Every year, millions of tons of paper are diverted from landfills and recycled. Newspaper constitutes a large portion of total paper recycled, providing a cheap source of raw material for the paper industry and helping sustainable forestry. The recycling of newsprint paper involves the separation of ink from the newsprint, which is done either by flotation or washing. Conventional flotation processes for separating ink are not adequate for newsprint printed using flexography printing technique and with water-based ink. The removal of these flexographic water-based inks by washing is a better alternative. However, one drawback of washing is that it has lower yield. In addition, the subsequent wash filtrate is difficult and costly to decontaminate. The overall goal is to develop a combination of processes that can remove ink from a feedstock that contains up to 100% flexographic ink newsprint; in the context of process variables with known effects. In the present work the objectives are to (1) demonstrate that incorporating an electric field into a conventional deinking process improves deinking efficiency, (2) propose a mechanism of how incorporating an electric field helps to improve deinking efficiency, (3) demonstrate that an electric field can decontaminate water containing flexographic inks and identify the mechanism behind electric field clarification of water, and (4) demonstrate that by incorporating electric fields into both the flotation deinking stage and water decontamination, the target deinking efficiency can be achieved.

Made available in DSpace on 2015-07-22T20:50:11Z (GMT). No. of bitstreams: 0 Previous issue date: 2010-02-24 / Introdução: A coloproctopatia actínica crônica (CAC) é uma complicação reconhecida da radioterapia. O sangramento retal (SR) é a queixa mais comum da CAC e a melhor modalidade de tratamento endoscópico para este sintoma permanece controversa. Objetivo: Comparar a eficácia e a segurança da eletrocauterização bipolar (EB) com a eletrocauterização com plasma de argônio (EPA) no tratamento do SR secundário à CAC. Pacientes e Métodos: Foram incluídos 30 pacientes com SR ativo proveniente da CAC, randomizados em 2 grupos (15 para EB e 15 para EPA) e classificados de acordo com escore de Saunders. A potência foi de 50 W para a EB e de 40 W para a EPA. Todos foram submetidos à colonoscopia inicial para o diagnóstico da lesão e sua extensão e exclusão de outras doenças. O sucesso do tratamento foi definido pela erradicação de todas as telangiectasias. Foram consideradas falhas de tratamento, os casos nos quais sete sessões não foram suficientes para o controle do sangramento. Complicações foram divididas em três diferentes grupos: sensitivas (dor anal, dor abdominal e febre), hemorrágicas (piora do sangramento durante o tratamento e sangramento por úlceras) e anatômico-motoras (afilamento das fezes, estenoses e pseudopólipos). Resultados: A média de idade foi de 67,4 anos (variação de 33 a 82 anos) com 14 mulheres e 16 homens. Não houve diferença estatística significante entre os grupos no número de sessões (p = 0,313). Não houve diferença significativa em relação às complicações sensitivas (p = 0,245), hemorrágicas (p = 0,169) ou anatômico-motoras (p = 0,700) entre os grupos. Entretanto, a incidência total de complicações foi significativamente maior no grupo EB. Somente uma falha terapêutica foi observada em cada grupo (p = 1,000). Também não houve diferença significativa na recidiva (p = 1,000). Pacientes em uso de aspirina necessitaram de um número maior de sessões para cessação do SR (p = 0,036) e para erradicação das telangiectasias (p = 0,047). Conclusões: A EPA e a EB apresentaram semelhanças em relação à eficácia no tratamento da coloproctopatia actínica crônica hemorrágica. Contudo, a EPA é mais segura que a EB. / Introduction: Chronic radiation coloproctopathy (CRCP) is a well-recognized complication of radiotherapy. Rectal bleeding is the most common symptom of radiation injury and the optimal endoscopic treatment of bleeding due to CRCP is still controversial. Aim: To compare the efficacy and safety of bipolar eletrocauterization (BEC) and argon plasma eletrocauterization (APE) in the management of bleeding from CRCP. Methods: Thirty patients with active bleeding from telangiectasias were enrolled, randomized into two groups (15 BEC and 15 APE) and classified according to Saunders score. Power settings were 50 W for BEC and 40 W for APE. Initial treatment was performed after a complete colonoscopy to rule out synchronous lesions and follow-up was performed with flexible sigmoidoscopies. Success was defined as eradication of all telangiectasias. Failure was defined whenever more than seven sessions or other therapies were necessary for treatment of bleeding. Complications were divided into three different groups: sensory (anal pain, abdominal pain and/or fever), hemorrhagic (worsening of bleeding during treatment, bleeding