Recombinant protein production using a Tobacco yellow dwarf virus-based episomal expression vector : control of Rep activity

Over the past decade, plants have been used as expression hosts for the production of pharmaceutically important and commercially valuable proteins. Plants offer many advantages over other expression systems such as lower production costs, rapid scale up of production, similar post-translational modification as animals and the low likelihood of contamination with animal pathogens, microbial toxins or oncogenic sequences. However, improving recombinant protein yield remains one of the greatest challenges to molecular farming. In-Plant Activation (InPAct) is a newly developed technology that offers activatable and high-level expression of heterologous proteins in plants. InPAct vectors contain the geminivirus cis elements essential for rolling circle replication (RCR) and are arranged such that the gene of interest is only expressed in the presence of the cognate viral replication-associated protein (Rep). The expression of Rep in planta may be controlled by a tissue-specific, developmentally regulated or chemically inducible promoter such that heterologous protein accumulation can be spatially and temporally controlled. One of the challenges for the successful exploitation of InPAct technology is the control of Rep expression as even very low levels of this protein can reduce transformation efficiency, cause abnormal phenotypes and premature activation of the InPAct vector in regenerated plants. Tight regulation over transgene expression is also essential if expressing cytotoxic products. Unfortunately, many tissue-specific and inducible promoters are unsuitable for controlling expression of Rep due to low basal activity in the absence of inducer or in tissues other than the target tissue. This PhD aimed to control Rep activity through the production of single chain variable fragments (scFvs) specific to the motif III of Tobacco yellow dwarf virus (TbYDV) Rep. Due to the important role played by the conserved motif III in the RCR, it was postulated that such scFvs can be used to neutralise the activity of the low amount of Rep expressed from a “leaky” inducible promoter, thus preventing activation of the TbYDV-based InPAct vector until intentional induction. Such scFvs could also offer the potential to confer partial or complete resistance to TbYDV, and possibly heterologous viruses as motif III is conserved between geminiviruses. Studies were first undertaken to determine the levels of TbYDV Rep and TbYDV replication-associated protein A (RepA) required for optimal transgene expression from a TbYDV-based InPAct vector. Transient assays in a non-regenerable Nicotiana tabacum (NT-1) cell line were undertaken using a TbYDV-based InPAct vector containing the uidA reporter gene (encoding GUS) in combination with TbYDV Rep and RepA under the control of promoters with high (CaMV 35S) or low (Banana bunchy top virus DNA-R, BT1) activity. The replication enhancer protein of Tomato leaf curl begomovirus (ToLCV), REn, was also used in some co-bombardment experiments to examine whether RepA could be substituted by a replication enhancer from another geminivirus genus. GUS expression was observed both quantitatively and qualitatively by fluorometric and histochemical assays, respectively. GUS expression from the TbYDV-based InPAct vector was found to be greater when Rep was expected to be expressed at low levels (BT1 promoter) rather than high levels (35S promoter). GUS expression was further enhanced when Rep and RepA were co-bombarded with a low ratio of Rep to RepA. Substituting TbYDV RepA with ToLCV REn also enhanced GUS expression but more importantly highest GUS expression was observed when cells were co-transformed with expression vectors directing low levels of Rep and high levels of RepA irrespective of the level of REn. In this case, GUS expression was approximately 74-fold higher than that from a non-replicating vector. The use of different terminators, namely CaMV 35S and Nos terminators, in InPAct vectors was found to influence GUS expression. In the presence of Rep, GUS expression was greater using pInPActGUS-Nos rather than pInPActGUS-35S. The only instance of GUS expression being greater from vectors containing the 35S terminator was when comparing expression from cells transformed with Rep, RepA and REnexpressing vectors and either non-replicating vectors, p35SGS-Nos or p35SGS-35S. This difference was most likely caused by an interaction of viral replication proteins with each other and the terminators. These results indicated that (i) the level of replication associated proteins is critical to high transgene expression, (ii) the choice of terminator within the InPAct vector may affect expression levels and (iii) very low levels of Rep can activate InPAct vectors hence controlling its activity is critical. Prior to generating recombinant scFvs, a recombinant TbYDV Rep was produced in E. coli to act as a control to enable the screening for Rep-specific antibodies. A bacterial expression vector was constructed to express recombinant TbYDV Rep with an Nterminal His-tag (N-His-Rep). Despite investigating several purification techniques including Ni-NTA, anion exchange, hydrophobic interaction and size exclusion chromatography, N-His-Rep could only be partially purified using a Ni-NTA column under native conditions. Although it was not certain that this recombinant N-His-Rep had the same conformation as the native TbYDV Rep and was functional, results from an electromobility shift assay (EMSA) showed that N-His-Rep was able to interact with the TbYDV LIR and was, therefore, possibly functional. Two hybridoma cell lines from mice, immunised with a synthetic peptide containing the TbYDV Rep motif III amino acid sequence, were generated by GenScript (USA). Monoclonal antibodies secreted by the two hybridoma cell lines were first screened against denatured N-His-Rep in Western analysis. After demonstrating their ability to bind N-His-Rep, two scFvs (scFv1 and scFv2) were generated using a PCR-based approach. Whereas the variable heavy chain (VH) from both cell lines could be amplified, only the variable light chain (VL) from cell line 2 was amplified. As a result, scFv1 contained VH and VL from cell line 1, whereas scFv2 contained VH from cell line 2 and VL from cell line 1. Both scFvs were first expressed in E. coli in order to evaluate their affinity to the recombinant TbYDV N-His-Rep. The preliminary results demonstrated that both scFvs were able to bind to the denatured N-His-Rep. However, EMSAs revealed that only scFv2 was able to bind to native N-His-Rep and prevent it from interacting with the TbYDV LIR. Each scFv was cloned into plant expression vectors and co-bombarded into NT-1 cells with the TbYDV-based InPAct GUS expression vector and pBT1-Rep to examine whether the scFvs could prevent Rep from mediating RCR. Although it was expected that the addition of the scFvs would result in decreased GUS expression, GUS expression was found to slightly increase. This increase was even more pronounced when the scFvs were targeted to the cell nucleus by the inclusion of the Simian virus 40 large T antigen (SV40) nuclear localisation signal (NLS). It was postulated that the scFvs were binding to a proportion of Rep, leaving a small amount available to mediate RCR. The outcomes of this project provide evidence that very high levels of recombinant protein can theoretically be expressed using InPAct vectors with judicious selection and control of viral replication proteins. However, the question of whether the scFvs generated in this project have sufficient affinity for TbYDV Rep to prevent its activity in a stably transformed plant remains unknown. It may be that other scFvs with different combinations of VH and VL may have greater affinity for TbYDV Rep. Such scFvs, when expressed at high levels in planta, might also confer resistance to TbYDV and possibly heterologous geminiviruses.

