesuainetta. Lisäksi emäksisiä P3-ultrasil 110, P3-ultrasil 112 ja P3-ultrasil 115 pesuaineita. Emäksisten pesujen tehokkuutta vertailtiin pelkällä natriumhydroksidilla tehtyyn pesuun. Membraanien likaantumista arvioitiin mittaamalla puhtaan veden vuota ennen ja jälkeen likaantumissuodatuksen ja laskemalla niiden vuoarvojen erotus. Samalla tavalla arvioitiin pesuaineiden vaikutusta membraanin peseytyvyyteen. Lisäksi peseytyvyyttä arvioitiin FTIR–analyyseillä, kontaktikulmamittauksilla ja membraanin sisältämän ligniinin värjäyksellä. Tutkimuksissa havaittiin, että koivuhydrolysaatilla liatuille UFX5 membraaneille vesivuon sekä FTIR–spektrin muuttumisen perusteella sopii parhaiten emäksisen ja happaman pesuaineen kaksivaiheinen pesu. Kontaktikulman palautumisen perusteella parhaiten sopi pelkällä emäksisellä P3-Ultrasil 115 tehty pesu. Ligniiniä parhaiten, mikroskooppiin liitetyllä kameralla otettujen kuvien perusteella, poisti entsymaattinen P3-ultrasil 67, mutta tämä samalla modifioi membraanin pintaa. Tässä tutkimuksessa havaittiin, että emäksinen ja entsymaattinen pesuaine pesevät melko hyvin koivuhydrolysaatilla liattuja membraaneja. Lisäksi havaittiin, että ligniini tunkeutuu suodatuksissa membraanin sisään, joten pelkkä pesuaineen kierrättäminen laitteistossa ei riitä vaan tarvitaan paineellista pesua.

Biolietteen kuiva-ainepitoisuuden parantaminen elektro-kuivauksen avulla

Tässä työssä tutkittiin sähkön käyttömahdollisuuksia metsäteollisuuden jäteveden-puhdistamolla syntyvän biolietteen kuivauksessa. Lisäksi selvityksen kohteena olivat lietteen sähkökuivaukseen vaikuttavat tekijät. Työn kirjallisessa osassa perehdyttiin lietteiden syntyyn jätevedenpuhdistamolla sekä lietteiden ominaisuuksiin. Työssä tutustuttiin myös lietteiden käsittelyyn ja siinä käytettäviin tekniikoihin. Ennen työn kokeellista osaa esiteltiin sähkökuivauksen periaate sekä sähkökuivaukselle aiemmin tehtyjä tutkimuksia ja niistä saatuja kokemuksia. Myös tuotteistetut elektrokuivauksen sovellukset olivat osa työtä. Kokeellisessa osassa keskityttiin varsinaisiin sähkökuivauskokeisiin. Tutkimukset suoritettiin suodatuskokein, jotka toteutettiin imuun perustuvalla Büchner-suodattimella sekä painesuodattimella. Kokeissa tutkittiin tasavirran, virran pulssituksen ja vaihtovirran vaikutusta metsäteollisuuden primääri- ja biolietteeseen. Tasavirtatutkimuksissa sähkövirtaa johdettiin lietteeseen suodatuksen aikana, kun taas vaihtovirtaa testattaessa liete käsiteltiin ensin sähköllä ja suodatettiin erikseen. Suodatuskokeiden lisäksi tutkimuksissa tarkkailtiin lietteiden kuiva-ainepitoisuuksia, redox-potentiaalia, lämpötilaa, pH:ta ja sähkönjohtokykyä. Lietteitä tutkittiin myös tuhkapitoisuuden suhteen sekä suoritettiin solututkimuksia fluoresenssilukijan avulla. Työn laboratoriotutkimukset osoittivat sähkön vaikuttavan selkeästi biolietteen ve-denerotuskykyyn: sähkö nopeutti lietteen suodatusta parhaimmillaan yli 70 %. Säh-kökuivauksella lietteen kuiva-ainepitoisuudet pysyivät samoina, mutta suodatus nopeutui ja suodatusajat jopa puolittuivat. Myös lietteen sähkönjohtokyky kasvoi sähkökäsittelyn aikana, mikä viittasi veden vapautumiseen solujen sisältä. Lietteen kunto ja ominaisuudet, polymeeri, sekoitus sekä sähkökäsittelyn parametrit olivat tärkeässä asemassa sähkökuivauksen onnistumisen kannalta.