from ulcers) and anatomic/motor (tapered feces, stenosis and/or pseudopolyps). Results: Mean age was 67.4 years (range 33-82), with 14 women and 16 men. There was no significant difference regarding the number of sessions in both groups (p = 0.313). There were no significant differences regarding sensory (p = 0.245) hemorrhagic (p = 0.169) or anatomic/motor (p = 0.700) complications between both groups. However, the overall complication rate was significantly higher in EB group (p = 0.020). Only one failure was observed in each group (p = 1.000). There was also no significant difference regarding relapse (p = 1.000) Conclusions: BEC and APE are equally effective in patients with bleeding telangiectasias from CRCP. Nevertheless, APE is safer than EB. / TEDE / BV UNIFESP: Teses e dissertações

Made available in DSpace on 2014-12-17T15:01:54Z (GMT). No. of bitstreams: 1 KatiaRS_TESE.pdf: 3330352 bytes, checksum: a77bcf257b8b71b30d6dadf0de0d7fd4 (MD5) Previous issue date: 2012-03-30 / Conselho Nacional de Desenvolvimento Cient?fico e Tecnol?gico / Among the waste generated in the petrochemical industry water associated with oil production is the most important. It is considered one of the great challenges due to the presence of considered toxic chemicals present in this composition. The presence of these substances difficult to reuse the water associated with the enhanced recovery processes, so that prior to their reuse or disposal, treatment is necessary. This paper aimed to study the removal efficiency of chemical species: Ba2+, Ni2+, Cd2+, Cu2+, Cr3+, Sr2+ and Zn2+, present in the composition of the water associated with oil production by electrocoagulation. The evaluation of removal of these chemical species was performed by laboratory tests using electrochemical batch reactors and continuous flow. Initial tests were performed with electrocoagulation of synthetic wastewater in batch reactor using iron electrode. Results of removal of Zn2+ and Ni2+ were 78 % and 59 % respectively. While the percentage of removed Ba2+ was 19 % by 30 minutes of treatment and by applying current of 1.10 A. The tests were performed on effluent batch reactor applying the electrochemical technique with stainless steel electrodes 304, the objective was to remove part of the dispersed oil and also of organic compounds in the effluent. Under the experimental conditions used, the maximum result was obtained TOG was 60 % and TOC was approximately 50 % compared to the initial concentration. In the experiments carried out in continuous reactor, with effluent semisynthetic, have been used electrodes of iron and aluminum and the results were 100 % removal of Cd2+, Cu2+, Cr3+ and Zn2+ and 77 % of Sr2+. These percentages were only attainable through the use of the iron electrode. However, when the electrode was replaced by aluminum, there was a reduction in the percentage of removal to 65 %, using the same flow rate and current. Therefore according to the results obtained using the iron electrode was more effective in removing these metals and the conditions of lower current and lower flow rate was satisfactory, as observed in the experimental design adopted / Dentre os res?duos gerados na ind?stria petroqu?mica a ?gua associada ? produ??o de petr?leo ? a mais importante. Ela ? considerada um dos grandes desafios devido ? presen?a de subst?ncias qu?micas consideradas t?xicas presente na sua composi??o. A presen?a dessas subst?ncias dificulta a reutiliza??o da ?gua associada nos processos de recupera??o avan?ada, fazendo com que antes da sua reutiliza??o ou descarte, seja necess?rio seu tratamento. Este trabalho teve como objetivo o estudo da efici?ncia de remo??o das esp?cies qu?micas: Ba2+, Ni2+, Cd2+, Cu2+, Cr3+, Sr2+e Zn2+, presentes na composi??o da ?gua associada ? produ??o de petr?leo por eletrocoagula??o. A avalia??o de remo??o dessas esp?cies qu?micas foi realizada por testes em laborat?rio utilizando reatores eletroqu?micos de batelada e de fluxo cont?nuo. Os testes iniciais da eletrocoagula??o foram realizados com efluente sint?tico em reator batelada utilizando eletrodo de ferro. Os resultados de remo??o de Zn2+ e de Ni2+ foram de 78% e 59%, respectivamente. Enquanto que o percentual removido de Ba2+ foi de 19%, em 30 minutos de tratamento, aplicando corrente de 1,10A. Os testes com efluente foram realizados em reator batelada aplicando a t?cnica eletroqu?mica com eletrodos de inox 304, o objetivo foi remover parte do ?leo disperso e tamb?m, de compostos org?nicos presentes no efluente. De acordo com as condi??es experimentais usadas, o resultado m?ximo obtido de TOG foi de 60% e de TOC foi aproximadamente de 50%, em rela??o ? concentra??o inicial. Para os experimentos realizados em reator cont?nuo, com efluente semi-sint?tico, foram usados eletrodos de ferro e de alum?nio e os resultados obtidos foram de 100% de remo??o de Cd2+, Cu2+, Cr3+ e Zn2+ e 77% de Sr2+. Esses percentuais s? foram poss?veis de alcan?ar mediante o uso do eletrodo de ferro. Entretanto quando esse eletrodo foi substitu?do pelo de alum?nio, ocorreu um decr?scimo no percentual de remo??o para 65%, utilizando-se a mesma vaz?o e corrente. Portanto segundo os resultados obtidos, a utiliza??o do eletrodo de ferro mostrou-se mais eficaz na remo??o desses metais e as condi??es de menor vaz?o e menor corrente foram satisfat?rias, conforme observado no planejamento fatorial adotado