Rapid production of a plasmid DNA encoding a malaria vaccine candidate via amino-functionalized poly(GMA-co-EDMA) monolith

Malaria is a global health problem; an effective vaccine is urgently needed. Due to the relative poverty and lack of infrastructure in malaria endemic areas, DNA-based vaccines that are stable at ambient temperatures and easy to formulate have great potential. While attention has been focused mainly on antigen selection, vector design and efficacy assessment, the development of a rapid and commercially viable process to manufacture DNA is generally overlooked. We report here a continuous purification technique employing an optimized stationary adsorbent to allow high-vaccine recovery, low-processing time, and, hence, high-productivity. A 40.0 mL monolithic stationary phase was synthesized and functionalized with amino groups from 2-Chloro-N,N- diethylethylamine hydrochloride for anion-exchange isolation of a plasmid DNA (pDNA) that encodes a malaria vaccine candidate, VR1020-PyMSP4/5. Physical characterization of the monolithic polymer showed a macroporous material with a modal pore diameter of 750 nm. The final vaccine product isolated after 3 min elution was homogeneous supercoiled plasmid with gDNA, RNA and protein levels in keeping with clinical regulatory standards. Toxicological studies of the pVR1020-PyMSP4/5 showed a minimum endotoxin level of 0.28 EU/m.g pDNA. This cost-effective technique is cGMP compatible and highly scalable for the production of DNA-based vaccines in commercial quantities, when such vaccines prove to be effective against malaria. © 2008 American Institute of Chemical Engineers.

