Revaloració de la fracció cel·lular de la sang de porc procedent d'escorxadors industrials

La sang de porc és un subproducte comestible que es genera als escorxadors industrials durant el procés d'obtenció de la canal. Aquest subproducte es caracteritza per presentar una elevada càrrega contaminant i, degut a l'elevat volum que es genera, és necessari trobar estratègies que permetin la seva revaloració i aprofitament, a la vegada que disminuïm la contaminació ambiental i les despeses que es deriven del seu processament abans de l'abocament. La fracció cel·lular (FC) constitueix el 40 % de la sang de porc i conté principalment l'hemoglobina (Hb), que representa al voltant del 90 % del contingut en proteïna d'aquesta fracció (un 35 % aproximadament). L'elevat percentatge en proteïna i en ferro, i les seves bones propietats funcionals fan que l'aprofitament d'aquest subproducte com a primera matèria o ingredient de la indústria alimentària sigui una alternativa molt útil a l'hora de reduir les despeses de la indústria càrnia, sempre que es resolguin els problemes de l'enfosquiment i dels sabors estranys que pot conferir la FC quan s'addiciona a productes alimentaris. Una altra possible utilització de la FC és aprofitar les propietats colorants de l'Hb o del grup hemo, com a colorant d'origen natural en diversos productes alimentaris. Els objectius del present treball eren, en primer lloc, determinar les millors condicions d'aplicació del procés de conservació de la FC mitjançant la deshidratació per atomització i caracteritzar físico-químicament i microbiològica el concentrat d'Hb en pols. En segon lloc, avaluar l'eficàcia de diferents additius antioxidants i/o segrestants del ferro per prevenir l'enfosquiment que pateix la FC durant la deshidratació. En tercer lloc, aplicar tractaments d'altes pressions hidrostàtiques com a procés d'higienització i avaluar els efectes d'aquest tractament sobre la microbiota contaminant, el color i les propietats funcionals de la FC. Finalment, desenvolupar un procés d'obtenció d'hidrolitzats proteics descolorats a partir de l'Hb amb la finalitat d'utilitzar-los com a ingredients nutricionals i/o funcionals. La millor temperatura de deshidratació per atomització de la FC hemolitzada era 140ºC. La FC en pols presentava un contingut en humitat del 5,3 % i un percentatge de solubilitat proteica del 96 %. La deshidratació per atomització induïa canvis en l'estructura nativa de l'Hb i, per tant, un cert grau de desnaturalització que pot conduir a una disminució de les seves propietats funcionals. L'extracte sec de la FC en pols estava composat per un 94,6 % de proteïna, un 3 % de sals minerals i un 0,7 % de greix. Els valors CIE L*a*b* del color de la FC en pols eren força constants i reflectien el color vermell marró fosc d'aquesta, a causa de l'oxidació del ferro hèmic que es produeix durant la deshidratació. La càrrega contaminant de la FC fresca de la sang de porc era força elevada i el tractament d'hemòlisi amb ultrasons i la centrifugació posterior no produïen una reducció significativa de la microbiota contaminant, obtenint un producte amb uns recomptes microbiològics de l'ordre de 106 ufc·mL-1. La deshidratació per atomització produïa una disminució d'una unitat logarítmica dels recomptes totals de la FC hemolitzada. Tanmateix, el producte en pols encara reflectia l'elevada contaminació de la primera matèria, fet que condiciona negativament la seva utilització com a ingredient alimentari, a no ser que es millorin les condicions de recollida de la sang a l'escorxador o que aquesta o la FC es sotmeti a algun tractament d'higienització prèviament a la deshidratació. Les isotermes de sorció a 20ºC de la FC en pols tenien forma sigmoïdal i una histèresi estreta i llarga. L'equació GAB és un bon model matemàtic per ajustar les dades de sorció obtingudes experimentalment i determinar la isoterma d'adsorció de la FC deshidratada per atomització. El percentatge d'humitat de la FC deshidratada a 140ºC es corresponia a un valor d'aw a 20 ºC d'aproximadament el 0,16. Tenint en compte que estava per sota dels valors d'aw corresponents a la capa monomolecular, es pot garantir la conservació a temperatura ambient del producte, sempre que s'envasi en recipients tancats que no permetin l'entrada d'humitat de l'exterior. De