1000 resultados para recuperação de amido


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The success achieved by thermal methods of recovery, in heavy oils, prompted the emergence of studies on the use of electromagnetic waves as heat generating sources in oil reservoirs. Thus, this generation is achieved by three types of different processes according to the frequency range used. They are: the electromagnetic induction heating, the resistive and the dielectric, also known as radiation. This study was based on computer simulations in oil reservoirs with characteristics similar to those found in the sedimentary basins of the Brazilian Northeast. All cases studied were simulated using the software STARS, CMG (Computer Group, version 2012.10 Modeling). Some simulations took into account the inclusion of electrically sensitive particles in certain sectors of the reservoir model studied by fracturing. The purpose of this work is the use of the electromagnetic induction heating as a recovery method of heavy oil, to check the influence of these aforementioned particles on the reservoir model used. Comparative analyses were made involving electromagnetic induction heating, the operation of hydraulic fracturing and the injection of water to the different situations of the reservoir model studied. It was found that fracturing the injection well in order that the electromagnetic heating occurs in the same well where there is water injection, there was a considerable increase in the recovery factor and in the cumulative oil production in relation to the models in which hydraulic fracturing occurred in the production well and water injection in the injection well. This is due to the generation of steam in situ in the reservoir.

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The growing interest and applications of biotechnology products have increased the development of new processes for recovery and purification of proteins. The expanded bed adsorption (EBA) has emerged as a promising technique for this purpose. It combines into one operation the steps of clarification, concentration and purification of the target molecule. Hence, the method reduces the time and the cost of operation. In this context, this thesis aim was to evaluate the recovery and purification of 503 antigen of Leishmania i. chagasi expressed in E. coli M15 and endotoxin removal by EBA. In the first step of this study, batch experiments were carried out using two experimental designs to define the optimal adsorption and elution conditions of 503 antigen onto Streamline chelating resin. For adsorption assays, using expanded bed, it was used a column of 2.6 cm in diameter by 30.0 cm in height coupled to a peristaltic pump. In the second step of study, the removal of endotoxin during antigen recovery process was evaluated employing the non-ionic surfactant Triton X-114 in the washing step ALE. In the third step, we sought developing a mathematical model able to predict the 503 antigen breakthrough curves in expanded mode. The experimental design results to adsorption showed the pH 8.0 and the NaCl concentration of 2.4 M as the optimum adsorption condition. In the second design, the only significant factor for elution was the concentration of imidazole, which was taken at 600 mM. The adsorption isotherm of the 503 antigen showed a good fit to the Langmuir model (R = 0.98) and values for qmax (maximum adsorption capacity) and Kd (equilibrium constant) estimated were 1.95 mg/g and 0.34 mg/mL, respectively. Purification tests directly from unclarified feedstock showed a recovery of 59.2% of the target protein and a purification factor of 6.0. The addition of the non-ionic surfactant Triton X-114 to the washing step of EBA led to high levels (> 99%) of LPS removal initially present in the samples for all conditions tested. The mathematical model obtained to describe the 503 antigen breakthrough curves in Streamline Chelanting resin in expanded mode showed a good fit for both parameter estimation and validation steps. The validated model was used to optimize the efficiencies, achieving maximum values of the process and of the column efficiencies of 89.2% and 75.9%, respectively. Therefore, EBA is an efficient alternative for the recovery of the target protein and removal of endotoxin from an E. coli unclarified feedstock in just one step.