Maidon ja heran mikrosuodatus

Työssä selvitettiin uudenaikaisten polymeerikalvojen soveltuvuutta maidon sekä heran mikrosuodatukseen. Kirjallisessa osassa perehdyttiin maidon ja heran koostumuksiin, mikrobikantoihin sekä erilaisiin maidon sekä heran rasvanpoisto- ja puhdistusmenetelmiin. Tämän lisäksi käsiteltiin mikrosuodatusmenetelmiä sekä niiden käyttöä heran ja maidon käsittelyssä meijeriteollisuudessa. Kokeellisessa osassa verrattiin kahdella eri suodatuslaitteistolla keraami- ja polymeerikalvojen suodatusominaisuuksia separoidun raakamaidon sekä heran poikkivirtausmikrosuodatuksessa. Tavoitteena oli erottaa suodatettavista liuoksista mikrobit sekä jäännösrasva ja tuottaa puhdasta, proteiinipitoista maitoa / heraa. Koeajoissa otetuista näytteistä analysoitiin ainesosakoostumus sekä mikrobipitoisuudet. Tuloksista määritettiin retentioarvot ja näiden perusteella vertailtiin polymeeri- ja keraamikalvojen erotustehokkuutta. Lisäksi kalvojen toimivuutta arvioitiin vuoarvojen avulla. Raakamaidon suodatuksissa polymeerikalvot pidättivät täydellisesti tai lähes täydellisesti jäännösrasvan ja mikrobit, mutta myös kaseiiniproteiinin. Tästä syystä yksikään polymeerikalvoista ei sovellu puhtaan maidon suodatukseen. Keraamikalvot soveltuvat tähän selkeästi paremmin ja yksikään toinen testatuista kalvoista ei päässyt samalle tasolle meijeriteollisuudessa jo käytössä olevan Membralox 1,4 μm -keraamikalvon kanssa. Heran suodatuksissa polymeerikalvot pidättivät täydellisesti tai lähes täydellisesti rasvan ja mikrobit, mutta keraamikalvo päästi huomattavasti enemmän haluttuja proteiineja permeaattiin. Membralox 0,8 μm -keraamikalvo pidätti täydellisesti mikrobit, mutta päästi jonkin verran jäännösrasvaa permeaattiin. Näin ollen kalvovalinta on kompromissi permeaatin puhtauden ja proteiinin saannon välillä. Keraamikalvojen vuohäviöt olivat merkittävästi pienemmät kuin polymeerikalvoilla molempien syöttöliuosten kanssa. Lisäksi keraamikalvojen puhdistus oli huomattavasti nopeampaa ja helpompaa. Tästä syystä keraamiset kalvot soveltuvat polymeerisiä paremmin maidon ja heran mikrosuodatukseen.