l'estudi de la possible estabilització del color de la FC deshidratada per atomització mitjançant l'addició d'antioxidants i/o segrestants de ferro, es va observar que només l'àcid ascòrbic, la glucosa, l'àcid nicotínic i la nicotinamida, tenien efectes positius sobre el color del producte en pols. L'ascòrbic i la glucosa no milloraven la conservació del color de l'Hb però disminuïen l'enfosquiment que es produeix durant la deshidratació, amb la qual cosa es pot obtenir un producte en pols de color marró més clar. L'addició de dextrina o L-cisteïna no disminuïa l'enfosquiment ni evitava el canvi de color de l'Hb. L'àcid nicotínic i la nicotinamida protegien el color de l'Hb durant el procés de deshidratació i l'emmagatzematge de la FC en pols. Les millors condicions d'aplicació del tractament amb altes pressions hidrostàtiques (HHP) sobre la FC eren 400 MPa, a 20ºC, durant 15 minuts, perquè produïen una millora significativa de la qualitat microbiològica, no afectaven negativament al color, no comprometien gaire la solubilitat proteica l'Hb i, malgrat que produïen un augment de la viscositat, la FC romania fluida després del tractament. Aquest tractament permetia una reducció de la microbiota contaminant de la FC d'entre 2 i 3 unitats logarítmiques. L'aplicació de l'alta pressió i la posterior deshidratació per atomització permetien obtenir un producte en pols amb recomptes totals de l'ordre de 2,8 unitats logarítmiques. El color de la FC pressuritzada en pols era igual que el de la FC control deshidratada, perquè ambdues mostres presentaven la mateixa susceptibilitat a l'oxidació del grup hemo produïda per la deshidratació. L'alta pressió incrementava la susceptibilitat de l'Hb als efectes desnaturalitzants de la deshidratació, fonamentalment a pH 7 (PIE), ja que es va observar una disminució de la solubilitat proteica a pH neutre després dels 2 processos tecnològics. La FC en pols presentava una màxima capacitat escumant al PIE de l'Hb. L'aplicació del tractament HHP produïa una disminució de la capacitat escumant de la FC en pols, però no tenia efectes negatius sobre l'estabilitat de l'escuma formada. Tampoc es van observar efectes negatius del tractament HHP sobre l'activitat emulsionant de l'Hb. La màxima activitat emulsionant de l'Hb s'aconseguia amb una concentració de FC en pols de l'1,5 % a pH 7 i de l'1 % a pH 4,5. Les pastes obtingudes per escalfament de la FC presentaven característiques molt diferenciades depenent del pH. A pH neutre es formaven unes pastes dures i consistents, mentre que a pH àcid les pastes eren poc consistents, molt adhesives i més elàstiques que les anteriors. Aquestes tenien una capacitat de retenció d'aigua molt superior que les de pH 7, en les quals l'aigua quedava retinguda per capil·laritat. La textura i capacitat de retenció d'aigua de les pastes tampoc eren afectades pel tractament HHP. El tractament HHP incrementava l'activitat de la Tripsina sobre l'Hb quan el substrat i l'enzim es tractaven conjuntament i afavoria el procés d'obtenció d'hidrolitzats descolorats a partir de la FC, la qual cosa permetia assolir el mateix grau de descoloració amb una dosi d'enzim inferior. El tractament d'hidròlisi de la FC amb la utilització combinada de Tripsina seguida d'un tractament amb Pepsina permetia l'obtenció d'un hidrolitzat proteic d'Hb descolorat i hidrolitzava completament la globina, donant lloc a 2 pèptids de 10,8 i 7,4 KDa. Val a dir que també produïa un 60 80 % de nitrogen soluble en TCA, constituït fonamentalment per pèptids petits i aminoàcids lliures. Els hidrolitzats trípsics i pèpsics d'Hb, obtinguts a partir de FC no pressuritzada i deshidratats per atomització a 180ºC, eren de color blanc i tenien un contingut en humitat del 4,7 %, un 84,2 % de proteïna i 9,7 % de sals minerals. El procés d'hidròlisi permetia una reducció considerable de la contaminació de la FC, obtenint un producte en pols amb uns recomptes totals de l'ordre de 102-103 ufc·g-1. Pel que fa a la funcionalitat dels hidrolitzats d'Hb deshidratats per atomització, aquests presentaven una elevada solubilitat proteica a pH 5 i 7 i romanien solubles després d'un escalfament a 80ºC durant 30 min. Tanmateix, aquesta hidròlisi afectava molt negativament la capacitat de mantenir escumes estables i l'activitat emulsionant.