Thermodynamic properties of oxygen in RE-O (RE = Gd, Tb, Dy, Er) solid solutions

The oxygen potentials of four rare-earth metal – oxygen (RE–O: RE=Gd, Dy, Tb, Er) solid solutions have been measured by equilibration with yttrium – oxygen (Y–O) and titanium – oxygen (Ti–O) solid solutions. Rare-earth metal, yttrium and titanium samples were immersed in calcium-saturated CaCl2 melt at temperatures between 1093 and 1233 K. Homogeneous oxygen potential was established in the metallic samples through the fused salt, which contains some dissolved CaO. The metallic samples were analyzed for oxygen after quenching. The oxygen potentials of RE–O solid solutions were determined using either Y–O or Ti–O solid solution as the reference. This method enabled reliable measurement of extremely low oxygen potentials at high temperature (circa pO2=10−48 atm at 1173 K). It was found that the oxygen affinity of the metals decreases in the order: Y>Er>Dy>Tb>Gd>Ti. Values for the standard Gibbs energy of solution of oxygen in RE metals obtained in this study, permit assessment of the extent of deoxidation that can be achieved with various purification techniques. It may be possible to achieve an oxygen level of 10 mass ppm using an electrochemical deoxidation method.

Complement factor H is a serum-binding protein for adrenomedullin, and the resulting complex modulates the bioactivities of both partners

Adrenomedullin (AM) is an important regulatory peptide involved in both physiological and pathological states. We have previously demonstrated the existence of a specific AM-binding protein (AMBP-1) in human plasma. In the present study, we developed a nonradioactive ligand blotting assay, which, together with high pressure liquid chromatography/SDS-polyacrylamide gel electrophoresis purification techniques, allowed us to isolate AMBP-1 to homogeneity. The purified protein was identified as human complement factor H. We show that AM/factor H interaction interferes with the established methodology for quantification of circulating AM. Our data suggest that this routine procedure does not take into account the AM bound to its binding protein. In addition, we show that factor H affects AM in vitro functions. It enhances AM-mediated induction of cAMP in fibroblasts, augments the AM-mediated growth of a cancer cell line, and suppresses the bactericidal capability of AM on Escherichia coli. Reciprocally, AM influences the complement regulatory function of factor H by enhancing the cleavage of C3b via factor I. In summary, we report on a potentially new regulatory mechanism of AM biology, the influence of factor H on radioimmunoassay quantification of AM, and the possible involvement of AM as a regulator of the complement cascade.

Extraction of added-value products from biomass using ionic liquids

The main purpose of this thesis is to investigate the potential of ionic liquids (ILs) as a new class of extractive solvents for added-value products from biomass. These include phenolic compounds (vanillin, gallic, syringic and vanillic acids), alkaloids (caffeine) and aminoacids (L-tryptophan). The interest on these natural compounds relies on the wide variety of relevant properties shown by those families and further application in the food, cosmetic and pharmaceutical industries. Aiming at developping more benign and effective extraction/purification techniques than those used, a comprehensive study was conducted using aqueous biphasic systems (ABS) composed of ILs and inorganic/organic salts. In addition, ILs were characterized by a polarity scale, using solvatochromic probes, aiming at providing prior indications on the ILs affinity for particular added-value products. Solid-liquid (S-L) extractions from biomass and using aqueous solution of ILs were also investigated. In particular, and applying and experimental factorial design to optimize the operational conditions, caffeine was extracted from guaraná seeds and spent coffee. With both types of extractions it was found that it is possible to recover the high-value compounds and to recycle the IL and salt solutions. Finally, aiming at exploring the recovery of added-value compounds from biomass using a simpler and more suistainable technique, the solubility of gallic acid, vanillin and caffeine was studied in aqueous solutions of several ILs and common salts. With the gathered results it was possible to demonstrate that ILs act as hydrotropes and that water can be used as an adequate antisolvent. This thesis describes the use of ILs towards the development of more effective and sustainable processes.