Submitted by Marilene Donadel (marilene.donadel@unioeste.br) on 2018-04-26T23:32:00Z No. of bitstreams: 1 Aline_Pauli_2018.pdf: 5534766 bytes, checksum: 389503e1e5a4307c462f405e73451ed5 (MD5) / Made available in DSpace on 2018-04-26T23:32:00Z (GMT). No. of bitstreams: 1 Aline_Pauli_2018.pdf: 5534766 bytes, checksum: 389503e1e5a4307c462f405e73451ed5 (MD5) Previous issue date: 2018-02-28 / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior - CAPES / This work aims to remove efficiently organic and inorganic pollutants from a municipal sanitary landfill leachate effluent (SLLE) through of the integrated purification treatment application, composed by the electrocoagulation (ECP) and biological oxidation processes (BOP), looking for the drastic drop on the toxicity. In the first treatment phase, an ECP-based reactor was constructed consisting in a series of 6 aluminum electrode, providing an effective area of 350 cm2 and a useful volume of 1,0 L. In the framework of the response surface methodology (RSM), a 3³ complete factorial experimental design (CFED) at three levels of the three ECP important parameters: initial pH, electric current density (ECD) and electrolysis time (ET) was regarded. A set of responses related to the ECP treatment, such as, the reduction of color, turbidity, COD and iron concentration, was interpreted within the RSM. Additionally, the Analysis of Variance (ANOVA was applied to assess the quality of the second-order polynomial mathematical models that were adjusted to the CFED data. Keeping fixed the best ECP condition (pH and ECD) for the pollutant removals, a set of kinetic tests was carried out regarding a wide range of ET values. The toxicity of ECP treated samples was assessed by the application of bioassays based on the mortality level of the brine shrimp (Artemia salina) and the germination of Lactuca sativa seeds. The toxicity level was assessed by a statistical estimation of the median lethal concentration (LC50) through the application of bioassays with Artemia salina and Lactuca sativa. The biodegradability index by applying the Zahn Wellens test was also assessed. Keeping fixed the ECP condition for which was obtained the lowest toxicity and the highest biodegradability index, the second phase of treatment by BOP was performed. In this regard, a biological reactor with a useful volume of 3.5 L was adjusted to operate keeping fixed the condition of pH 7, temperature of 33 oC and dissolved oxygen of 50%. A relation food/microorganism of one was considered. After that, the residual ammonia in samples was completely removed applying the stripping method (air injection of 50 Lh-1). From the CFED data related to the first treatment phase, the best ECP condition was found by setting the pH at 5, ET at 120 min and ECD at 128.57 Am-2 for which was obtained the maximum removal of 99, 98, 68 e 99% for color, turbidity, COD and iron concentration, respectively. From the kinetic tests, it was possible to verify that the application of the ECP has actually reduced the SLLE toxicity being an ET of 5 min enough to achieve the minimum time required to obtain the lowest toxicity index (LC50 of 43%) that was found in both biotests. The highest biodegradability index was found when an ET value of 45 min. was regarded. The second POB treatment has showed a significant performance on removals of the organic parameters, with values of 95% and 89% for COD and DOC, respectively. Because of achieving an almost 100% removal of the ammoniacal nitrogen, the main result was the substantial improvement on the LC50 value about of 95%, as suggested by the A. salina biotest. Thus, although there were small amounts of pollutants after both treatments (PEC and POB), an almost total toxicity depletion. / Este trabalho, tem como objetivo remover eficientemente os poluentes orgânicos e inorgânicos de efluente de lixiviado proveniente de aterro sanitário municipal mediante a aplicação do tratamento de purificação integrado composto pelos Processos de Eletrocoagulação (PEC) e Oxidação Biológica (POB), visando especificamente a queda da toxicidade e o cumprimento da condição ambientalmente segura para o descarte final em corpos hídricos. Para o PEC, construiu-se um reator com 6 eletrodos de alumínio, tendo uma área efetiva de 350 cm2 e um volume efetivo de efluente de 1,0 L. No contexto da Metodologia de Superfícies de Resposta (MSR), foi proposto um planejamento experimental 3³, variando-se três