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Sandstone-type reservoir rocks are commonly responsible for oil accumulation. The wettability is an important parameter for the physical properties of the container, since it interferes in characteristics such as relative permeability to the aqueous phase, residual oil distribution in the reservoir, operating characteristics with waterflood and recovery of crude oil. This study applied different types of microemulsion systems - MES - in sandstone reservoirs and evaluated their influences on wettability and residual oil recovery. For this purpose, four microemulsion were prepared by changing the nature of ionic surfactants (ionic and nonionic). Microemulsions could then be characterized by surface tension analysis, density, particle diameter and viscosity in the temperature range 30° C to 70° C. The studied oil was described as light and the sandstone rock was derived from the Botucatu formation. The study of the influence of microemulsion systems on sandstone wettability was performed by contact angle measurements using as parameters the rock treatment time with the MES and the time after the brine surface contact by checking the angle variation behavior. In the study results, the rock was initially wettable to oil and had its wettability changed to mixed wettability after treatment with MES, obtaining preference for water. Regarding rock-MES contact time, it was observed that the rock wettability changed more when the contact time between the surface and the microemulsion systems was longer. It was also noted only a significant reduction for the first 5 minutes of interaction between the treated surface and brine. The synthesized anionic surfactant, commercial cationic, commercial anionic and commercial nonionic microemulsion systems presented the best results, respectively. With regard to enhanced oil recovery performance, all systems showed a significant percentage of recovered oil, with the anionic systems presenting the best results. A percentage of 80% recovery was reached, confirming the wettability study results, which pointed the influence of this property on the interaction of fluids and reservoir rock, and the ability of microemulsion systems to perform enhanced oil recovery in sandstone reservoirs.

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Sandstone-type reservoir rocks are commonly responsible for oil accumulation. The wettability is an important parameter for the physical properties of the container, since it interferes in characteristics such as relative permeability to the aqueous phase, residual oil distribution in the reservoir, operating characteristics with waterflood and recovery of crude oil. This study applied different types of microemulsion systems - MES - in sandstone reservoirs and evaluated their influences on wettability and residual oil recovery. For this purpose, four microemulsion were prepared by changing the nature of ionic surfactants (ionic and nonionic). Microemulsions could then be characterized by surface tension analysis, density, particle diameter and viscosity in the temperature range 30° C to 70° C. The studied oil was described as light and the sandstone rock was derived from the Botucatu formation. The study of the influence of microemulsion systems on sandstone wettability was performed by contact angle measurements using as parameters the rock treatment time with the MES and the time after the brine surface contact by checking the angle variation behavior. In the study results, the rock was initially wettable to oil and had its wettability changed to mixed wettability after treatment with MES, obtaining preference for water. Regarding rock-MES contact time, it was observed that the rock wettability changed more when the contact time between the surface and the microemulsion systems was longer. It was also noted only a significant reduction for the first 5 minutes of interaction between the treated surface and brine. The synthesized anionic surfactant, commercial cationic, commercial anionic and commercial nonionic microemulsion systems presented the best results, respectively. With regard to enhanced oil recovery performance, all systems showed a significant percentage of recovered oil, with the anionic systems presenting the best results. A percentage of 80% recovery was reached, confirming the wettability study results, which pointed the influence of this property on the interaction of fluids and reservoir rock, and the ability of microemulsion systems to perform enhanced oil recovery in sandstone reservoirs.

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The objective of this randomized, blind and prospective clinical trial was to compare the pain, the edema, the mandibular movements, the masticatory efficiency and life quality, in the first 60 days after surgery using 2 different clinical protocols for myofunctional recovery, in patients who underwent orthognathic surgery. A sample of 19 patients was used and divided into 2 groups. The control group (CG) consisted of 10 patients who had postoperative rehabilitation guided by a standard protocol, conducted by the Service of Surgery and Traumatology Oral and Maxillofacial. In other hand, the experimental group (EC) totaled 9 patients who received the speech therapy rehabilitation protocol specialized, by professionals in the area. The variables pain, edema and mandibular movements were analyzed during 48h, 96h, 7 days, 14 days, 30 and 60 days post-surgery. The masticatory efficiency and the quality of life were classified with 60 days after surgery . The data were submitted an analysis of variance, Student's t-test and Fisher's independence, at the level of 5% probability. It was identified that patients of GE have benefited in the first 14 days(p<0,001), as they have had reported less pain than those in the CG. Significant statistics differences between groups for pain parameters (after 14 days) (p=0,065), edema(p=0,063), mandibular movements(p=0,068), masticatory efficiency(p=0,630) and the impact on quality of life (p=0,813) were not observed on this study. The speech therapy protocol for myofunctional recovery (EG), although it has not obtained statistical results superiors than the CG in the general context, presents itself as a viable alternative to conventional therapy assumed by many maxillofacial surgeons, allowing the surgeon to optimize time with patients in the period postoperatively.