Sels de tétraarylphosphonium : synthèse et application à la synthèse de la (–)-coniine ; capacité trans-directrice du groupement amide en cyclopropanation d’oléfines

Le développement ainsi que l’amélioration des différentes techniques de purification sont des défis importants pour la chimie d’aujourd’hui. Certaines des méthodes actuelles, tel que le greffage d’un réactif sur un support solide permettant d’accéder à un produit pur par simple filtration du milieu, comportent toutefois certains inconvénients. En effet, les propriétés de solubilité de ces polymères rendent la mise en œuvre des réactions plus difficiles. C’est dans ce contexte que le groupe du Pr. Charette a rapporté l’utilisation de réactifs liés à un sel de tétraarylphosphonium (TAP). Ces sels peuvent être solubilisés dans un solvant tel que le dichlorométhane et aisément retirés du milieu réactionnel par précipitation à l’aide d’éther diéthylique (Chapitre 1). L’un des objectifs de cette thèse a donc été lié à la découverte de deux méthodes complémentaires qui, jusqu’à présent, sont considérées comme des méthodes de choix pour la synthèse des sels de TAP fonctionnalisés (Chapitre 2). L’une d’entre elles est utilisée par Soluphase inc., une entreprise qui commercialise ces sels de TAP. L’efficacité des sels en tant que support dans la synthèse de petites molécules a été démontrée lors de la synthèse d’un produit naturel, la (–)-coniine (Chapitre 3). L’isolement des intermédiaires synthétiques instables par simple précipitation à l’aide d’un support de TAP a permis de rendre cette synthèse plus efficace que celle déjà connue. Dans le deuxième volet de cette thèse, plusieurs problèmes reliés à la synthèse de dérivés cyclopropaniques 1,1-disubstitués ont été étudiés. Ces derniers font partie intégrale de plusieurs produits naturels et de médicaments. Cependant, leur formation par une réaction de cyclopropanation d’alcènes utilisant des réactifs diazoïques possédant deux groupements de type accepteur n’est pas tâche facile (Chapitre 4). En effet, cette réaction souffre d’un faible contrôle diastéréosélectif. Par le fait même, très peu de méthodologies de synthèse ont rapporté l’utilisation de ce type de réactifs diazoïques dans des réactions de cyclopropanation stéréosélectives. L’étude du mécanisme de la réaction de cyclopropanation catalysée au Rh(II) a proposé des indices favorisant un modèle ayant des précédents dans la littérature (Chapitre 5). Ces études nous ont mené à la découverte de la «capacité trans-directrice» du groupement amide lors des réactions de cyclopropanation d’oléfines. Nous avons donc utilisé cette propriété afin de résoudre plusieurs problèmes rencontrés dans la littérature. Nous avons montré qu’elle permet l’accès à des dérivés cyclopropaniques possédant deux groupements carboxyliques géminaux avec des sélectivités élevées (Chapitre 6). Ces produits étaient accessibles que par des séquences synthétiques nécessitant plusieurs étapes. De plus, nous avons démontrés que ces nouveaux dérivés cyclopropaniques sont des outils synthétiques fort utiles dans la synthèse de produits naturels d’intérêt biologique. Cette formidable «capacité trans-directrice» du groupement amide nous a permi de résoudre le problème de la synthèse asymétrique de dérivés carboxyliques α-cyano cyclopropaniques (Chapitre 7). De plus, ce projet nous a menées à la découverte de l’effet de divers additif achiraux permettant d’augmenter la sélectivité dans certaines réactions. Cette réaction possède une vaste étendue et l’utilité de ces nouveaux dérivés cyclopropaniques a été démontrée par plusieurs transformations de groupements fonctionnels.