Low molecular weight organogelators from self-assembling synthetic tripeptides with coded amino acids: morphological, structural, thermodynamic and spectroscopic investigations

A series of self-assembling terminally blocked tripeptides (containing coded amino acids) form gels in various aromatic solvents including benzene, toluene, xylenes at low concentrations. However these tripeptides do not form gels in aliphatic hydrocarbons like n-hexane, cyclohexane, n-decane etc. Morphological studies of the dried gel indicate the presence of an entangled fibrous network, which is responsible for gelation. Differential scanning calorimetric (DSC) studies of the gels produced by peptide 1 clearly demonstrates thermoreversible nature of the gel and tripeptide-solvent complex may be produced during gel formation. FT-IR and H-1 NMR studies of the gels demonstrate that an intermolecular hydrogen-bonding network is formed during gelation. Single crystal X-ray diffraction studies for peptides 1, 2 and 3 have been performed to investigate the molecular arrangement that might be responsible for forming the fibrous network of these self-assembling peptide gelators. It has been found that the morph responsible for gelation of peptides 1, 2 and 3 in benzene is somewhat different from that of its xerogel.

Simulating the formation of secondary organic aerosol from the photooxidation of aromatic hydrocarbons

The formation and composition of secondary organic aerosol (SOA) from the photooxidation of benzene, p-xylene, and 1,3,5-trimethylbenzene has been simulated using the Master Chemical Mechanism version 3.1 (MCM v3.1) coupled to a representation of the transfer of organic material from the gas to particle phase. The combined mechanism was tested against data obtained from a series of experiments conducted at the European Photoreactor (EUPHORE) outdoor smog chamber in Valencia, Spain. Simulated aerosol mass concentrations compared reasonably well with the measured SOA data only after absorptive partitioning coefficients were increased by a factor of between 5 and 30. The requirement of such scaling was interpreted in terms of the occurrence of unaccounted-for association reactions in the condensed organic phase leading to the production of relatively more nonvolatile species. Comparisons were made between the relative aerosol forming efficiencies of benzene, toluene, p-xylene, and 1,3,5-trimethylbenzene, and differences in the OH-initiated degradation mechanisms of these aromatic hydrocarbons. A strong, nonlinear relationship was observed between measured (reference) yields of SOA and (proportional) yields of unsaturated dicarbonyl aldehyde species resulting from ring-fragmenting pathways. This observation, and the results of the simulations, is strongly suggestive of the involvement of reactive aldehyde species in association reactions occurring in the aerosol phase, thus promoting SOA formation and growth. The effect of NO, concentrations on SOA formation efficiencies (and formation mechanisms) is discussed.

Electrocombustion of humic acid and removal of algae from aqueous solutions

This paper reports experiments involving the electrochemical combustion of humic acid (HA) and removal of algae from pond water. An electrochemical flow reactor with a boron-doped diamond film anode was used and constant current experiments were conducted in batch recirculation mode. The mass transfer characteristics of the electrochemical device were determined by voltammetric experiments in the potential region of water stability, followed by a controlled current experiment in the potential region of oxygen evolution. The average mass transfer coefficient was 5.2 x 10(-5) m s(-1). The pond water was then processed to remove HA and algae in the conditions in which the reaction combustion occurred under mass transfer control. To this end, the mass transfer coefficient was used to estimate the initial limiting current density applied in the electrolytic experiments. As expected, all the parameters analyzed here-solution absorbance at 270 nm, total phenol concentration and total organic carbon concentration-decayed according to first-order kinetics. Since the diamond film anode successfully incinerated organic matter, the electrochemical system proved to be predictable and programmable.

Solubilizacao e interacao de pigmentos com solventes organicos e agentes tenso-ativos