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The recycling of metals from secondary sources can be advantageous. Among the metals of interest, we have cobalt, a metal used for various purposes. As regards the secondary sources of cobalt, the lithium-ion batteries can be considered, since they contain cobalt oxide in their composition (LiCoO2). This way, the objective of this work was to use the microorganism strains (Acidithiobacillus ferrooxidans and Acidithiobacillus thiooxidans) to bioleach the LiCoO2 extracted from discarded lithium ion batteries with emphasis on the recovery of cobalt for synthesis of new materials of interest. The lineage growth occurred in T&K medium and the growth investigation was made by observing the media, by platelet growth and microscope analysis. Then, the inoculum was standardized on 5 x 106 cells mL-1 and used in bioleaching tests. The bioleaching was investigated: the microorganism nature: separate strains and A. ferrooxidans and A. thiooxidans consortium, bioleaching time (0 to 40 days), inoculum proportion (5 to 50% v/v), energy source (iron and sulfur) and residue concentration (1063 to 8500 mg L-1 of cobalt). The cobalt concentration in the media was found by atomic absorption spectrometry and the medium pH was monitored during the bioleaching. The results show that the amount of bioleached cobalt increases with time and the iron concentration. The bioleaching with A. thiooxidans was not influenced by the addition of sulfur. The use of the two lineages together did not improve the bioleaching rates. Among the lineages, the A. thiooxidans presented better results and was able to bioleach cobalt amounts above 50% in most of the experiments. A. thiooxidans presented lower bioleaching rates, with a maximum of 50% after 24 days of experiment. After reprocessing by bioleaching, the cobalt in solution was used for synthesis of new materials: such as LiCoO2 cathode and as adsorbent pesticide double lamellar hydroxide (HDL Co-Al-Cl) by the Pechini and co-precipitation methods. The reprocessed LiCoO2 presented a unique stoichiometric phase relative to the HT-LiCoO2 structure similar to the JCPDS 44-0145, presenting electrochemical activity when tested as a cathode material. The double lamellar hydroxide Co-Al-Cl was tested as pesticide adsorbent, being possible to adsorb around 100% of the pesticide. The bioleaching was efficient in the recovery of cobalt present in lithium-ion batteries and microorganisms presented high tolerance to the residue, being able to bioleach even at higher LiCoO2 concentrations. The cobalt bioleaching medium did not impair the synthesis phases and the obtained materials presented structure and activity similar to the sintered materials from the reagents containing cobalt.

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Grande parte da energia contida no combustível consumido por um motor de combustão interna é desperdiçada sob forma de calor, através do sistema de refrigeração do motor, do sistema de recirculação dos gases de escape e principalmente através dos gases de escape. Daí o interesse no estudo de sistemas que permitem o aproveitamento dessa energia residual dos veículos automóveis. Este trabalho centra-se no estudo de sistemas de aproveitamento da energia térmica contida nos gases de escape dos veículos automóveis, sendo o objetivo principal o estudo do permutador de calor que será utilizado para recuperação da energia térmica. Existem vários tipos de permutadores, na sua escolha entram fatores como as características dos fluidos de trabalho envolvidos, o custo, facilidade de manutenção, a aplicação. Para o caso deste estudo selecionou-se um permutador de carcaça e tubos e um permutador de tubos concêntricos. Uma vez que a seleção e otimização de um permutador de calor implica a minimização da perda de carga dos gases de escape e a maximização da eficiência térmica do sistema, numa primeira fase selecionou-se a geometria mais adequada. Em seguida fez-se uma comparação de diferentes modelos de cálculo da perda de carga e analisou-se o desempenho termo hidráulico do permutador. Por fim realizou-se um estudo paramétrico para verificar a influência dos parâmetros de construção (número de tubos, diâmetro e comprimento dos tubos).

