Kakun rakenteen vaikutus pesutulokseen

Tässä työssä tutkittiin suodatukseen vaikuttavien tekijöiden vaikutusta suodatuksessa syntyvän kakun ominaisuuksiin sekä kakun ominaisuuksien vaikutusta syrjäytyspesun tehokkuuteen. Lisäksi määritettiin tärkeimmät suodatusparametrit sekä niiden riippuvuudet suodatusolosuhteista. Toissijaisena tavoitteena oli lisäksi tutkia, miten suodatusolosuhteita ja suodatettavan lietteen ominaisuuksia muuttamalla voidaan vaikuttaa suodatusjakson kestoon. Työn kirjallisuusosassa käsiteltiin aluksi yleisesti kiintoaineen erotusta nesteestä. Tämän jälkeen käsiteltiin yleisimmät suodatustekniikat ja tarkasteltiin yksityiskohtaisemmin painesuodatusta ja varsinkin syntyvän kakun rakenteeseen vaikuttavia tekijöitä. Lopuksi käytiin läpi kakulle suodatuksen jälkeen suoritettavat jälkikäsittelymenetelmät ja selvitettiin varsinkin syrjäytyspesun tehokkuuteen vaikuttavia tekijöitä tarkemmin. Kokeellisessa osassa tehtiin koesuodatuksia lietteellä joka sisälsi hienojakoista pigmenttiä. Koesuodatukset tehtiin kahdella eri kankaalla panostoimisella piston press- laboratoriopainesuodattimella johon oli liitetty tiedonkeruuohjelmisto, joka keräsi tiedostoon paineet suodatuskammiossa, kankaan alapuolella ja työsylinterin syöttölinjassa sekä lisäksi männän korkeuden, lietteen lämpötilan ja suodosvaakalukeman. Lietteiden ominaisuuksia seurattiin analysoimalla niiden kiintoainepitoisuuksia, kloridipitoisuuksia, z-potentiaaleja ja partikkelikokojakau-mia siten että jokaisessa suodatuksessa käytetyn lietteen ominaisuudet olivat tiedossa. Suodatusten jälkeen syntyneistä kakuista määritettiin kiintoaine- sekä joissain tapauksissa myös kloridipitoisuudet. Suodatus- ja puristuspaineiden havaittiin vaikuttavan kakkujen huokoisuuksiin ja ominaisvastuksiin selvästi, joskin muutokset olivat melko pieniä. Vaikutus näkyi selvästi myös suodatusten kestoissa ja muutosten havaittiin olevan merkittävän suuruisia. Myös lietteen pH:n havaittiin vaikuttavan merkitsevästi suodatusten kestoihin ja kakkujen ominaisuuksiin. Pesutuloksen ja kakun ominaisuuksien välille löydettiin riippuvuus heikoksi jääneestä pesutuloksesta huolimatta. Myös koesuodatuksissa käytettyjen kankaiden välillä havaittiin selviä eroavaisuuksia.

Factors Affecting Filterability

In this thesis the factors affecting lime mud filterability were studied. In the literature part there is information about recausticizing process, lime mud properties and filterability, and general filtration theory. In the experimental part the properties of lime mud particles and the properties of lime mud filter cake were investigated and the behavior of lime mud precoat was studied. The experiments were also carried out with R-PCC (rhombohedral precipitated calcium carbonate). The filtration and precoat studies were performed with a laboratory scale pressure filter. The pressure differences used were between 0.25-1.50 bars. Six different lime mud samples with varying amount of impurities and two R-PCC samples were used in the experiments. The average specific cake resistance of different lime mud samples varied quite extensively. The most influential factor affecting the lime mud filterability and dry solids content was found to be silica content. As the lime mud contained silica, the average specific cake resistance was high and the lime mud dryness was low. If the lime mud samples containing silica were not taken into account, the smaller the mean particle size, the higher the average specific cake resistance of the lime mud. The R-PCC had also a high average specific cake resistance, which was because of small particle size. In addition, the pressure difference affected the average specific cake resistance of some lime mud samples. In those cases lime mud was compressible material. During the precoat experiments the lime mud samples having the largest mean particle sizes, compressed. However, the average specific cake resistances of the filtration and precoat part were approximately the same magnitude. A brief displacement by air did not affect the behavior of the precoat. Instead, vibration and a brief but relatively great change in pressure difference had a slight influence.