Puuhydrolysaatin esikäsittely foulaantumisen vähentämiseksi ultrasuodatuksessa

Tässä kandidaatintyössä tutkittiin, voidaanko puuhydrolysaatin esikäsittelyllä vähentää sen ultrasuodatuksen aikana esiintyvää kalvojen foulaantumista. Kokeellinen osa rajattiin koskemaan hydrolysaatin käsittelyä lakkaasientsyymillä, flokkulanteilla, kitosaanilla sekä adsorbentin ja lakkaasientsyymin yhdistelmällä. Esikäsittelyjen tavoitteena oli poistaa tai hajottaa hydrolysaatin sisältämää ligniiniä. Käsittelyjen teho testattiin suodattamalla eri tavoin käsiteltyä hydrolysaattia laboratoriokokeissa. Kokeissa adsorbentin ja lakkaasientsyymin yhdistelmäkäsittely osoittautui parhaaksi. Suodatuskapasiteetti parani ja foulaantuminen väheni verrattuna esikäsittelemättömän hydrolysaatin suodatukseen. Ligniiniä poistui käsittelyssä, kuten tavoitteena oli. Suodatuksessa kuitenkin edelleen tapahtui foulaantumista ja esikäsittelyn tehoa tulisi siksi vielä parantaa. Myös esikäsittely lakkaasientsyymillä paransi suodatuskapasiteettia ja vähensi foulaantumista, mutta vähemmän kuin entsyymi-adsorbenttikäsittely.

Myxosporidiosis in intensively-reared Piaractus mesopotamicus: Histopathological diagnosis by means of Ziehl-Neelsen staining

Samples of different organs from intensively-reared Piaractus mesopotamicus were collected and processed using routine histological techniques in order to produce thin sections for staining with hematoxylin-eosin and with the Ziehl-Neelsen method. Through examination under an optical microscope, myxosporidians of the genera Henneguya sp. and Myxobolus sp. were identified, respectivelyin the gills and kidneys of P. mesopotamicus. Plasmodia with immature spores of Henneguya sp. were located along the secondary lamellae, with total length of 30.45±4.84µm and width of 3.52±0.33µm. Spores of Myxobolus sp. were located in the kidneys, with total length of 8.94±0.82µm and width of 5.59±0.39µm. Histopathological analysis of the gills showed plasmodia containing spores of Henneguya sp., at intralamellar and intravascular localities, at different stages of development. Spores of Myxobolus sp. were identified in the kidneys, in the peritubular region and in the interstices and glomerulus, surrounded by melanomacrophages. Focal hemorrhage was recorded in a few cases. Ziehl-Neelsen staining allowed to identify particular features of the spores and facilitated biometry and enabled classification in comparison with hematoxylin-eosin, thus demonstrating its usefulness for histopathological diagnosis of the parasitosis.

Extraction of polymeric galactoglucomannans from spruce wood by pressurized hot water

The major type of non-cellulosic polysaccharides (hemicelluloses) in softwoods, the partly acetylated galactoglucomannans (GGMs), which comprise about 15% of spruce wood, have attracted growing interest because of their potential to become high-value products with applications in many areas. The main objective of this work was to explore the possibilities to extract galactoglucomannans in native, polymeric form in high yield from spruce wood with pressurised hot-water, and to obtain a deeper understanding of the process chemistry involved. Spruce (Picea abies) chips and ground wood particles were extracted using an accelerated solvent extractor (ASE) in the temperature range 160 – 180°C. Detailed chemical analyses were done on both the water extracts and the wood residues. As much as 80 – 90% of the GGMs in spruce wood, i.e. about 13% based on the original wood, could be extracted from ground spruce wood with pure water at 170 – 180°C with an extraction time of 60 min. GGMs comprised about 75% of the extracted carbohydrates and about 60% of the total dissolved solids. Other substances in the water extracts were xylans, arabinogalactans, pectins, lignin and acetic acid. The yields from chips were only about 60% of that from ground wood. Both the GGMs and other non-cellulosic polysaccharides were extensively hydrolysed at severe extraction conditions when pH dropped to the level of 3.5. Addition of sodium bicarbonate increased the yields of polymeric GGMs at low additions, 2.5 – 5 mM, where the end pH remained around 3.9. However, at higher addition levels the yields decreased, mainly because the acetyl groups in GGMs were split off, leading to a low solubility of GGMs. Extraction with buffered water in the pH range 3.8 – 4.4 gave similar yields as with plain water, but gave a higher yield of polymeric GGMs. Moreover, at these pH levels the hydrolysis of acetyl groups in GGMs was significantly inhibited. It was concluded that hot-water extraction of polymeric GGMs in good yields (up to 8% of wood) demands appropriate control of pH, in a narrow range about 4. These results were supported by a study of hydrolysis of GGM at constant pH in the range of 3.8 – 4.2 where a kinetic model for degradation of GGM was developed. The influence of wood particle size on hot-water extraction was studied with particles in the range of 0.1 – 2 mm. The smallest particles (< 0.1 mm) gave 20 – 40% higher total yield than the coarsest particles (1.25 – 2 mm). The difference was greatest at short extraction times. The results indicated that extraction of GGMs and other polysaccharides is limited mainly by the mass transfer in the fibre wall, and for coarse wood particles also in the wood matrix. Spruce sapwood, heartwood and thermomechnical pulp were also compared, but only small differences in yields and composition of extracts were found. Two methods for isolation and purification of polymeric GGMs, i.e. membrane filtration and precipitation in ethanol-water, were compared. Filtration through a series of membranes with different pore sizes separated GGMs of different molar masses, from polymers to oligomers. Polysaccharides with molar mass higher than 4 kDa were precipitated in ethanol-water. GGMs comprised about 80% of the precipitated polysaccharides. Other polysaccharides were mainly arabinoglucuronoxylans and pectins. The ethanol-precipitated GGMs were by 13C NMR spectroscopy verified to be very similar to GGMs extracted from spruce wood in low yield at a much lower temperature, 90°C. The obtained large body of experimental data could be utilised for further kinetic and economic calculations to optimise technical hot-water extractionof softwoods.