parâmetros importante do PEC: pH inicial, Densidade de Corrente Elétrica (DCE) e Tempo de Eletrólise (TE). As respostas ao tratamento por PEC (cor, turbidez, DQO e concentração de ferro) foram interpretadas dentro da MSR, verificando pela Análise de variância (ANOVA) a qualidade da representatividade dos modelos matemáticos, polinomiais de segunda ordem, ajustados aos dados. Mantendo fixa a melhor condição de remoção de poluentes pelo PEC quanto ao pH e DCE, experimentos cinéticos foram realizados considerando um amplo intervalo de TE. O nível de toxicidade foi inferido a partir da estimativa estatística da concentração letal mediana (CL50) mediante a aplicação de biotestes utilizando o microcrustáceo Artemia salina e sementes de Lactuca sativa. Avaliou-se o índice de biodegradabilidade, segundo o teste de Zahn Wellens. Na menor toxicidade e o maior índice de biodegradabilidade do lixiviado tratado pelo PEC foi realizada a aplicação da segunda fase de tratamento por POB. Para tanto, foi ajustado o reator biológico, com volume útil de 3,5 L a operar, de forma controlada, na condição de pH 7, temperatura de 33 oC e oxigênio dissolvido de 50%. Utilizou-se uma relação alimento/microrganismo igual a um. Após a realização da integração dos processos, foi feita a remoção de amônia residual do efluente pelo método de arraste (injeção de ar a 50 Lh-1). Da análise do planejamento da primeira fase de tratamento, encontrou-se a melhor condição do PEC no valor de pH igual a 5; TE em 120 min e DCE em 128,57 Am-2 cujo efeito foi a obtenção da máxima remoção de 99, 98, 68 e 99% na cor, turbidez, DQO e concentração de ferro, respectivamente. A partir dos testes cinéticos, foi possível verificar que o PEC reduziu consideravelmente a toxicidade, sendo o TE de 5 minutos a condição de menor toxicidade (CL50 de 43%) que foi encontrada por ambos os biotestes. O índice de biodegradabilidade do efluente de lixiviado tratado teve um aumento de aproximadamente 20% em relação ao efluente bruto para todos os tempos de tratamento por PEC; porém, o maior índice de biodegradabilidade foi encontrado quando houve um TE de 45 minutos. O segundo tratamento por POB apresentou expressiva remoção dos parâmetros orgânicos, sendo obtidas remoções de 95% e 89% para a DQO e o COD, respectivamente. Após a aplicação do processo de arraste de amônia, uma remoção de quase 100% do nitrogênio amoniacal foi alcançada, obtendo uma a CL50 da ordem de 95%, como revelada pelo bioteste com A. salina. Portanto, embora houvesse quantidades pequenas de poluentes após ambos os tratamentos (PEC e POB), atingiu-se a quase total depleção da toxicidade.

Abstract Oily wastewaters are heterogeneous, containing various types of oils, surfactants from detergents, metals etc. Oily wastewaters are produced from a wide range of industries such as metalworking, petroleum refineries, the petrochemical industry, transportation as well as the textile and food industries. Oily wastewaters, especially those containing stable oil-in-water emulsions, require advanced treatment as conventional treatment methods have their limitations to meet ever-stricter environmental regulations. Ultrafiltration is a widely accepted and commonly used treatment method for oily wastewaters. The first aim of this thesis was to increase knowledge concerning the performance of an industrial-scaled ultrafiltration-based process treating concentrated real oily wastewaters. The demand for a more effective pre-treatment method for ultrafiltration to enhance performance and decrease fouling of membrane was observed. The second aim of the thesis was to investigate the suitability and efficiency of different methods for treating concentrated model oil-in-water emulsions and real oily wastewaters. The treatment methods studied were electrocoagulation (electrolytic dissolution of anodic metal), conventional coagulation-flocculation followed by either sedimentation or dissolved air flotation, and dissolved air flotation utilising cationic air bubbles. Electrocoagulation was discovered to be a promising treatment method for various types of oil-in-water emulsions. Dissolved air flotation with cationic modified air bubbles was proven to be an efficient method with even higher treatment results with smaller chemical doses when compared to conventional coagulation-flocculation followed by dissolved air flotation. The biodegradation of various components is an important measure of their impact on the environment in case of spillage. The third aim of the thesis was to explore the biodegradability of different types of oils and surfactants in solution conditions and soils. It was discovered that the biodegradation of light fuel oil continued during a three-month time period, reaching a biodegradation degree of over 60% in mineral-rich soil. For surfactants, their distinct effect on the biodegradation of organic material in soil was observed, and it masked the biodegradation of