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The yeast cell wall is a complex structure whose main function is to protect the cell from physical and chemical damage, providing it with rigidity. It is composed of a matrix of covalently linked polysaccharides and proteins, including ß-glucans, mannoproteins, and chitin, whose proportion can vary according to the yeast species and environmental conditions. The main components of the yeast cell wall have relevant properties that expand the possibilities of use in different industrial sectors, such as pharmaceutical, food, medical, veterinary, and cosmetic. Some applications include bioremediation, enzyme immobilization, animal feed, wine production, and hydrogel production. In the literature it is the description of the cell wall composition of model species like Saccharomyces cerevisiae and Candida albicans, however, it is important to know that this composition can vary according to the species or the culture medium conditions. Thus, understanding the structural composition of different species holds promise as an alternative to expanding the utilization of residual yeast from different bioprocesses. In the context of a circular economy, the conversion of residual yeast into valuable products is an attractive prospect for researchers aiming to develop sustainable technologies. This review provides an overview of yeast cell wall composition and its significance in biotechnological applications, considering prospects to increase the diversification of these compounds in industry.

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In swine farming, antibiotics are often used to reduce disease and promote animal growth. Part of these compounds is not absorbed by the swine body, being excreted and later reaching the treatment systems, soil, and nearby waterbodies. This research sought to investigate the influence of adding ciprofloxacin (CIP) on the anaerobic digestion of swine wastewater. For that, a bench-scale anaerobic sequential batch reactor (ASBR) was used, with 5 L of working volume in six different phases, with volumetric organic loading rate (VOLR) and CIP dosage variation. According to the results, the optimal VOLR for the reactor was 0.60 ± 0.11 gSV L-1 d-1, resulting in biogas productivity of 0.51 ± 0.03 Lbiogas L-1 d-1. After initial stability, adding substrate with 0.5 mgCIP L-1 resulted in an abrupt drop of 82% in the productivity from the 7th to 11th day of addition, coinciding with volatile acids accumulation. Afterward, the reactor recovered and reached apparent stability, with productivity similar to the previous step without the drug. For 2.5 mgCIP L-1 in the substrate, the biogas productivity at equilibrium was 11.8% lower than in the phases with the same VOLR and 0.0 and 0.5 mgCIP L-1. Organic matter removals near 80% were achieved for both dosages. The 16S rRNA metagenomic analyses showed an increase in the relative abundance of most of the phyla found, indicating that the dosages used allowed the acclimatization of microorganisms and possibly the compound biodegradation.

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RESUMO Objetivou-se estimar a prevalência da Violência Sexual (VS) contra homens brasileiros e fatores associados. Estudo transversal, que estimou a prevalência de várias formas de VS entre homens brasileiros por meio de questionário virtual. Participaram do estudo 1.241 homens de todos os estados. A maioria era jovem, entre 18 e 39 anos de idade (61,7%), heterossexual (50,2%), do Sudeste (54,4%), das classes socioeconômicas C/D/E (72,1%) e brancos (64,3%). Sobre as prevalências de VS, 70,5% afirmaram ter sofrido VS sem contato, 43,1%, VS com contato, 23,9%, VS com penetração, e 33,1%, sexo forçado. Ser bissexual, ser homossexual e ser divorciado/separado aumentaram as chances de sofrer sexo forçado. Este estudo indica que homens bissexuais e homossexuais têm mais chances de sofrer VS, corroborando outras pesquisas. Entre divorciados/separados, as chances de sofrer VS também se mostraram significativas e precisam ser mais bem exploradas. O estudo oferece a possibilidade de problematização para acolhimento de homens vítimas de VS, pensando majoritariamente na prevenção de efeitos adversos após a violência e na implantação de políticas públicas da área da saúde mais direcionadas para o público-alvo, considerando os principais fatores associados.