Solids removal in pyrolysis

Pyrolysis is a process for turning biomass into liquid fuel. The process consists of heating the biomass in inert conditions and quenching the resulting vapors into oil. The oil has many potential uses, such as heating fuel in peak heating plants. In order to broaden the application base and improve the quality of the oil, solids removal has to be addressed. The solids may also increase the probability of plugging in downstream equipment. The purpose of this research was to gain an understanding of the formation of solids in the pyrolysis process and to assess options for reducing the solid content of the oil. From literature it is known that the solids can be removed either by hot vapor filtration, liquid treatment or multiple cyclones. Hot vapor filtration decreases yield, but improves the stability of the oil while simultaneously removing solids and ash. Liquid treatment techniques are good for removing large particles but involve losses of pyrolysis liquid. Cyclones are a traditional robust technique used regularly in pyrolysis. In the experimental part of this thesis, a 2 MWfuel pyrolysis setup with 2 cyclones in series was operated and monitored. Solid and liquid samples were collected from various parts of the process for further examination. Sampling and sample treatment techniques were developed. The chemical properties of the pyrolysis char were also analyzed and assessed as a function of reactor temperature and fluidizing velocity. By measuring the particle size distributions it was noticed that there were much smaller particles collected from the second cyclone than fed into pyrolysis. The solids in the pyrolysis oil were even smaller. This was most likely caused by attrition and shrinkage. Due to better separation efficiency of the cyclones in large particles, excess attrition should be avoided.

Tekniset vaatimukset huonekohtaisen ilmanpuhdistimen valitsemiseksi sisäilmaongelmaisessa kohteessa

Tässä työssä tarkastellaan rakennusten sisäilman laatua heikentäviä epäpuhtauksia sekä niiden suodattamiseen huonekohtaisissa ilmanpuhdistimissa käytettäviä suodatustekniikoita. Tavoitteena oli selvittää ilmanpuhdistimien soveltuvuus sisäilmaongelmista kärsiviin kohteisiin. Ilmanpuhdistimia testattiin laboratoriossa ja testitulosten perusteella arvioitiin niiden teknisiä ominaisuuksia. Lisäksi laadittiin valintakriteerit huonekohtaisen ilmanpuhdistimen valitsemiseksi sisäilmaongelmaisessa kohteessa. Diplomityö tehtiin Helsingin kaupungin kiinteistöviraston Tilakeskuksessa vastaamaan tarpeeseen selvittää ilmanpuhdistimien teknisiä ominaisuuksia. Laboratoriotesteissä laitteista löydettiin eroavaisuuksia, ja tulosten perusteella laitteet asetettiin paremmuusjärjestykseen. Työssä suoritetun tutkimuksen perusteella voidaan todeta, että nykyisin markkinoilla olevat huonekohtaiset ilmanpuhdistimet soveltuvat pääosin melko heikosti sisäilmaongelmien ratkaisemiseen. Tähän syynä on erityisesti laitteiden aiheuttama suuri melupäästö.