the surfactants themselves. / Tiivistelmä Öljyiset jätevedet ovat heterogeenisiä, sisältäen mm. erityyppisiä öljyjä, metalleja ja pesuaineiden pinta-aktiivisia aineita. Öljyisiä jätevesiä muodostuu laajalti eri teollisuuksista, kuten metallintyöstöstä, öljyn jalostuksesta, petrokemian teollisuudesta, ruoka- ja tekstiiliteollisuudesta sekä liikenteestä. Öljyiset jätevedet, varsinkin stabiileja öljyemulsioita sisältävät, vaativat tehokkaan käsittelymenetelmän, jotta ympäristölainsäädännön ja luvituksen ehdot täyttyvät. Ultrasuodatus on yleisesti käytössä oleva öljyisten jätevesien käsittelymenetelmä. Tämän väitöstyön ensimmäinen tavoite oli lisätä tietoutta teollisen mittakaavan konsentroituneiden öljyisten jätevesien ultrasuodatusprosessien tehokkuudesta. Prosessien strategisista kohdista kerättyjen öljyisten jätevesien karakterisointitulosten perusteella havaittiin, että ennen ultrasuodatusta tarvitaan tehokas esikäsittelyvaihe prosessin tehostamiseksi ja ultrasuodattimen tukkeutumisen vähentämiseksi. Täten toinen väitöstyön tavoite oli selvittää eri menetelmien soveltuvuutta ja tehokkuutta konsentroituneiden malliaineina käytettyjen öljyemulsioiden ja öljyisten jätevesien käsittelyssä. Tutkitut käsittelymenetelmät olivat elektrokoagulaatio (sähkökemiallinen flokkaavien metalli-ionien liuottaminen anodilta), koagulaatio-flokkulaatio ja laskeutus/korkeapaineflotaatio sekä korkeapaineflotaatiomenetelmä, joka hyödyntää kationisia ilmakuplia. Elektrokoagulaation todettiin olevan erittäin tehokas käsittelymenetelmä, jolla saavutettiin korkeat puhdistustulokset erityyppisille öljyemulsioille. Korkeapaineflotaatiolla, joka hyödyntää kationisia ilmakuplia, saavutettiin hyvät puhdistustulokset jopa pienemmillä kemikaalimäärillä verrattuna perinteiseen koagulaatio-flokkulaatioon ja korkepaineflotaation. Erilaisten komponenttien biohajoavuus on tärkeä suure arvioitaessa niiden ympäristövaikutuksia. Väitöstyön kolmas tavoite oli selvittää erilaisten öljyjen ja pinta-aktiivisten aineiden biohajoavuutta erilaisissa liuosolosuhteissa ja maa-aineksissa. Tärkeimmät biohajoavuustutkimustulokset olivat, että kevyt polttoöljy saavutti kolmen kuukauden mittauksen aikana yli 60 % biohajoavuusasteen mineraalirikkaassa maa-aineksessa. Pinta-aktiivisten aineiden havaittiin lisäävän huomattavasti maan orgaanisen aineksen biohajoamista, ja tämä vaikeutti itse pinta-aktiivisten aineiden biohajoamisen arviointia.

Produced water is the largest waste product by volume in the oil industry and its treatment in onshore or offshore fields poses bigger and different challenges than what water engineers are used to encounter. Process to achieve reuse quality of this water is very expensive with many technical hurdles to overcome making the optimization of the treatment steps necessary. Electrocoagulation (EC) generates coagulants in-situ responsible for destabilizing oil droplets, suspended particles, and common pollutant in produced water. Furthermore, EC is a very efficient technology compared with traditional primary treatments used in the oil & gas industry and has several advantages such as: no hazardous chemical handling (which diminishes the risk of accident and logistic costs), high efficiency potential concerning boron removal, potential small footprint and less sludge generation. In this research, the treatment of produced water using EC was investigated in a practical manner for the oilfield to aim for a cleaner effluent for further processing and help to achieve a reuse quality. For this, an EC cell was designed using different parameters normally used in the literature to fit this scenario. After preliminary tests, the treatment time was set to 3 seconds. Response surface method (RSM) was employed to optimize the operating conditions for TOC removal on a broad quality of synthetic produced water while varying: salinity, initial oil concentration and initial pH. TOC was chosen to be the main response because of its importance in legislation and sensibility on the method. Furthermore, turbidity removal, change of pH value after EC in water with lack of buffer capacity, aluminum concentration and preliminary tests involving boron removal and influence of hydrogen carbonate were also studied. Real produced water was treated with EC to assess the optimum conditions obtained by the RSM showing the results were closely related. Finally, an estimation of volume required and operating cost for EC in the different types of produced water was made to assess how realistic it is for onshore and offshore applications.:ERKLÄRUNG DES PROMOVENDEN I ACKNOLEDGEMENT III ABSTRACT V TABLE OF CONTENT VII LIST OF FIGURES IX LIST OF TABLES X LIST OF EQUATIONS XII ABBREVIATIONS XIV 1. INTRODUCTION 1 2. PRODUCED WATER 6 2.1 Characterization of Oilfield Produced Water 6 2.2 Produced Water Management 10 2.2.1 Discharge and Regulations 10 2.2.2 Efforts on Reuse 11 2.2.3 Cost 14 3. PRODUCED WATER TREATMENT 17 3.1 