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NASCIMENTO, Bruna Laís C. do; FELIPE, Carla Beatriz Marques; BEZERRA, Midinai Gomes.Política de indexação: visando a qualidade para a recuperação da informação. In: SEMINÁRIO DE PESQUISA DO CCSA, 16., 2010, Natal. Anais eletrônicos... Natal: UFRN, 2010. Disponível em:.

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v. 17, n .2, p. 164-174, abr./jun. 2016.

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The main objective of this work is the development of a hardmetal components (WC-6%Co) recovery method by thermal deposition process. The thermal deposition technique used was HVOF (high velocity oxygen-fuel). The HVOF enables depositions of thick coatings (100-500 µm) with low porosity levels, high hardness and excellent adhesion. Before deposition, hardmetal samples with different geometries (plates and cylinders) were finished in order to have different roughness. The influence of these parameters in adhesion was studied. After this step, different re-sintering temperatures were used, in order to determine which one allows to obtain the maxima densification, elements distribution and metallurgical bonding. The re-sintering promotes the densification of the coating, with an increase of its hardness and metallurgical bonding formation. The inclusion of an intermetallic layer was tested along with different layer parameters. In liquid phase sintering (1383 and 1455 ºC) a complete densification of the coating occurred, while a bonding between the substrate and the coating only partially happened. The results of SEM/EDS show low levels of porosity and a complete and uniform distribution of the elements of the alloy. The cylindrical samples without intermetallic layer showed the lowest level of porosity and best metallurgical bonding. When the substrate surface was polished (Ra = 0.05 mm) lower levels of porosity and greater metallurgical bonding were found for both geometries. Taking into account the results obtained in this study, we can conclude that the implementation of this process is appropriate for cylindrical components with a polished surface. In these components the intermetallic layer is unnecessary and punctual defects like pores can be repaired with this process.

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NASCIMENTO, Bruna Laís C. do; FELIPE, Carla Beatriz Marques; BEZERRA, Midinai Gomes.Política de indexação: visando a qualidade para a recuperação da informação. In: SEMINÁRIO DE PESQUISA DO CCSA, 16., 2010, Natal. Anais eletrônicos... Natal: UFRN, 2010. Disponível em:.