Studies on Production of Bacterial Xylanases

Xylanases with hydrolytic activity on xylan, one of the hemicellulosic materials present in plant cell walls, have been identified long back and the applicability of this enzyme is constantly growing. All these applications especially the pulp and paper industries require novel enzymes. There has been lot of documentation on microbial xylanases, however, none meeting all the required characteristics. The characters being sought are: higher production, higher pH and temperature optima, good stabilities under these conditions and finally the low associated cellulase and protease production. The present study analyses various facets of xylanase biotechnology giving emphasis on bacterial xylanases. Fungal xylanases are having problems like low pH values for both enzyme activity and growth. Moreover, the associated production of cellulases at significant levels make fungal xylanases less suitable for application in paper and pulp industries.Bacillus SSP-34 selected from 200 isolates was clearly having xylan catabolizing nature distinct from earlier reports. The stabilities at higher temperatures and pH values along with the optimum conditions for pH and temperature is rendering Bacillus SSP-34 xylanase more suitable than many of the previous reports for application in pulp and paper industries.Bacillus SSP-34 is an alkalophilic thertmotolerant bacteria which under optimal cultural conditions as mentioned earlier, can produce 2.5 times more xylanase than the basal medium.The 0.5% xylan concentration in the medium was found to the best carbon source resulting in 366 IU/ml of xylanase activity. This induction was subjected to catabolite repression by glucose. Xylose was a good inducer for xylanase production. The combination of yeast extract and peptone selected from several nitrogen sources resulted in the highest enzyme production (379+-0.2 IU/ml) at the optimum final concentration of 0.5%. All the cultural and nutritional parameters were compiled and comparative study showed that the modified medium resulted in xylanase activity of 506 IU/ml, 5 folds higher than the basal medium.The novel combination of purification techniques like ultrafiltraton, ammonium sulphate fractionation, DEAE Sepharose anion exchange chromatography, CM Sephadex cation exchange chromatography and Gel permeation chromatography resulted in the purified xylanase having a specific activity of 1723 U/mg protein with 33.3% yield. The enzyme was having a molecular weight of 20-22 kDa. The Km of the purified xylanase was 6.5 mg of oat spelts xylan per ml and Vmax 1233 µ mol/min/mg protein.Bacillus SSP-34 xylanase resulted in the ISO brightness increase from 41.1% to 48.5%. The hydrolytic nature of the xylanase was in the endo-form.Thus the organism Bacillus SSP-34 was having interesting biotechnological and physiological aspects. The SSP-34 xylanase having desired characters seems to be suited for application in paper and pulp industries.

Ação antifúngica do resíduo líquido integral e fracionado do desfibramento da folha do sisal (Agave sisalana) sobre Malassezia pachydermatis, Tricophyton mentagrophytes e Candida albicans

Pós-graduação em Ciências Biológicas (Microbiologia Aplicada) - IBRC

BIOMOLECULES EXTRACTED BY ATPS: PRACTICAL EXAMPLES

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Biomolecules extracted by ATPs: practical examples

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

HCl gas gettering of 3d transition metals for crystalline silicon solar cell concepts