Identification of research trends in the field of separation processes. Application of epidemiological model, citation analysis, text mining, and technical analysis of the financial markets

Choice of industrial development options and the relevant allocation of the research funds become more and more difficult because of the increasing R&D costs and pressure for shorter development period. Forecast of the research progress is based on the analysis of the publications activity in the field of interest as well as on the dynamics of its change. Moreover, allocation of funds is hindered by exponential growth in the number of publications and patents. Thematic clusters become more and more difficult to identify, and their evolution hard to follow. The existing approaches of research field structuring and identification of its development are very limited. They do not identify the thematic clusters with adequate precision while the identified trends are often ambiguous. Therefore, there is a clear need to develop methods and tools, which are able to identify developing fields of research. The main objective of this Thesis is to develop tools and methods helping in the identification of the promising research topics in the field of separation processes. Two structuring methods as well as three approaches for identification of the development trends have been proposed. The proposed methods have been applied to the analysis of the research on distillation and filtration. The results show that the developed methods are universal and could be used to study of the various fields of research. The identified thematic clusters and the forecasted trends of their development have been confirmed in almost all tested cases. It proves the universality of the proposed methods. The results allow for identification of the fast-growing scientific fields as well as the topics characterized by stagnant or diminishing research activity.

Indoor air quality at a waste incineration plant in Finland

Waste has been incinerated for energy utilization for more than a hundred years, but the harmful emissions emitted from the incineration plants did not begin to cause concern until the 1980s. Many plants were shutdown and the waste incineration plant in Kyläsaari Helsinki was one of them. In later years, new landfill regulations have increased the interest in waste incineration. During the last year, four new plants were taken into operation in Finland, Westenergy in Vaasa among them. The presence of dust has been observed indoors at Westenergy waste incineration plant. Dust is defined as particles with a diameter above 10 μm, while fine particles have a diameter smaller than 2.5 μm, ultrafine under 0.1 μm and nanoparticles under 0.05 μm. In recent years, the focus of particle health research has been changed to investigate smaller particles. Ultrafine particles have been found to be more detrimental to health than larger particles. Limit values regulating the concentrations of ultrafine particles have not been determined yet. The objective of this thesis was to investigate dust and particles present inside the Westenergy waste incineration facility. The task was to investigate the potential pollutant sources and to give recommendations of how to minimize the presence of dust and particles in the power plant. The total particle number concentrations and size distributions where measured at 15 points inside the plant with an Engine Exhaust Particle Sizer (EEPS) Spectrometer. The measured particles were mainly in the ultrafine size range. Dust was only visually investigated, since the main purpose was to follow the dust accumulation. The measurement points inside the incineration plant were chosen according to investigate exposure to visitors and workers. At some points probable leakage of emissions were investigated. The measurements were carried out during approximately one month in March–April 2013. The results of the measurements showed that elevated levels of dust and particles are present in the indoor air at the waste incineration plant. The cleanest air was found in the control room, warehouse and office. The most polluted air was near the sources that were investigated due to possible leakage and in the bottom ash hall. However, the concentrations were near measured background concentrations in European cities and no leakage could be detected. The high concentrations were assumed to be a result of a lot of dust and particles present on surfaces that had not been cleaned in a while. The main source of the dust and particles present inside the waste incineration plant was thought to be particles and dust from the outside air. Other activities in the area around the waste incineration facility are ground work activities, stone crushing and traffic, which probably are sources of particle formation. Filtration of the outside air prior entering the facility would probably save personnel and visitors from nuisance and save in cleaning and maintenance costs.