Höyryn käyttö suodinkakun pesussa ja kuivauksessa

Työssä käsitellään suodinkakkujen kuivapitoisuuksien muuttumista, kun kuivauksessa käytetään paineilman sijasta kylläistä höyryä.

Water circulations for effective bleaching of high-brightness mechanical pulps

The amount of water available is usually restricted, which leads to a situation where a complete understanding of the process, including water circulations and the influence of water components, is essential. The main aim of this thesis was to clarify the possibilities for the efficient use of residual peroxide by means of water circulation rearrangements. Rearranging water circulations and the reduction of water usage may cause new problems, such as metal induced peroxide decomposition that needs to be addressed. This thesis introduces theoretical methods of water circulations to combine two variables; effective utilization of residual peroxide and avoiding manganese in the alkaline peroxide bleaching stage. Results are mainly based on laboratory and mill site experiments concerning the utilization of residual peroxide. A simulation model (BALAS) was used to evaluate the manganese contents and residual peroxide doses. It was shown that with optimum recirculation of residual peroxide the brightness can be improved or chemical costs can be decreased. From the scientific perspective, it was also very important to discover that recycled peroxide was more effective pre-bleaching agent compared to fresh peroxide. This can be due to the organic acids i.e. per acetic acid in wash press filtrate that have been formed in alkaline bleaching stage. Even short retention time was adequate and the activation of residual peroxide using sodium hydroxide was not necessary. There are several possibilities for using residual peroxide in practice regarding bleaching. A typical modern mechanical pulping process line consist of defibering, screening, a disc filter, a bleach press, high consistency (HC) peroxide bleaching and a wash press. Furthermore there usually is not a particular medium consistency (MC) pre-bleaching stage that includes additional thickening equipment. The most advisable way to utilize residual peroxide in this kind of process is to recycle the wash press filtrate to the dilution of disc filter pulp (low MC pre-bleaching stage). An arrangement such as this would be beneficial in terms of the reduced convection of manganese to the alkaline bleaching stage. Manganese originates from wood material and will be removed to the water phase already in the early stages of the process. Recycling residual peroxide prior to the disc filter is not recommended because of low consistencies. Regarding water circulations, the novel point of view is that, it would be beneficial to divide water circulations into two sections and the critical location for the division is the disc filter. Both of these two sections have their own priority. Section one before the disc filter: manganese removal. Section two after the disc filter: brightening of pulp. This division can be carried out if the disc filter pulp is diluted only by wash press filtrate before the MC storage tower. The situation is even better if there is an additional press after the disc filter, which will improve the consistency of the pulp. This has a significant effect on the peroxide concentration in the MC pre-bleaching stage. In terms of manganese content, it is essential to avoid the use of disc filter filtrate in the bleach press and wash press showers. An additional cut-off press would also be beneficial for manganese removal. As a combination of higher initial brightness and lower manganese content, the typical brightness increase varies between approximately 0.5 and 1% ISO units after the alkaline peroxide bleaching stage. This improvement does not seem to be remarkable, but as it is generally known, the final brightness unit is the most expensive and difficult to achieve. The estimation of cost savings is not unambiguous. For example in GW/TMP mill case 0.6% ISO units higher final brightness gave 10% savings in the costs of bleaching chemicals. With an hypothetical 200 000 ton annual production, this means that the mill could save in the costs of bleaching chemicals more than 400 000 euros per year. In general, it can be said that there were no differences between the behavior of different types of processes (GW, PGW, TMP and BCTMP). The enhancement of recycling gave a similar response in all cases. However, we have to remember that the utilization of residual peroxide in older mills depends a great deal on the process equipment, the amount of water available and existing pipeline connections. In summary, it can be said that processes are individual and the same solutions cannot be applied to all cases.

The influence of crystallization conditions on the filtration characteristics of sulphathiazole suspensions