In order to reduce the costs of crystalline silicon solar cells, low-cost silicon materials like upgraded metallurgical grade (UMG) silicon are investigated for the application in the photovoltaic (PV) industry. Conventional high-purity silicon is made by cost-intensive methods, based on the so-called Siemens process, which uses the reaction to form chlorosilanes and subsequent several distillation steps before the deposition of high-purity silicon on slim high-purity silicon rods. UMG silicon in contrast is gained from metallurgical silicon by a rather inexpensive physicochemical purification (e.g., acid leaching and/or segregation). However, this type of silicon usually contains much higher concentrations of impurities, especially 3d transition metals like Ti, Fe, and Cu. These metals are extremely detrimental in the electrically active part of silicon solar cells, as they form recombination centers for charge carriers in the silicon band gap. This is why simple purification techniques like gettering, which can be applied between or during solar cell process steps, will play an important role for such low-cost silicon materials. Gettering in general describes a process, whereby impurities are moved to a place or turned into a state, where they are less detrimental to the solar cell. Hydrogen chloride (HCl) gas gettering in particular is a promising simple and cheap gettering technique, which is based on the reaction of HCl gas with transition metals to form volatile metal chloride species at high temperatures.rnThe aim of this thesis was to find the optimum process parameters for HCl gas gettering of 3d transition metals in low-cost silicon to improve the cell efficiency of solar cells for two different cell concepts, the standard wafer cell concept and the epitaxial wafer equivalent (EpiWE) cell concept. Whereas the former is based on a wafer which is the electrically active part of the solar cell, the latter uses an electrically inactive low-cost silicon substrate with an active layer of epitaxially grown silicon on top. Low-cost silicon materials with different impurity grades were used for HCl gas gettering experiments with the variation of process parameters like the temperature, the gettering time, and the HCl gas concentration. Subsequently, the multicrystalline silicon neighboring wafers with and without gettering were compared by element analysis techniques like neutron activation analysis (NAA). It was demonstrated that HCl gas gettering is an effective purification technique for silicon wafers, which is able to reduce some 3d transition metal concentrations by over 90%. Solar cells were processed for both concepts which could demonstrate a significant increase of the solar cell efficiency by HCl gas gettering. The efficiency of EpiWE cells could be increased by HCl gas gettering by approximately 25% relative to cells without gettering. First process simulations were performed based on a simple model for HCl gas gettering processes, which could be used to make qualitative predictions.

Reduction of haloacetonitriles and haloacetones in natural waters using ceramic nanofiltration membranes

Póster presentado en 19th International Congress of Chemical and Process Engineering, Prague, Czech Republic August 28th-September 1st, 2010.