Most Common Primary Treatment 17 3.1.1 Hydrocyclones 17 3.1.2 Flotation unit 18 3.2 Further Water Treatment Technologies 19 3.2.1 Membrane Process 19 3.2.1.1 Microfiltration 19 3.2.1.2 Ultrafiltration 21 3.2.1.3 Nanofiltration 23 3.2.1.4 Reverse Osmosis 24 3.2.1.5 Forward osmosis 24 3.2.2 Electrodialysis 25 3.2.3 Biological treatment 28 3.2.3.1 Aerobic and anaerobic process 28 3.2.3.2 Combining membrane and bio-reactor 29 3.2.4 Oxidative process 30 3.2.4.1 Oxidation process 30 3.2.4.2 Anodic oxidation 32 3.2.5 Thermal technology 34 3.2.5.1 Evaporation 34 3.2.5.2 Eutectic freeze crystallization 35 3.2.6 Adsorption and ion-exchange 36 3.3 Electrocoagulation 39 3.3.1 Colloidal Stability Theory 39 3.3.2 Theory of Electrocoagulation 40 3.3.3 Mechanism of Abatement of Impurities 44 3.3.4 Operational parameters and efficiency 49 4. MATERIALS AND METHODS 51 4.1 Analytical Techniques and Synthetic Solutions 51 4.1.1 Analytical Techniques 51 4.1.2 Synthetic Produced Water 51 4.2 Design of Experiment and Models 54 4.3 Experimental Protocol for EC 56 4 .4 Development of the new Electrocoagulation cell 57 4.5 Real Produced water 58 5. RESULTS AND DISCUSSION 59 5.1 Designing EC Cell Process 59 5.1.1 Computational Fluid Dynamics for EC manufacturing 59 5.2 Preliminary Experiments 61 5.2.1 TOC Removal and Residence Time Determination 61 5.2.2 Aluminum Concentration 64 5.3 Models Quality and Range of Validity 66 5.3.1 TOC Removal 66 5.3.2 Turbidity Removal 69 5.3.3 Final pH value 71 5.3.4 Ionic Strength and Interpolation for Different Salinities 73 5.3.5 Partial Conclusions 76 5.4 Evolution of the Final pH Value 78 5.5 Operation Region for Effective Treatment of Produced Water with EC 80 5.5.1 Produced Water with Low Salinity 80 Organic Compounds Removal 80 Turbidity Removal 83 5.5.2 Produced Water with Medium Salinity 84 Organic Compounds Removal 84 Turbidity Removal 86 5.5.3 Produced Water with High Salinity 87 Organic Compounds Removal 87 5.6 Influence of Hydrogen Carbonate 90 5.7 Real Produced water 91 5.8 Boron Removal 93 5.9 Estimation of the Size for EC in Full scale 94 5.10 Produced Water with Very Low Salinity and EC 95 5.11 Estimation of Operation Cost 96 6. CONCLUSION AND RECOMMENDATIONS 98 6.1 Conclusion 98 6.2 Recommendations for Future Work 101 Scale up on EC for upstream 101 Further processing and reuse 101 Online optimization for EC 101 Recommendations for any research related to upstream produced water 101 BIBLIOGRAPHY 102 APPENDIX A 117 APPENDIX B 120

Research on the electrocoagulation (EC) of hexane extractable materials (HEM) has been conducted at the University of New Orleans using a proprietary bench-scale EC reactor. The original reactor configuration forced the fluid to follow a vertical upward-downward path. An alternate electrode arrangement was introduced so that the path of flow became horizontal. Both configurations were evaluated by comparing the residence time distribution (RTD) data generated in each case. These data produced indication of internal recirculation and stagnant water when the fluid followed a vertical path. These anomalies were attenuated when the fluid flowed horizontally and at a velocity higher than 0.032 m s-1 . A series of EC experiments were performed using a synthetic emulsion with a HEM concentration of approximately 700 mg l-1. It was confirmed that EC of HEM follows first-order kinetics, and kinetic constants of 0.0441 s-1 and 0.0443 s-1 were obtained from applying both the dispersion and tanks-in-series (TIS) models, respectively. In both cases R2 was 0.97. Also, the TIS model indicated that each cell of the EC behaves as an independent continuous-stirred-tank reactor.

<p>Predmet doktorske disertacije je uklanjanje neorganskih i organskih polutanata iz efluenata ofset tehnike štampe (otpadnog razvijača i otpadnog sredstva za vlaženje) u cilju minimiziranja njihovog štetnog uticaja na životnu sredinu. Uklanjanje polutanata sprovedeno je primenom elektrokoagulaciono/ flotacionog (EKF) tetmana, adsorpcionog (AD) tretmana i kombinacijom navedenih tretmana. Izvodljivost i efikasnost tretmana analizirana je ispitivanjem uticaja karakterističnih operativnih promenljivih u okviru procesa na smanjivanje količine polutanata. Mehanizmi EKF i AD tretmana definisani su na osnovu teorijskih matematičko kinetičkih modela. Za rešavanje problema odlaganja mulja nastalog nakon EKF tretmana primenjen je solidifikaciono/stabiliza-cioni tretman sa odgovarajućim imobilizacionim agensima. Razvijen je efikasan model kombinacije tretmana efluenata grafičkih procesa ofset štampe kojim je omogućena konverzija efluenata u proizvode kompatibilne sa principima i normativima životne sredine.