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Although the transition metal chemistry of many dialkylamido ligands has been well studied, the chemistry of the bulky di(tert-butyl)amido ligand has been largely overlooked. The di(tert-butyl)amido ligand is well suited for synthesizing transition metal compounds with low coordination numbers; such compounds may exhibit interesting structural, physical, and chemical properties. Di(tert-butyl)amido complexes of transition metals are expected to exhibit high volatilities and low decomposition temperatures, thus making them well suited for the chemical vapor deposition of metals and metal nitrides. Treatment of MnBr₂(THF)₂, FeI₂, CoBr₂(DME), or NiBr₂(DME) with two equivalents of LiN(t-Bu)2 in benzene affords the two-coordinate complex M[N(t-Bu)₂]₂, where M is Mn, Fe, Co, or Ni. Crystallographic studies show that the M-N distances decrease across the series: 1.9365 (Mn), 1.8790 (Fe), 1.845 (Co), 1.798 Å (Ni). The N-M- N angles are very close to linear for Mn and Fe (179.30 and 179.45°, respectively), but bent for Co and Ni (159.2 and 160.90°, respectively). As expected, the d⁵ Mn complex has a magnetic moment of 5.53 μΒ that is very close to the spin only value. The EPR spectrum is nearly axial with a low E/D ratio of 0.014. The d⁶ Fe compound has a room temperature magnetic moment of 5.55 μΒ indicative of a large orbital angular momentum contribution. It does not exhibit a Jahn-Teller distortion despite the expected doubly degenerate ground state. Applied field Mössbauer spectroscopy shows that the effective internal hyperfine field is unusually large, Hint = 105 T. The magnetic moments of Co[N(t-Bu)₂]₂ and Ni[N(t-Bu)₂]₂ are 5.24 and 3.02 μΒ respectively. Both are EPR silent at 4.2 K. Treatment of TiCl₄ with three equivalents of LiN(t-Bu)2 in pentane affords the briding imido compound Ti₂[μ-N(t-Bu)]₂Cl₂[N(t-Bu)₂]₂ via a dealkylation reaction. Rotation around the bis(tert-butyl)amido groups is hindered, with activation parameters of ΔH‡ = 12.8 ± 0.6 kcal mol-1 and ΔS‡ = -8 ± 2 cal K-1 ·mol-1, as evidenced by variable temperature 1H NMR spectroscopy. Treatment of TiCl₄ with two equivalents of HN(t-Bu)₂ affords Ti₂Cl₆[N(t-Bu)₂]₂. This complex shows a close-contact of 2.634(3) Å between Ti and the carbon atom of one of the CH₃ substituents on the tert-butyl groups. Theoretical considerations and detailed structural comparisons suggest this interaction is not agostic in nature, but rather is a consequence of interligand repulsions. Treatment of NiI₂(PPh3)₂ and PdCl₂(PPh₃)₂ with LiN(t-Bu)₂in benzene affords Ni[N(t-Bu)₂](PPh₃)I and Pd₃(μ₂-NBut₂)2(μ₂-PPh₂)Ph(PPh₃) respectively. The compound Ni[N(t-Bu)₂](PPh₃)I has distorted T-shape in geometry, whereas Pd₃(μ₂-NBut₂)₂(μ₂-PPh₂)Ph(PPh₃) contains a triangular palladium core. Manganese nitride films were grown from Mn[N(t-Bu)₂]₂ in the presence of anhydrous ammonia. The growth rate was several nanometers per minute even at the remarkably low temperature of 80⁰C. As grown, the films are carbon- and oxygen-free, and have a columnar morphology. The spacings between the columns become smaller and the films become smoother as the growth temperature is increased. The composition of the films is consistent with a stoichiometry of Mn₅N₂.

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O objetivo deste trabalho foi utilizar diferentes técnicas químicas (dimetilsulfóxido, ácido clorídrico, acético e lático), técnicas mecânicas (banho ultrassônico, abrasão com pérolas de vidro, maceração com terra diatomácea, ruptor ultrassônico e imersão em nitrogênio líquido) e técnica enzimática (preparado enzimático comercial Glucanex®) para a recuperação de carotenoides a partir da ruptura da parede celular das leveduras Sporidiobolus pararoseus e Rhodotorula mucilaginosa isoladas de amostras ambientais. Para isso a obtenção de biomassa foi realizada através de cultivos submersos no meio YM, a 25 °C, 180 rpm por 168 h. Para a ruptura celular, a operação de congelamento da biomassa (-18°C por 48 h) foi estudada. Os métodos de secagem convencional por ar forçado (35°C/48h) e liofilização (-80°C/48h, em ultrafreezer, seguido de liofilizador até alcançar 2% de umidade da amostra) também foram avaliados. Nas técnicas químicas aplicadas, o dimetilsulfóxido apresentou os melhores resultados para as duas leveduras, porém o seu uso é limitado devido a sua toxicidade. Para S. pararoseus, os maiores valores encontrados foram para o ácido clorídrico, seguido do acético e do lático, sendo detectada diferença entre eles quando aplicado o congelamento. Com R. mucilaginosa, os maiores valores foram encontrados para os ácidos acético e lático, seguido do ácido clorídrico, no qual o congelamento da biomassa também não influenciou a recuperação dos carotenoides. Dentre as técnicas mecânicas estudadas, para a levedura S. pararoseus, o banho ultrassônico e a abrasão com pérolas de vidro apresentaram os resultados mais promissores comparados ao DMSO (84,79±2,34 e 76,87±2,06 μg/g respectivamente), onde o processo de congelamento da biomassa não influenciou positivamente no percentual de extratibilidade e na concentração específica dos carotenoides quando utilizada estas técnicas. Com Rhodotorula mucilaginosa, o banho ultrassônico propiciou a recuperação da maior concentração específica de carotenoides (193,5±25,8 μg/g), sendo que o processo de congelamento também não influenciou positivamente no percentual de extratibilidade e na concentração específica dos carotenoides. Através do Delineamento Central Composto Rotacional (DCCR) 23 foi possível avaliar que a levedura S. pararoseus não demonstrou nenhum efeito sob as variáveis pH, temperatura e concentração de enzima. Assim, a melhor condição de trabalho escolhida foi pH 7,4, 30 ºC e concentração de enzima de 1,0 g/gcs, onde apresentou a concentração específica de 42,6 μg/g e volumétrica de 308 μg/L de carotenoides. Para R. mucilaginosa, a condição ótima foi definida como 1,0 g/gcs, pH 5,0 e temperatura de 30 ºC, onde foi encontrado 115,1±8,1 μg/g e 470,1±38,8 μg/L para a concentração específica e volumétrica de carotenoides, respectivamente. A utilização de técnicas combinadas empregando banho ultrassônico e lise enzimática não proporcionou melhorias nos resultados para ambas as leveduras. A liofilização provocou um ganho de 20% e 13,7% na concentração específica dos carotenoides das leveduras S. pararoseus e R. mucilaginosa, respectivamente, onde o congelamento da biomassa não influenciou significativamente (p<0,05) a recuperação de carotenoides provenientes das duas leveduras, podendo ser eliminada do processo. Assim, para S. pararoseus o banho ultrassônico e as pérolas de vidro apresentaram os melhores resultados na recuperação de carotenoides, e para R. mucilaginosa o melhor resultado foi alcançado com o banho ultrassônico.