Cooling crystallization is one of the most important purification and separation techniques in the chemical and pharmaceutical industry. The product of the cooling crystallization process is always a suspension that contains both the mother liquor and the product crystals, and therefore the first process step following crystallization is usually solid-liquid separation. The properties of the produced crystals, such as their size and shape, can be affected by modifying the conditions during the crystallization process. The filtration characteristics of solid/liquid suspensions, on the other hand, are strongly influenced by the particle properties, as well as the properties of the liquid phase. It is thus obvious that the effect of the changes made to the crystallization parameters can also be seen in the course of the filtration process. Although the relationship between crystallization and filtration is widely recognized, the number of publications where these unit operations have been considered in the same context seems to be surprisingly small. This thesis explores the influence of different crystallization parameters in an unseeded batch cooling crystallization process on the external appearance of the product crystals and on the pressure filtration characteristics of the obtained product suspensions. Crystallization experiments are performed by crystallizing sulphathiazole (C9H9N3O2S2), which is a wellknown antibiotic agent, from different mixtures of water and n-propanol in an unseeded batch crystallizer. The different crystallization parameters that are studied are the composition of the solvent, the cooling rate during the crystallization experiments carried out by using a constant cooling rate throughout the whole batch, the cooling profile, as well as the mixing intensity during the batch. The obtained crystals are characterized by using an automated image analyzer and the crystals are separated from the solvent through constant pressure batch filtration experiments. Separation characteristics of the suspensions are described by means of average specific cake resistance and average filter cake porosity, and the compressibilities of the cakes are also determined. The results show that fairly large differences can be observed between the size and shape of the crystals, and it is also shown experimentally that the changes in the crystal size and shape have a direct impact on the pressure filtration characteristics of the crystal suspensions. The experimental results are utilized to create a procedure that can be used for estimating the filtration characteristics of solid-liquid suspensions according to the particle size and shape data obtained by image analysis. Multilinear partial least squares regression (N-PLS) models are created between the filtration parameters and the particle size and shape data, and the results presented in this thesis show that relatively obvious correlations can be detected with the obtained models.

Solo contaminado com cádmio: extratibilidade do metal e cinética química de degradação da matéria orgânica de torta de filtro

The chemical kinetics of sugarcane filter cake (FC) organic matter degradation at rates (0, 40, 80, and 120 t ha-1) in non-contaminated and different degrees of cadmium-contaminated Oxisol (0.19, 28, 56, 112 and 200 mg Cd kg-1) and DTPA-extractable Cd was studied. FC degradation was determined by quantifying CO2 emitted from soil samples during 72 days of incubation. DTPA-extractable Cd was performed after the incubation period. FC degradation was described by a two-stage equation of chemical kinetics. FC degradation rates were between 15 and 33%. Total CO2 emitted from FC declined with increasing degree in Cd-contamination and the DTPA-extractable Cd declined with FC rates.

Microscopic simulation of pigment coating consolidation

The control of coating layer properties is becoming increasingly important as a result of an emerging demand for novel coated paper-based products and an increasing popularity of new coating application methods. The governing mechanisms of microstructure formation dynamics during consolidation and drying are nevertheless, still poorly understood. Some of the difficulties encountered by experimental methods can be overcome by the utilisation of numerical modelling and simulation-based studies of the consolidation process. The objective of this study was to improve the fundamental understanding of pigment coating consolidation and structure formation mechanisms taking place on the microscopic level. Furthermore, it is aimed to relate the impact of process and suspension properties to the microstructure of the coating layer. A mathematical model based on a modified Stokesian dynamics particle simulation technique was developed and applied in several studies of consolidation-related phenomena. The model includes particle-particle and particle-boundary hydrodynamics, colloidal interactions, Born repulsion, and a steric repulsion model. The Brownian motion and a free surface model were incorporated to enable the specific investigation of consolidation and drying. Filter cake stability was simulated in various particle systems, and subjected to a range of base substrate absorption rates and system temperatures. The stability of the filter cake was primarily affected by the absorption rate and size of particles. Temperature was also shown to have an influence. The consolidation of polydisperse systems, with varying wet coating thicknesses, was studied using imposed pilot trial and model-based drying conditions. The results show that drying methods have a clear influence on the microstructure development, on small particle distributions in the coating layer and also on the mobility of particles during consolidation. It is concluded that colloidal properties can significantly impact coating layer shrinkage as well as the internal solids concentration profile. Visualisations of particle system development in time and comparison of systems at different conditions are useful in illustrating coating layer structure formation mechanisms. The results aid in understanding the underlying mechanisms of pigment coating layer consolidation. Guidance is given regarding the relationship between coating process conditions and internal coating slurry properties and their effects on the microstructure of the coating.

