Desenvolvimento de coagulante/ floculante para tratamento de águas residuais numa indústria de adesivos

Esta dissertação teve como objetivo clarificar a qualidade das águas residuais de uma indústria de fabricação de adesivos. Para esta clarificação optou-se por um tratamento de coagulação/floculação a ser efetuado com a adição de apenas um produto no estado sólido. Para este estudo, selecionou-se substâncias comercialmente disponíveis destacando-se para esta formulação um coagulante, sulfato de alumínio (Al2 (SO4).3H2O, dois adjuvantes, hidróxido de cálcio, Ca(OH)2 (adjuvante H) e Montmorillonite, Al2O3.4SiO2.H2O (adjuvante M) e um floculante, uma poliacrilamida aniónica (C3H5NO)n. O efluente bruto da indústria de adesivos foi caraterizado e verificou-se que dos parâmetros analisados, apenas o pH obedece aos valores limite de emissão para descarga no coletor municipal. Determinaram-se as quantidades ótimas das substâncias selecionadas, a quantidade mínima de produto formulado e foi feita a otimização da composição do produto formulado, para três níveis de pH e duas condições de agitação Numa primeira fase, a realização de ensaios preliminares sobre a quantidade de cada uma das substâncias conduziu aos valores 5 e 30 g de coagulante, 2 e 10 g de adjuvante M; 3 g de adjuvante H e 0,01 g de floculante por 500 mL de efluente. Na otimização da quantidade mínima de produto formulado obteve-se o valor de 5g de produto por 500 mL de efluente. Relativamente à formulação do produto foi definido estudar o efeito da variação das razões, %(m/m), dos adjuvantes (M e H) em função do coagulante, para diferentes valores de pH inicial (6,2; 8,1 e 10) e para duas condições de agitação (A e B), sobre os parâmetros analisados (CQO, SST, turvação, pH final e IVL). Na condição A manteve-se uma agitação de 150 rpm durante 2 minutos, reduzindo-se para 60 rpm durante 15 minutos e, por fim, para 30 rpm durante 5 minutos. Na condição B foi usada uma agitação constante de 90 rpm durante 22 minutos. O estudo do efeito das variações das razões % (m/m) dos adjuvantes M e H foi dividido em três grupos com três subgrupos: 1º grupo - 0,6 a razão mássica adjuvante M/coagulante e 0,4, 1,2 e 2 a razão mássica adjuvante H/ coagulante; 2º grupo - 0,2 a razão mássica adjuvante M/coagulante e 0,1, 0,4 e 0,6 a razão mássica adjuvante H/ coagulante; 3º grupo - 0,1 a razão mássica adjuvante M/coagulante e 0,1, 0,2 e 0,3 a razão mássica adjuvante H/ coagulante. Após este estudo obteve-se para cada condição de agitação (A e B), as razões %(m/m) e o pH inicial mais adequados, com base nos melhores resultados obtidos no efeito sobre a CQO. Para a condição de agitação A o melhor resultado obteve-se para pH inicial igual a 8,1 com a razão mássica de adjuvante M/ coagulante igual a 0,1 e a razão mássica de adjuvante H/coagulante igual a 0,1 (percentagens de remoção de 98,01%, 99,60% e 99,43% para a CQO, SST e turvação, respetivamente). Para a condição de agitação B o melhor resultado obteve-se para pH inicial igual a 8,1 com a razão mássica de adjuvante M/ coagulante igual a 0,1 e a razão mássica de adjuvante H/coagulante igual a 0,1 (percentagens de remoção de 98,67%, 99,77% e 98,40% para a CQO, SST e turvação, respetivamente). Nestas condições é necessário efetuar a correção do pH após o tratamento. Apesar das elevadas percentagens de remoção obtidas, o índice volumétrico de lamas indica fraca qualidade de sedimentação.

Influence of lime type and curing conditions on lime and lime-metakaolin mortars

Durability of Building Materials and Components (Vasco Peixoto de de Freitas, J.M.P.Q. Delgado, eds.), Building Pathology and Rehabilitation, vol. 3, VIII, 105-126. ISBN: 978-3-642-37474-6 (Print) 978-3-642-37475-3 (Online). Springer-Verlag Berlin Heidelberg. DOI: 10.1007/978-3-642-37475-3_5

Chromatic reintegration of historical mortars with lime-based pozzolanic consolidant products

3rd Historic Mortars Conference, 11-14 September 2013, Glasgow, Scotland

Evaluation of Pozzolanic Reactivity of Artificial Pozzolans

Materials Science Forum Vols. 730-732 (2013) pp 433-438

The influence of brick residues in the behaviour of lime mortars

XXXVI IAHS World Congress on Housing - National Housing Programs-New Visions, November 03–07, 2008, Kolkata, India