A Mg e Mn-Ftalocianina (Mg e Mn-Pc) foram solubilizados à 25°C em dimetilsulfóxido (DMSO); N, N-dimetilacetamida (DMA); N,N-dimetilformamida (DMF); N-metil-formamida, formamida, piridina, o-diclorobenzeno, monoclorobenzeno, tolueno, metanol, etanol, propanol-1, propanol-2, butanol-1 e octanol-1. Alguns valores representativos obtidos para o logarítimo da absortividade molar (E) da Mn-Pc, são os seguintes: o-diclorobenzeno (E = 4,94); DMSO (E = 4,39); octanol-1 (E = 3,90). Valores correspondentes para Mg-Pc são: o-diclarobenzeno (E = 4,93); DMSO (E = 5,22) e Octanol-1 ( E = 5,06). Em função de interação com solventes, pode-se classificar a Mg-Pc como um indicador básico e a Mn-Pc como indicador ácido. Os pigmentos Mg e Mn-Pc foram também solubillzados em soluções aquosas contendo vários surfatantes à 25°C. A Mg-Pc apresentou solubilidade significativa em água contendo brometo de cetiltrimetilamônio (CTAB), Brij-35, cloreto de cetilpiridinio (CPC1), brometo de cetilpiridínio (CPBr,) Triton X-100, cloreto de metildodecilbenziltrimetilamônio, brometo de cetildimetiletilamõnio e brometo de laurilisoquinolínio. A Mn-Pc foi solúvel em soluções aquosas de Brij-35 e Triton X-100. Em função de sua interação com surfatantes a Mg-Pc é classificada como corante catiônico e a Mn-Pc como corante aniônico. O corante comercial quinóide Oil Blue A [1,4-di(isopropilarnina)-antraquinona - 9,10 foi solubilizado à 25°C em DMF, DMSO, DMA, monoclorobenzeno, benzeno, tolueno, piridina, metanol, etanol, propanol-1, propanol-2, butanol-1 e octanol-1. Foi também solubilizado em soluções aquosas de surfatantes, tais como sódio lauril-sulfato (NaLS), cloreto de cetiltrimetilamônio (CTAB), brometo de cetildimetiletilamônio, Triton X-100, cloreto de cetilpiridínio (CPCl), Brij-35, cloreto de rnetildodecilbenziltrimetilamônio e brometo de laurilisoquinolínio. Em função de suas interações com os solventes o corante é um indicador ácido-básico pouco sensível e em função de sua interação com surfatantes é um corante catiônico. 0s resultados experimentais apresentam importância teórica e prática considerando sistemas que envolvem armazenamento e transferência de energia, compostos porfirínicos, fotossíntese, fotocondutores, coletores solares, semi-condutores e processos de embelezamento e proteção de superficies de vários materiais.

Uso de argilominerais e diatomita como adsorvente de fenóis em águas produzidas na indústria de petróleo

The oil production in Brazil has been increasing each year. Consequently, increasing volumes of water produced are generated with large quantities of contaminants, which brings many problems in disposing of these waters. The concern that the concentrations of contaminants in water produced meet existing laws for disposal of effluents, has been extremely important for the development of different techniques for treatment of water produced. The study of clay minerals as adsorbents of organic contaminants has grown considerably so in order to combine the low cost with the efficiency of environmental preservation and health issues. Thus, this study aims to understand the characteristics of vermiculite clay, sodium bentonite, calcium bentonite and diatomite and evaluate their performance as adsorbents for phenol in the water produced. Through adsorption isotherms it was possible to observe the behavior of these adsorptive clay and diatomite for adsorption of phenol, the main phenolic compound found in water produced. Different concentrations of synthetic solutions of phenol were put in touch with these adsorbents under same conditions of agitation and temperature. The adsorbents were composted adsorptive favorable, but the vermiculite and diatomite showed little capacity for absorption, being suggested for absorbs small concentrations of phenol in the balance isothermal

Rejeito de xisto como adsorvente para remoção de fenol em águas produzidas na indústria de petróleo

Produced water is the main effluent linked to the activity of extraction of oil and their caring management is necessary due to the large volume involved, to ensure to minimize the negative impacts of discharges of these waters in the environment. This study aimed to analyze the use of retorted shale, which is a reject from the pyrolysis of pirobituminous shale, as adsorbent for the removal of phenols in produced water. The material was characterized by different techniques (grain sized analysis, thermal analysis, BET, FRX, FT-IR, XRD and SEM), showing the heterogeneity in their composition, showing its potential for the removal of varied compounds, as well as the phenols and their derivatives. For the analysis of the efficiency of the oil shale for the adsorption process, assays of adsorption balance were carried through, and also kinetic studies and dynamics adsorption, in the ETE of the UTPF of Petrobras, in Guamaré-RN. The balance assays shown a bigger conformity with the model of Langmuir and the kinetic model more adjusted to describe the adsorption of phenols in retorted shale was of pseudo-second order. The retorted shale presented a low capacity of adsorption of phenols (1,3mg/g), when related to others conventional adsorbents, however it is enough to the removal of these composites in concentrations presented in the produced water of the UTPF of Guamaré. The assays of dynamics adsorption in field had shown that the concentration of phenol in the effluent was null until reaching its rupture (58 hours). The results showed the possibility of use of the reject for removal of phenols in the final operations of the treatment process, removing as well, satisfactorily, the color and turbidity of the produced water, with more than 90% of removal