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O trabalho apresentado nesta tese focou-se no estudo do amido, nomeadamente na avaliação das características físico-químicas, morfológicas, térmicas e reológicas do amido de seis variedades de milho crioulo, preservadas no estado de Santa Catarina (Brasil), com o intuito de contribuir para a valorização e preservação de variedades locais que são cultivadas em sistemas de produção orgânica, também conhecidas como variedades crioulas. Estas sementes são importantes quer para a preservação da biodiversidade quer para os pequenos produtores que as conservam e as produzem fazendo uso de uma agricultura sustentável e independente comercialmente. Para além da caracterização dos amidos crioulos foram também analisadas as alterações que ocorrem nos processos de gelatinização e retrogradação do amido quando realizados na presença de outros biopolímeros, nomeadamente a quitosana e galactomananas. No Capítulo I é apresentada uma breve revisão do conhecimento científico sobre o amido e sobre a quitosana e galactomananas, os outros biopolímeros utilizados. Igualmente é feita uma sucinta abordagem sobre as principais técnicas analíticas que foram utilizadas: reologia fundamental, calorimetria diferencial de varrimento, microscopia eletrónica de varrimento e espectroscopia de infravermelho médio. No capítulo II apresenta-se o isolamento dos amidos das seis variedades de milho crioulo e a sua caracterização junto com um amido comercial usado como modelo de comparação. Os amidos apresentaram genericamente características físicoquímicas semelhantes e o amido extraído das variedades crioulas MT e MPA 01 apresentaram menor temperatura de gelatinização e maior percentagem de retrogradação, respetivamente. Os efeitos da adição da quitosana e de três galactomananas (goma guar, goma de alfarroba e goma cassia) em sistemas mistos com o amido são analisados nos Capítulos III e IV respetivamente. A adição dos biopolímeros aos amidos resultou no aumento das temperaturas de gelatinização, na alteração da retrogradação do amido pelas galactomananas e na alteração das propriedades viscoeláticas dos géis formados. Os dados de infravermelho esclareceram que nos sistemas com quitosana, o amido formou complexos com o ácido acético usado para dissolver a quitosana e que esta por sua vez formou acetato de quitosana. O comportamento durante a gelatinização do amido comercial quando comparado com o amido do milho crioulo MPA na sua interação com as galactomananas é diferenciado.