</p> / <p>The topic of this doctoral dissertation is the removal of inorganic and organic pollutants from the offset printing effluents (waste developer and waste fountain solution) in order to minimize their damaging influence onto the environment. The removal of the pollutants has been performed by electrocoagulation/flotation (ECF) treatment, adsorption (AD) treatment and the combination of the two said treatments. Feasibility and efficacy of the treatments has been analyzed by investigating the effect of characteristic operational variables within the process on the decrease in the quantity of pollutants. The mechanisms of ECF and AD treatments have been defined on the basis of theoretical mathematical-kinetic models. For the solution of the problem of sludge disposal, originating from the ECF treatment, a solidification/stabilization treatment with immobilization agents has been applied. An efficient model that combines the offset printing effluent treatments has been developed, the one which enables the conversion of effluents into products compatible with environmental principles and norms.</p>

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / In this study, an analytical method was developed for the quantification of statins Atorvastatin and Simvastatin, in hospital effluent (University Hospital of Santa Maria, using Solid phase extraction and Dispersive liquid-liquid microextraction, followed in liquid chromatography coupled to diode array detector. The principal variables of Dispersive liquid-liquid microextraction were investigated with aid of experimental central composite design. The recovery rates of Solid phase extraction varied from 95% for Atorvastatin and 83.2% for Simvastatin, in aqueous solution, and 92.0% for Atorvastatin and 81.5% for Simvastatin, in hospital effluent. As for the Dispersive liquid-liquid microextraction the recovery rates ranged from 85.5% for Atorvastatin and 89.4% for Simvastatin, in aqueous solution, and 83.0% for Atorvastatin and 83.1% for Simvastatin, in hospital effluent. The sampling was carried out in two sample points called Emergency Effluent and General Effluent . The concentration rates detected in the effluent were 30.1 μg L-1 in Emergency Effluent and 29.0 μg L-1 in General Effluent for Atorvastatin and 37.1 μg L-1 in Emergency Effluent and 36.1 μg L-1 in GE for Simvastatin. Ozonation and electrocoagulation were applied for the degradation/removal of statins. The principal variables of electrocoagulation were investigated with aid of experimental central composite design. The degradation rate obtained in ozonation was 100% for Atorvastatin, in 25 minutes reaction for aqueous solution and hospital effluent; and 100% for Simvastatin, in 4 minutes reaction for aqueous solution and 10 minutes reaction in hospital effluent. As for the electrocoagulation the removal rate was 75.6% in aqueous solution and 70.9% in hospital effluent for Atorvastatin; and 100% in aqueous solution and hospital effluent for Simvastatin in 60 minutes reaction. A preliminary risk evaluation revealed that the statins showed a low environmental risk, PEC/PNEC < 1. / Neste trabalho foi desenvolvida metodologia analítica para a quantificação de estatinas Atorvastatina e Sinvastatina, em efluente hospitalar (Hospital Universitário de Santa Maria), utilizando Extração em fase sólida e Microextração dispersiva líquido-líquido seguida de cromatografia líquida com detector de arranjo de diodos. As principais variáveis da Microextração dispersiva líquido-líquido foram investigadas utilizando a Metodologia de Superfície de Resposta através de um delineamento composto central rotacional. As taxas de recuperação da Extração em fase sólida foram de 95,8% para Atorvastatina e 83,5% para Sinvastatina, em solução aquosa e 92,0% para Atorvastatina e 81,5% para Sinvastatina em efluente hospitalar. Já para a Microextração dispersiva líquido-líquido as taxas de recuperação foram de 85,5% para Atorvastatina e 89,4% para Sinvastatina, em solução aquosa e 83,0% para Atorvastatina e 83,1% para Sinvastatina, em efluente hospitalar. A amostragem foi feita em dois pontos de coleta, denominados Efluente PA e Efluente Geral . A concentração média detectada no efluente foi de 30,1 μg L-1 no Efluente PA e 29,0 μg L-1 no Efluente Geral para Atorvastatina e 37,1 μg L-1 no Efluente PA e 36,1 μg L-1 no Efluente Geral para Sinvastatina. Ozonização e eletrocoagulação foram aplicados na degradação/remoção das estatinas. As principais variáveis da eletrocoagulação foram investigadas utilizando a Metodologia de Superfície de Resposta através de um delineamento composto central. As taxas de degradação obtidas na ozonização foram de 100% para Atorvastatina, em 25 min de reação, para solução aquosa e efluente hospitalar; e 100% para Sinvastatina em 4 min em solução aquosa, e 10 min em efluente hospitalar. Já para a eletrocoagulação as taxas de remoção foram de 75,9% em solução aquosa e 70,9% em efluente hospitalar para Atorvastatina; e 100% para solução aquosa e afluente hospitalar para Sinvastatina, em 60 min de reação. A análise preliminar de risco ambiental revelou que as estatinas apresentam baixo risco ambiental, com PEC/PNEC < 1.