Estudo de adsorvente obtido de terras diatomáceas para remoção de metais pesados em águas produzidas: processamento, caracterização e dinâmica em leito fixo

The acceleration of industrial growth in recent decades on all continents aroused the interest of the companies to counter the impacts produced on the environment, spurred primarily by major disasters in the petroleum industry. In this context, the water produced is responsible for the largest volume of effluent from the production and extraction of oil and natural gas. This effluent has in its composition some critical components such as inorganic salts, heavy metals (Fe, Cu, Zn, Pb, Cd, ), presence of oil and chemicals added in the various production processes. In response to impact, have been triggered by research alternative adsorbent materials for water treatment and water produced, in order to removing oils and acids and heavy metals. Many surveys of diatomaceous earth (diatomite) in Brazil involve studies on the physico-chemical, mineral deposits, extraction, processing and applications. The official estimated Jazi are around 2.5 million tonnes, the main located in the states of Bahia (44%) and Rio Grande do Norte (37,4%). Moreover, these two states appear as large offshore producers, earning a prominent role in research of adsorbents such as diatomite for treatment of water produced. Its main applications are as an agent of filtration, adsorption of oils and greases, industrial load and thermal insulator. The objective of this work was the processing and characterization of diatomite diatomaceous earth obtained from the municipality of Macaíba-RN (known locally as tabatinga) as a low cost regenerative adsorbent for removal of heavy metals in the application of water produced treatment. In this work we adopted a methodology for batch processing, practiced by small businesses located in producing regions of Brazil. The characterization was made by X-ray diffraction (XRD), scanning electron microscopy (SEM) and specific surface area (BET). Research conducted showed that the improvement process used was effective for small volume production of diatomite concentrated. The diatomite obtained was treated by calcination at temperature of 900 oC for 2 hours, with and without fluxing Na2CO3 (4%), according to optimal results in the literature. Column adsorption experiments were conducted to percolation of the in nature, calcined and calcined fluxing diatomites. Effluent was used as a saline solution containing ions of Cu, Zn, Na, Ca and Mg simulating the composition of produced waters in the state of Rio Grande do Norte, Brazil. The breakthrough curves for simultaneous removal of copper ions and zinc as a result, 84.3% for calcined diatomite and diatomite with 97.3 % for fluxing. The calcined fluxing diatomite was more efficient permeability through the bed and removal of copper and zinc ions. The fresh diatomite had trouble with the permeability through the bed under the conditions tested, compared with the other obtained diatomite. The results are presented as promising for application in the petroleum industry

Avaliação preliminar da contaminação por BTEX, em água subterrânea de poços tubulares, no município de Natal-RN

Among the different types of pollutants typically attributed to human activities, the petroleum products are one of the most important because of its toxic potential. This toxicity is attributed to the presence of substances such as benzene and its derivatives are very toxic to the central nervous system of man, with chronic toxicity, even in small concentrations. The area chosen for study was the city of Natal, capital of Rio Grande do Norte, where samples were collected in six different areas in the city, comprising 10 wells located in the urban area, being carried out in three distinct periods March/2009, December / June/2010 and 2009, and were evaluated for contamination by volatile hydrocarbons (BTEX - benzene, toluene, ethylbenzene and xylenes), so this work aimed to assess the quality of groundwater wells that supply funding for public supply and trade in the urban area of the city of Natal, in Rio Grande do Norte, contributing to the environmental assessment of the municipality. The analysis of BTEX in water was performed according to EPA Method 8021b. Was used the technique of headspace (TriPlus TP100) coupled to high resolution gas chromatography with selective photoionization detector (PID) and flame ionization (FID) - model Trace GC Ultra, Thermo Electron Corporation brand. The procedure adopted allowed the detection of concentrations of the order of μg.L-1. Data analysis with respect to BTEX in groundwater in the area monitored so far, shows that water quality is still preserved, because it exceeds the limits imposed by the potability Resolution CONAMA Nº. 396, April 2008