Purificação de C-ficocianina e sua incorporação em nanofibras

C-ficocianina (C-FC) é uma ficobiliproteína, de cor natural azul, com diversas aplicações na indústria alimentícia, farmacêutica e biomédica, dependendo do seu grau específico de pureza, que pode variar de 0,7 a 4,0, com respectivo aumento de seu valor comercial. Essa pureza é alcançada através de diversas técnicas de purificação, que podem ser aplicadas em diferentes sequências. Um destes processos de purificação de proteínas baseia-se na cromatografia de troca iônica, que utiliza trocadores que adsorvem as proteínas como resultado de interações iônicas entre a superfície da proteína e o trocador. Resinas e colunas de leito expandido podem ser utilizadas para aumentar a produtividade dessa técnica. É fundamental conhecer o perfil do processo de adsorção, para melhor aplicá-lo como ferramenta para o design e otimização de parâmetros operacionais. Outra tecnologia para o tratamento de biomoléculas é a ultrafiltração. Esta técnica é aplicável em larga escala, apresenta baixa complexidade de aplicação e pode ser realizada em condições brandas, minimizando o dano para o produto. Para aumentar a estabilidade da C-FC, e facilitar a sua aplicação, podem ser avaliadas técnicas recentes, não exploradas para este fim, como as nanofibras obtidas através do processo de electrospinning. Estas fibras possuem uma área superficial específica extremamente elevada devido a seu pequeno diâmetro. O objetivo deste trabalho foi avaliar parâmetros de adsorção e diferentes técnicas para purificação de C-ficocianina de Spirulina platensis e obter nanofibras poliméricas incorporadas de C-ficocianina. O trabalho foi dividido em quatro artigos. No primeiro artigo, foram avaliados os parâmetros e as isotermas de adsorção de C-ficocianina em resina de troca iônica para leito expandido Streamline® DEAE. Verificou-se que o maior coeficiente de partição foi obtido em pH 7,5, nas temperaturas de 15 e 25 °C. As isotermas de adsorção da Cficocianina foram bem representadas pelos modelos de Langmuir, de Freundlich e de Langmuir-Freundlich, sendo os valores estimados para Qm e Kd obtidos pela isoterma de Langmuir foram, respectivamente, 33,92 mg.mL-1 e 0,123 mg.mL-1, respectivamente. No segundo artigo foi avaliada a purificação de C-FC até grau alimentar, utilizando ultrafiltração (UF). Com a membrana de 50 kDa, identificou-se que somente a temperatura e a aplicação de diferentes ciclos de diafiltração (DF) causaram influência significativa sobre a purificação e recuperação da C-ficocianina. Foram então aplicados o aumento gradativo da quantidade de ciclos, e a diafiltração previamente à ultrafiltração (DF/UF), onde obteve-se um extrato de Cficocianina com pureza de 0,95. No terceiro artigo foram propostos processos de purificação, envolvendo a utilização das diferentes técnicas para obtenção de C-FC com diferentes purezas. Determinou-se que a partir de cromatografia de troca iônica em leito fixo seguido de DF/UF, obtém-se C-FC para uso em cosméticos e a partir de precipitação com sulfato de amônio, e DF/UF obtém-se C-FC para uso em biomarcadores. Com uma sequência de precipitação com sulfato de amônio, DF/UF e cromatografia de troca iônica em leito fixo chega-se a C-FC de grau analítico. No último artigo, C-FC foi incorporada a nanofibras de óxido de polietileno (PEO) através de processo de electrospinning. Foram determinadas a condutividade da solução de C-FC/PEO, a estrutura e comportamento termogravimétrico das nanofibras formadas. Soluções de polímeros com concentração de 6 e 8% proporcionaram a formação de nanofibras com diâmetro médio inferior a 800 nm, homogêneas, sem a presença de gotas. A análise termogravimétrica identificou aumento na resistência térmica da C-FC incorporada nas fibras.

Fukushima-derived radionuclides in sediments of the Japanese Pacific Ocean coast and various Japanese water samples (seawater, tap water, and coolant water of Fukushima Daiichi reactor unit 5)

We investigated Ocean sediments and seawater from inside the Fukushima exclusion zone and found radiocesium (134Cs and 137Cs) up to 800 Bq kg-1 as well as 90Sr up to 5.6 Bq kg-1. This is one of the first reports on radiostrontium in sea sediments from the Fukushima exclusion zone. Seawater exhibited contamination levels up to 5.3 Bq kg-1 radiocesium. Tap water from Tokyo from weeks after the accident exhibited detectable but harmless activities of radiocesium (well below the regulatory limit). Analysis of the Unit 5 reactor coolant (finding only 3H and even low 129I) leads to the conclusion that the purification techniques for reactor coolant employed at Fukushima Daiichi are very effective.

Molecular Techniques for Dicistrovirus Detection without RNA Extraction or Purification

Dicistroviridae is a new family of small, nonenveloped, and +ssRNA viruses pathogenic to both beneficial arthropods and insect pests as well. Triatoma virus (TrV), a dicistrovirus, is a pathogen of Triatoma infestans (Hemiptera: Reduviidae), one of the main vectors of Chagas disease. In this work, we report a single-step method to identify TrV, a dicistrovirus, isolated from fecal samples of triatomines. The identification method proved to be quite sensitive, even without the extraction and purification of RNA virus.