Made available in DSpace on 2017-07-10T18:08:06Z (GMT). No. of bitstreams: 1 Ariadine R C de Souza.pdf: 3448582 bytes, checksum: c9a134accab4a823b60c11ba4b8a1727 (MD5) Previous issue date: 2016-02-23 / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / This research project aimed the evaluation of the antibiotic ciprofloxacin hydrochloride (CIP (HCl)) removal in solution, by applying an electrocoagulation (EC) process. The CIP (HCl) solution was prepared with an initial concentration of 25 mg L-1 CIP (HCl) in distilled water. The experiments were conducted in an EC reactor in laboratory scale, consisting of aluminum electrodes. In order to get the best reactor operating parameters, regarding its variables (initial pH, current intensity and time of electrolysis), a response surface methodology was applied based on a complete experimental design (CED) 3³. The CIP (HCl) concentration was monitored by high-performance liquid chromatography (HPLC), and the mineralization was accompanied based on the reduction of total organic carbon (TOC). To obtain the operating conditions considered ideal for the operation of the EC reactor, a predicted second-order model was adjusted to the experimental responses and then validated by ANOVA. The influence of each reactor operating parameter was individually investigated, in a wider range than the one studied in the CED. Thus, the optimal values for each operating parameters were initial pH at 9.0 and current intensity of 0.8 A. From these responses, a kinetic analysis of the EC process was performed, reaching a rapid reduction of CIP (HCl) in the first minutes of electrolysis, stabilizing at 99% in times greater than 40 minutes. The toxicity of the treated solution was measured by applying ecotoxicity and phytotoxicity bioassays, taking as bioindicators Artemia salina and Lactuca sativa, respectively. The toxicity test using Artemia salina was susceptible to the type of remaining toxic compounds formed after the CIP (HCl) solution treatment of short duration. Furthermore, the remaining toxicity after 75 min of EC became nearly harmless to this bioindicator. On the other hand, the bioindicator Lactuca sativa was not susceptible to the action of these compounds at any treatment time. Due to the possible presence of the organic compound CIP (HCl) at a low concentration in the solutions treated by high electrolysis time, an antimicrobial activity analysis using the microorganisms S. aureus and E. coli was applied. The antimicrobial activity of the solution over 40 min electrolysis treatments was almost null or absent. In order to identify the CIP (HCl) in the sludge generated during the process, an X-ray diffraction (XRD) analysis was applied. CIP (HCl) was not identified in the residual sludge or the treated solution, indicating degradation of the compound during the treatment, possibly by electro-oxidation reactions. Therefore, the electrocoagulation provided the degradation of CIP (HCl) pollutant maintaining the treated solution free of toxicity and adverse biological effects to aquatic biota enabling their disposal in the environment, if the ideal operational conditions are maintained (initial pH 9.0, current density 0.8 A and electrolysis time of 75 min). / Este projeto de investigação visa avaliar a remoção do antibiótico cloridrato de ciprofloxacina (CIP(HCl)) em solução, por meio de um processo de eletrocoagulação (EC). A solução de CIP(HCl) foi preparada com concentração inicial de 25 mg L-1 de CIP(HCl) em água destilada. Os experimentos foram realizados em um reator de EC, em escala laboratorial, constituído por eletrodos de alumínio. A fim de obter os melhores parâmetros de operação do reator em relação as suas variáveis (pH inicial, intensidade de corrente e tempo de eletrólise), uma metodologia de superfície de resposta foi aplicada baseada em um planejamento experimental completo (PEC) 3³. A concentração de CIP(HCl) foi monitorada por cromatografia líquida de alta eficiência (CLAE) e sua mineralização foi baseada na redução do carbono orgânico total (COT). Para obtenção das condições operacionais consideradas ideais para o funcionamento do reator de EC, um modelo previsto de segunda ordem foi ajustado às respostas experimentais e em seguida validado pela ANOVA. A influência de cada parâmetro de funcionamento do reator foi investigada individualmente em uma faixa de estudo mais ampla do que a avaliada PEC. Desta maneira, os valores considerados ideais para cada parâmetro operacional foram: pH inicial 9,0 e intensidade de corrente 0,8 A. A partir destas respostas, foi realizada uma análise cinética do processo de EC, onde se atingiu uma rápida redução de CIP(HCl) nos primeiros minutos de eletrólise, se estabilizando em 99% em tempos superiores a 40 min. A toxicidade da solução tratada foi avaliada aplicando bioensaios de ecotoxicidade e de fitotoxicidade, tomando como bioindicadores a Artemia salina e a Lactuca sativa, respectivamente. O teste de toxicidade utilizando a Artemia salina foi susceptível aos compostos tóxicos remanescentes formados após o tratamento da solução de CIP(HCl) de curta duração. Além disso, a toxicidade após 75 min de EC se tornou quase inócua a este bioindicador. Por outro lado, o bioindicador Lactuca sativa não foi susceptível à ação dos compostos tóxicos remanescentes a qualquer tempo de tratamento. Devido a possível presença do composto orgânico CIP(HCl) em baixas concentrações, nas soluções tratadas por elevados tempos de eletrólise, aplicou-se a análise de atividade antimicrobiana utilizando os micro-organismos S. aureus e E. coli. A atividade antimicrobiana da solução com tratamentos acima de 40 min de eletrólise foi ausente. Visando a identificação da CIP(HCl) no lodo gerado durante o processo, análises de difração de raio-X (DRX) foram realizadas. Não se identificou CIP(HCl) no lodo residual nem na solução tratada, indicando a degradação do composto durante o tratamento, possivelmente por reações de eletroxidação. Portanto, o processo de EC proporcionou a degradação do poluente CIP(HCl), mantendo a solução tratada isenta de toxicidade e de efeitos biológicos adversos à biota aquática possibilitando seu descarte no meio ambiente, se mantidas as condições operacionais ideais para o funcionamento do reator (pH inicial 9,0, intensidade de corrente 0,8 A e tempo de eletrólise de 75 min).