Avaliação de HPA e BTEX no solo e água subterrânea, em postos de revenda de combustíveis: estudo de caso na cidade de Natal -RN

The retail fuel stations are partially or potentially polluters and generators of environmental accidents, potentially causing contamination of underground and surface water bodies, soil and air. Leaks in fuel retail stations´ underground storage systems are often detected in Brazil and around the world. Monoaromatic hydrocarbons, BTEX (benzene, toluene, ethylbenzene and xylenes) and polycyclic aromatic hydrocarbons (PAHs) are an indication of the presence of contamination due to its high toxicity. This paper presents a case study of contamination in a Fuel Retail Station by petroleum derivative products in the city of Natal. For identification and quantification of the hydrocarbons, EPA analytical methods were used. The values of benzene quantified by EPA method 8021b CG-PID/FID, ranged from 1.164 to 4.503 mg.Kg-1 in soil samples, and from 12.10 to 27,639 μg.L-1 in underground water samples. Among the PAHs, naphthalene and anthracene showed the most significant results in soil samples, 0.420 to 15.46 mg.Kg-1 and 0.110 to 0,970 mg.Kg-1, respectively. In underground water samples, the results for Naphthalene varied between 0.759 and 614.7 μg.L-1. PAHs were quantified by EPA Method 8270 for GCMS. All of the results for the chemical analysis were compared with the values for the CONAMA 420/2009 resolution. The results for benzene (27,639 μg.L-1) showed levels highly above the recommended by the CONAMA 420 resolution, wherein the maximum permissible for underground water is 5 μg.L-1. This is a worrying factor, since underground water makes up 70% of the city of Natal´s water supply

Tratamento eletroquímico de efluente proveniente de caixas separadoras de água e óleo de postos revendedores de combustíveis

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior

Aplicação de técnicas eletroquímicas na determinação do potencial de corrosividade de ligas de alumínio em água produzida

The resistance of aluminum and their alloys, to the corrosion phenomenon, in aqueous solutions, is a result of the oxide layer formed. However, the corrosion process in the aluminum alloy is associated with the presence a second phase of particles or the presence of chloride ions which promote the disruption of the oxide layer located producing the corrosion process. On the other hand, the term water produced is used to describe the water after the separation of the oil and gas in API separators. The volumes of produced water arrive around 5 more times to the volume of oil produced. The greatest feature of the water is the presence of numerous pollutants. Due to the increased volume of waste around the world in the current decade, the outcome and the effect of the discharge of produced water on the environment has recently become an important issue of environmental concern where numerous treatments are aimed at reducing these contaminants before disposal. Then, this study aims to investigate the electrochemical corrosion behavior of aluminum alloy 6060 in presence of water produced and the influence of organic components as well as chloride ions, by using the electrochemical techniques of linear polarization. The modification of the passive layer and the likely breakpoints were observed by atomic force microscopy (AFM). In the pit formation potential around -0.4 to -0.8 V/EAg/AgCl was observed that the diffusion of chloride ions occurs via the layer formed with the probable formation of pits. Whereas, at temperatures above 65 °C, it was observed that the range of potential for thepit formation was -0.4 to -0.5 V/EAg/AgCl. In all reactions, the concentration of Al(OH)3 in the form of a gel was observed

Estudo do efeito dos metabólitos do benzeno e tolueno sobre as mitocôndris cerebrais e hepáticas de ratos

Aim: The aim of this work was to investigate the hypothesis that catechol and 3MC inhibit FADH2-linked basal respiration in mitochondria isolated from rat liver and brain homogenates. Moreover, catechol ability to induce DNA damage in rat brain cells through the comet assay (alkaline single-cell gel electrophoresis assay) was also observed. Methods: Two different catechols were evaluated: pirocatechol (derived from benzene) and 3-methylcatechol (derived from toluene); rat liver and brain homogenates were incubated with 1mM catechol at pH 7.4 for up to 30 minutes. After that, mitochondrial fractions were isolated by differential centrifugation. Basal oxygen uptake was measured using a Clark-type electrode after the addition of 10 mM sodium succinate for a period of 12 minutes. In additional experiments, rat brain cells were treated with 1, 5 and 10mM pirocatechol for up to 20 minutes at 37º C, and submitted to electrophoresis. Results: Catechols (pirocatechol and 3methylcatechol) induced a time-dependent partial inhibition of FADH2-linked basal mitochondrial respiration. Indeed, pirocatechol was able to produce a dosedependent DNA oxidative damage in rat brain cells by 2 and 4 injury levels. These results suggest that reactive oxygen species generated by the oxidation of catechols, induced an impairment on mitochondrial respiration and a DNA damage, which might be related to their citotoxicity. Conclusion: Catechols produced an inhibition of basal respiration associated to FADH2 in isolated liver and brain mitochondria; 3-methylcatechol, at the same concentration, produced similar toxicity in the mitochondrial model. Indeed, pirocatechol induced a DNA damage in rat brain cells, mainly observed in comets formation and consequent DNA degradation