Lime mortars with brick dust and grounded particles for ancient masonry: development and evaluation

HMC08 - 1st Historical Mortars Conference: Characterization, Diagnosis, Conservation, Repair and Compatibilit, LNEC, Lisbon, 24-26 September 2008

Barramento delgado anti carbonatação

Dissertação de mestrado integrado em Engenharia Civil

Ligantes de baixo impacto ambiental e baixo custo, baseados na ativação química de escórias de aciaria

Dissertação de mestrado integrado em Engenharia Civil

A estimação do efeito residual de fertilizantes por meio da Lei de Mitscherlich

This paper deals with the estimation of the residual effect of fertilizers through the use of Mitscherlich's law. The formulas and reasonings now presented are a further development of those introduced previously by PIMENTEL GOMES (2). The new formulas allow the estimation of the residual effect h in cases where the experiments are carried out in the same plots for two or three subsequent years (or crops). In an experiment analysed as an example, the residual effect of calcium hydroxide was estimated to be h = 0.423, that is, about 42%, so that one should advise the use of frequent application of small amounts of lime instead of heavy quantities used at long intervals.

Evaluation of Carbide Waste Lime for Soil Stabilization, Progress Report, HR-111

A lime by-product from the manufacture of acetylene from calcium carbide will be commercially available in Iowa. Since the cost of carbide waste lime f.o.b. source is only about half that of ordinary commercial lime, this material was investigated for potential uses in soil stabilization. The by-product lime is calcium hydroxide in a water slurry with approximately 40% solid concentration. Its effectiveness at stabilizing soils was checked by comparing with commercial high-calcium and dolomitic monohydrate varieties of lime. This was done by soil strength and plasticity tests in addition to studies of the reaction products by X-ray diffraction and chemical methods.

Histopathological evaluation of root canal filling materials for primary teeth

This study aimed to assess the response of apical and periapical tissues of dogs¿ teeth after root canal filling with different materials. Forty roots from dogs¿ premolars were prepared biomechanically and assigned to 4 groups filled with: Group I: commercial calcium hydroxide and polyethylene glycol-based paste (Calen®) thickened with zinc oxide; Group II: paste composed of iodoform, Rifocort® and camphorated amonochlorophenol; Group III: zinc oxide-eugenol cement; Group IV: sterile saline. After 30 days, the samples were subjected to histological processing. The histopathological findings revealed that in Groups I and IV the apical and periapical regions exhibited normal appearance, with large number of fibers and cells and no resorption of mineralized tissues. In Group II, mild inflammatory infiltrate and mild edema were observed, with discrete fibrogenesis and bone resorption. Group III showed altered periapical region and thickened periodontal ligament with presence of inflammatory cells and edema. It may be concluded that the Calen paste thickened with zinc oxide yielded the best tissue response, being the most indicated material for root canal filling of primary teeth with pulp vitality.

Kaivosteollisuudessa syntyvän kipsin hyödyntäminen

Diplomityön tarkoituksena oli tutkia ja kehittää käyttökohde kaivosteollisuudessa syntyvälle märälle kipsisivuvirralle, joka sisältää metalliepäpuhtauksina alumiinia, rautaa ja mangaania ja jonka määrä on noin 1 000 000 t/a. Kirjallisuuden pohjalta tutkittiin aluksi mahdollisuutta hyödyntää kipsiaines asfaltti- ja sementtiteollisuuden raaka-aineena. Sementin joukkoon lisätään tavallisesti noin 5 p-% kipsiä, mutta harvinaisimpiin sementtilaatuihin sitä voidaan lisätä jopa 30 p-%. Tästä huolimatta vain pieni osa tutkimuksen kohteessa syntyvästä kipsisivuvirrasta voitaisiin hyödyntää tässä sovelluksessa. Lisäksi kipsisivuvirran sisältämät epäpuhtaudet täytyisi poistaa tai saattaa inaktiiviseen muotoon. Myöskään sen kosteuspitoisuus ei saisi olla suuri. Näin ollen tämän kipsisivuvirran hyödyntäminen asfaltti- ja sementtiteollisuuden lisäaineena ei ole mahdollista Seuraavaksi harkittiin kipsin kierrättämistä, jolloin yhtenä vaihtoehtona oli hajottaa kipsi termisesti rikkioksideiksi ja valmistaa niistä rikkihappoa. Taloudellisista syistä hajoamistuotteen on oltava rikkitrioksidia, josta voitaisiin veteen imeyttämällä valmistaa rikkihappoa. Kipsin hajottaminen termovaa´alla osoitti, että kipsi vaatii noin 1400 ºC:n lämpötilan ja haihtuvat komponentit ovat H2O, SO ja SO2, muttei SO3. Alempien oksidien muuttaminen rikkihapoksi vaatisi katalyyttisen hapetuksen, mikä olisi käytännössä liian kallista. Toisena vaihtoehtona kipsin kierrättämiseksi tutkittiin sen biologista pelkistämistä rikkivedyksi ja kalsiumhydroksidilietteeksi. Laboratoriossa Ca(OH)2-lietteestä valmistettiin hiilidioksidin avulla kalsiumkarbonaattia, jolloin päästiin 90 %:n kalsiumhydroksidin konversiossa. Lisäksi alumiinihydroksidi saatiin erotettua kipsilietteestä kokeellisesti hydrosyklonin avulla. Diplomityössä päädyttiin siihen, että sulfaatin biologinen pelkistäminen ja alumiinihydroksidin mekaaninen erotus jatkuvatoimisesti on varteenotettava vaihtoehto kipsisivuvirran hyödyntämiseksi.