Outplanting performace of eucalyptus clonal cuttings produced in different containers and substrates

The objective of this work was to evaluate the outplanting growth of Eucalyptus grandis e E. saligna clones, produced by cuttings in tubes (50cm³) and in pressed blocks (40x60x07cm) - 175 cm³/ seedlings, with different substrates (BT - sugarcane bagasse+sugarcane filter cake; AR - carbonized rice hull + eucalyptus bark; TF - peat). The experiment was arranged in a randomized block design, in a 2x7 factorial (2 clones and 7 treatments), with four replicates with 25 plants. Survival was evaluated two months later. Plant growth was monitored through height and ground level diameter at 20, 40, 60, 120 and 180 days after outplanting. To evaluate the effect of the containers on stem and root biomass in both clones, 180 days after outplanting, the cuttings grown in BT substrate with fertilizer were selected. One plant per plot of each clone, grown in tubes and in pressed blocks was selected. The E. grandis and E. saligna cuttings grown in pressed blocks with sugarcane bagasse+sugarcane filter cake presented greater height and diameter after out planting. Both clones presented larger root, bark, log and branch biomass production in plants produced in the block system. Cuttings of E. saligna grown in pressed blocks showed 80% most wood biomass 180 days after outplanting, compared to that grown in tubes. In E. grandis, the differences in diameter and height, in function of the cutting production system, decreased along time, while in E. saligna these differences increased along the evaluation period.

Technology for sugarcane agroindustry waste reuse as granulated organomineral fertilizer

Aiming to evaluate the use of sugarcane industry waste such as byproducts from vinasse concentration process, it was assessed the organomineral fertilizer BIOFOM (concentrated vinasse, filter cake, boiler ash, soot from chimneys and supplemented with mineral fertilizers). The study included characterization and agronomic potential analysis of a test plant (corn), by noting the differences between mineral fertilizers and BIOFOM fertilization until 45 days after sowing. The technology traditionally used to produce BIOFOM was based on vinasse evaporation with high heat transfer coefficients. It was observed that the technology, which can be formulated according to the needs of any crop, could be used in many cases as mineral fertilizer. Therefore, the use of this organomineral fertilizer reduces waste generation of sugarcane industry.

Characterization of organic matter from composting of different residues by physicochemical and spectroscopic methods

Chemical and spectroscopic methods were used to characterize organic matter transformations during the composting process. Four different residue mixtures were studied: P1 - garden trimmings (GT) only, P2 - GT plus fresh cattle manure, P3 - GT plus orange pomace and P4 - GT plus filter cake. The thermophilic phase was not reached in PI compost, but the P2, P3 and P4 composts showed all three typical process phases. The thermophilic phase and CEC/C ratio stabilized after 90 days, while C/N ratio and the ash content stabilized after 60 days. The increasing E(4)/E(6) ratio indicated oxidation reactions occurring during the process in the material from P2, P3 and P4. The (13)C NMR and FTIR results suggested extraction of both pectin and lignin in the HA-like fraction. The CEC/C ratio, temperature and E(4)/E(6) ratio showed that within 90 days P2, P3 and P4 composts were humified. However, material from P1 did not show characteristics of humified compost. From these data, it is apparent that C/N ratio and ash content are not reliable methods for monitoring the composting process. (C) 2009 Elsevier Ltd. All rights reserved.

Modelagem e previsão da perda de injetividade em poços canhoneados

Waterflooding is a technique largely applied in the oil industry. The injected water displaces oil to the producer wells and avoid reservoir pressure decline. However, suspended particles in the injected water may cause plugging of pore throats causing formation damage (permeability reduction) and injectivity decline during waterflooding. When injectivity decline occurs it is necessary to increase the injection pressure in order to maintain water flow injection. Therefore, a reliable prediction of injectivity decline is essential in waterflooding projects. In this dissertation, a simulator based on the traditional porous medium filtration model (including deep bed filtration and external filter cake formation) was developed and applied to predict injectivity decline in perforated wells (this prediction was made from history data). Experimental modeling and injectivity decline in open-hole wells is also discussed. The injectivity of modeling showed good agreement with field data, which can be used to support plan stimulation injection wells

Characterization and thermal behavior of residues from industrial sugarcane processing

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Desempenho de cultivares de alface americana em resposta a diferentes doses de torta de filtro