Remoção de óleo da água de produção por flotação em coluna utilizando tensoativos de origem vegetal

In the petroleum industry, water is always present in the reservoir formation together with petroleum and natural gas and this fact provokes the production of water with petroleum, resulting in a great environmental impact. Several methods can be applied for treatment of oily waters, such as: gravitational vases, granulated media filtration systems, flotation process, centrifugation process and the use of hydrocyclones, which can also be used in a combined way. However, the flotation process has showed a great efficiency as compared with other methods, because these methods do not remove great part of the emulsified oil. In this work was investigated the use of surfactants derived from vegetable oils, OSS and OGS, as collectors, using the flotation process in a glass column with a porous plate filter in its base for the input of the gaseous steam. For this purpose, oil/water emulsions were prepared using mechanical stirring, with concentrations around 300 ppm. The air flow rate was set at 700 cm3/min and the porous plate filter used for the generation of the air bubbles has pore size varying from 16 to 40 Pm. The column operated at constant volume (1500mL). A new methodology has been developed to collect the samples, where, instead of collecting the water phase, it was collected the oil phase removed by the process in the top of the flotation column. It has been observed that it is necessary to find an optimum surfactant concentration to achieve enhanced removal efficiency. Being for OSS 1.275 mmol/L and for OGS 0.840 mmol/L, with removal efficiencies of 93% and 99%, respectively, using synthetic solutions. For the produced water, the removal in these concentrations was 75% for OSS and 65% for OGS. It is possible to remove oil from water in a flotation process using surfactants of high HLB, fact that is against the own definition of HLB (Hydrophile-Lipophile Balance). The interfacial tension is an important factor in the oil removal process using a flotation process, because it has direct interference in the coalescence of the oil drops. The spreading of the oil of the air bubble should be considered in the process, and for the optimum surfactant concentrations it reached a maximum value. The removal kinetics for the flotation process using surfactants in the optimum concentration has been adjusted according to a first order model, for synthetic water as for the produced water.

Aperfeiçoamento no projeto de um protótipo de misturador-decantador à inversão de fases visando aplicação na indústria do petróleo

In the oil industry the mixture oil/water occurs in the operations of production, transportation and refining, as well as during the use of its derivatives. The amount of water produced associated with the oil varies and can reach values of 90% in volume in the case of mature phase of the production fields. The present work deals with the development of new design of the Mixer Settler based on Phase Inversion (MDIF) in a laboratory scale. We envisage this application in industrial scale so the phases of project, construction and operation are considered. The modifications most significant, in comparison with the original prototype, include the materials of construction and the substitution of the equipment used in the mixing stage of the process. It was tested the viability of substitution of the original system of mechanical mixing by a static mixer. A statistical treatment by means of an experimental design of composed central type was used in order to evaluate the behavior of the main variables of the separation process as function of the efficiency of separation for the new device. This procedure is useful to delimit an optimal region of operation with the equipment. The variables of process considered on the experimental design were: oil concentration in the feeding water (mg/L); Total volumetric flow rate (L/h); Ratio organic/water on volumetric basis (O/A). The separation efficiency is calculated by comparison of the content of oil and greases in the inlet and outlet of the equipment. For determination of TOG (Total Oil and Grease), the method used was based in the absorption of radiation in the infra-red region. The equipment used for these determinations was InfraCal® TOG/TPH Model HATR-T2 of the Wilks Enterprise, Incorporation. It´s important to stand out that this method of measure has being used by PETROBRAS S.A. Results of global efficiency of separation oil/water varied from 75.3 to 97.7% for contaminated waters containing up to 1664,1 mg/L of oil. By means of tests carried out with a real sample of contaminated water supplied by PETROBRAS we have got an effluent specified in terms of the legal standards required for discharging. Thus, the new design of equipment constitutes a real alternative for the conventional systems of treatment of produced water in the oil industry