Influence of initial CaO/SiO2 ratio on the hydration of rice husk ash-Ca(OH)2 and sugar cane bagasse ash-Ca(OH)2 pastes

This work presents the results of a study on the hydration of pastes containing calcium hydroxide and either rice husk ash (RHA) or sugar cane bagasse ash (SCBA) in various initial CaO/SiO2 molar ratios. The products of the reactions were characterized by thermal analyses X-ray diffraction, and scanning electron microscopy. In the case of the RHA pastes, the product was composed of CaO-SiO2-H2O (type I C-S-H) or CaO-SiO2-H2O (type II C-S-H) according to the CaO/SiO2 ratio of the mixture. In contrast, in the case of the SBCA pastes, the product was composed primarily of CaO-SiO2-H2O that differed from both the previous types; the product also contained inclusions of calcium aluminate hydrates.

Epäpuhtauksien poistaminen prosessivesistä

Kemira Chemicals Oy in Äetsä produces sodium chlorate as its main product. It is produced with electrolysis in electrolyte cells. During the manufacturing process impurities, out of which the largest one is iron, accumulate in the cells. These impurities are removed in cell wash with hydrochloric acid liquid, after which the wash water is precipitated with sodium hydroxide and sodium carbonate, and filtered with filter press. After the treatment the wash water is recycled back to the manufacturing process. The aim of this thesis was primarily to improve the treatment of wash water in order to remove the impurities with low costs. This would result in more impurity-free water and in sufficient capacity of impurity removal. The second aim was to maintain the chromium in the treated wash water because it forms a diaphragm of chromium hydroxide to cathode which prevents the flow of anions to cathode. The literature part investigates properties, use and manufacturing of sodium chlorate, electrolyte cell and its wash technique, and impurities of wash water. The beginning of the applied part investigates alternatives of separation methods which could be used to improve the treatment of wash water. In the experiments an optimum pH for the precipitation of wash water was determined, and a research of the use of sodium hydroxide, sodium carbonate, calcium hydroxide and calcium chloride as a precipitant was carried out. Also a suitable flocculant and a filter cloth for the treatment of wash water were determined. Finally, process changes were introduced, partly by applying the current equipment, and the costs and savings were calculated.

Lannoitetehtaan prosessivesien käsittelyvaihtoehtojen soveltuvuuden arviointi

Phosphorus and nitrogen cause eutrophication of water bodies, causing severe damage to the ecosystem. Eutrophication of the waters causes oxygen depletion, which in turn increases fish mortality, releasing toxins in waters. The released toxins can cause damage to animals and humans, which is the reason in many countries to set emission limits for waste water. Nutrients exist naturally, but due to human activities there is high nutrient leaching to water bodies. Human activity is one of the main reasons to the eutrophication. The aim of this thesis was to estimate the suitability of different water treatment options for Yara Finland’s fertilizer plant’s process waters in Siilinjärvi. The fertilizer plant process waters are high concentrate and especially nitrogen concentrations are high, which bring challenge to the treatment. At the theoretical part was investigated conventional and as well advanced wastewater treatment methods like reverse osmosis, adsorption and ion exchange. Beside different treatment methods corporate environmental requirements, responsibility and strategies were researched. At the empirical part of the thesis the goal was to find out possibil-ities to intensify the efficiency of purification at lamella clarifier with chemical precipitation. In addition possibility to use already existing chemical purifying plant for process waters was estimated. As a result of the research Yara has a possibility to intensify lamella clarifier’s action by addi-tion of calcium hydroxide and thus to obtain the phosphorus and fluorine to precipitate out of the water. But in practice this would be too expensive. It is possible to eliminate nitrogen compounds by adsorption or ammonia stripping, both methods requires additional testing. It is possible to process waters in chemical purifying plant, if ammonium nitrogen has been reduced before. Reverse osmosis is possible to exploit for the phosphoric acid plant’s waters.