Com objetivo de estudar o desempenho de três cultivares de alface americana (Júlia, Tainá e Grandes Lagos) em quatro doses de torta de filtro (0; 10; 20 e 40 ton ha-1), sob cultivo protegido (túnel alto), foi conduzido um experimento na Universidade do Estado de Mato Grosso, em área de Latossolo Vermelho (textura argilosa), nos meses de março a maio de 2009. O delineamento experimental foi em blocos casualizados, distribuídos em esquema fatorial 3 x 4 (cultivares x doses) com quatro repetições. Foram avaliadas as seguintes características agronômicas: circunferência da planta (CP), massa fresca total (MFT), massa fresca comercial (MFCo), massa fresca da cabeça (MFCa), diâmetro do caule (DC), número de folhas comerciais (NFC), comprimento do caule (CC) e número de folhas totais (NFT). As cultivares Júlia e Tainá responderam à adubação com torta de filtro até a dose de 40 ton-1. A cultivar Grandes Lagos respondeu à adubação com torta de filtro até a dose de 35 ton ha-1 para MFT e MFCa e até 40 ton-1 para MFCo. A cultivar Grandes Lagos apresentou melhor desempenho em MFT, MFCo, CC e CP, em relação às demais cultivares, e equiparou-se com a cultivar Tainá em MFCa e NFC e com a cultivar Júlia em DC. Todas as cultivares tiveram comportamentos semelhantes quanto a NFT. A adubação orgânica com torta de filtro aumenta a produtividade de cultivares de alface americana.

Alterações em algumas propriedades de um latossolo degradado com uso de lodo de esgoto e resíduos orgânicos

A recuperação de áreas muito impactadas, como as oriundas da construção de hidrelétricas, é um processo lento e, usualmente, requer a adição de resíduos orgânicos, como fonte de matéria orgânica, e de nutrientes, como condicionador das propriedades do solo. O objetivo deste trabalho foi verificar o efeito da adição de lodo de esgoto e resíduos orgânicos (maravalha e torta de filtro de cana-de-açúcar) sobre o crescimento de duas espécies arbóreas de Cerrado na recuperação de um subsolo de uma área degradada pela construção da Usina Hidrelétrica de Ilha Solteira, localizada em Selvíria - MS. O experimento foi conduzido em casa de vegetação em delineamento experimental inteiramente casualizado, com oito tratamentos, seis repetições e uma planta por repetição, para cada planta-teste. Cada repetição (saco plástico) teve 3,3 L e as proporções em volume da mistura de cada resíduo foram de: 30 % de lodo de esgoto, 20 % de torta de filtro e 10 % de maravalha de madeira. Foram mensuradas a fertilidade, a micorrização, a atividade microbiana (C-CO2 liberado) do subsolo, a massa do sistema radicular e parte aérea e a altura de plantas de duas espécies nativas do Cerrado [monjoleiro (Acacia polyphylla DC.) e jatobá-do-Cerrado (Hymenaea stigonocarpa Mart)]. Os tratamentos com lodo de esgoto proporcionaram maior atividade microbiana no substrato e maior crescimento para as duas espécies arbóreas. A presença do lodo de esgoto promoveu melhora na fertilidade do subsolo, com aumento dos teores de matéria orgânica, P, K, Ca e Mg. A matéria orgânica e o P tiveram seus teores elevados nos tratamentos com mistura de lodo de esgoto e demais resíduos. Os resultados permitem concluir que as misturas contendo lodo associado a resíduos promoveram melhores incrementos na qualidade do subsolo, com perspectivas de sua recuperação.

Qualidade tecnológica da cana-de-açúcar sob adubação com torta de filtro enriquecida com fosfato solúvel

The study had the objective to evaluate the effect of the fertilization with filter cake enriched with soluble phosphate on the sugar yield. The experiment carried at Presidente Prudente-SP, used a randomized complete block design, in the factorial scheme 5 x 4, where the first factor consisted of doses of filter cake (0; 0.5; 1.0; 2.0 and 4.0 t ha(-1)) and the second, doses of phosphorus fertilizer (0, 50, 100, 200 kg ha(-1) of P2O5), with 4 replicates, totaling 80 plots. The results indicated that phosphorus applied in planting furrows improves the quality of sugarcane raw matter by increasing the levels of soluble solids, total reducing sugars and sucrose in the stalks. The phosphorus also increases the productivity of sugar. The filter cake applied in planting furrow has the potential to partially replace the chemical fertilization with phosphate aiming to improve the quality and the productivity of sugar. The best combination was filter cake at dose between 2.6 and 2.7 t ha(-1) combined with dose between 160 and 190 kg P2O5 ha(-1) for obtaining best response of soluble solids and productivity of sugar.