ABSTRACT We aimed to estimate the prevalence of sexual violence against Brazilian men and associated factors. A cross-sectional study was conducted, which estimated the prevalence of various forms of sexual violence among Brazilian men by means of a virtual questionnaire. A total of 1241 men from all Brazilian states participated in the study. Most participants were young men between 18 and 39 years (61.7%), heterosexual (50.2%), from the Southeast (54.4%), from socioeconomic classes C/D/E (72.1%), and white (64.3%). Regarding the prevalences of sexual violence, 70.5% reported non-contact sexual violence, 43.1% sexual violence with contact, 23.9% sexual violence with penetration, and 33.1% forced sex. Being bisexual homosexual, and being divorced/separated increased the odds of experiencing forced sex. This study indicates that bisexual and homosexual men are more likely to suffer sexual violence, corroborating other research. Among divorced/separated men the chances of experiencing sexual violence were also significant and need to be further explored. The study offers the possibility of problematization for the care of male victims of sexual violence, focusing mainly on the prevention of adverse effects after violence and the implementation of public policies in health that are more directed to the target audience, considering the main associated factors.

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This paper presents the profits and disadvantages of the chemometrics approach instead of the one-factor-at-a-time (OFAT) coagulation diagram approach for tropical water physicochemical treatment. Central composite design associate to response surface methodology (CCD-RSM) is used to find the real best conditions for coagulant dosage and pH aiming at high-turbidity removal. The number of experiments needed to chemometrics model construction (12) is comparatively smaller than that used in the coagulation diagram (84), saving financial and environmental resources. Arguments for Water Treatment Plants (WTP) considering the replacement of coagulation diagram approach by the CCD-RSM approach in drinking water treatment are presented. Chemometrics models are all constructed on a free software platform, providing the best pH within the range 7.7-8.1, and the best coagulant dosage (polyaluminium chloride, PAC) between 2.0 and 3.1 mg Al2O3 L-1 (equivalent in mass). CCD-RSM provides a faster, lower-cost and more reliable alternative tool for WTP decision-making instead of the OFAT model, mainly for waters more affected by seasonal effects as can be seen in tropical and subtropical countries.

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Recent advances in biomass conversion technologies have shown a promising future toward fermentation during xylitol production. Xylitol is one of the top 12 renewable added-value chemicals that can be obtained from biomass according to US Department of Energy (USDOE). Currently, xylitol accounts for approximately US$823.6 million of annual sales in the market, and this amount is expected to reach US$1.37 billion by 2025. This high demand has been achieved owing to the chemical conversion of hemicellulosic hydrolysates from different lignocellulosic biomasses, which is a costly and non-ecofriendly process. Xylose-rich hemicellulosic hydrolysates are the major raw materials for xylitol production through either chemical or biotechnological routes. Economic production of a clean hemicellulosic hydrolysate is one of the major bottlenecks for xylitol production on the commercial scale. Advancements in biotechnology, such as the isolation of novel microorganisms, genetic manipulation of xylose metabolizing strains, and modifications in the fermentation process, can enhance the economic feasibility of xylitol production on the large scale. Furthermore, xylitol production in integrated biorefineries can be even more economic, given the readily available raw materials and the co-use of steam, electricity, and water, among others. Exploring new biotechnology techniques in integrated biorefineries would open new markets and opportunities for sustainable xylitol production to fulfill the market's growing demands for this sugar alcohol. This article is a review of the advancements reported in the whole biotechnological process for xylitol production, and involve pretreatment technologies, hemicellulosic hydrolysate preparation, xylose conversion into xylitol, and product recovery. Special attention is devoted to current metabolic engineering strategies to improve this bioprocess, as well as to the importance of xylitol production processes in biorefineries.

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Abstract Sugarcane straw has become an available lignocellulosic biomass since the progressive introduction of the non-burning harvest in Brazil. Besides keeping this biomass in the field, it can be used as a feedstock in thermochemical or biochemical conversion processes. This makes feasible its incorporation in a biorefinery, whose economic profitability could be supported by integrated production of low-value biofuels and high-value chemicals, e.g., xylitol, which has important industrial and clinical applications. Herein, biotechnological production of xylitol is presented as a possible route for the valorization of sugarcane straw and its incorporation in a biorefinery. Nutritional supplementation of the sugarcane straw hemicellulosic hydrolyzate as a function of initial oxygen availability was studied in batch fermentation of Candida guilliermondii FTI 20037. The nutritional supplementation conditions evaluated were: no supplementation; supplementation with (NH4)2SO4, and full supplementation with (NH4)2SO4, rice bran extract and CaCl2·2H2O. Experiments were performed at pH 5.5, 30 °C, 200 rpm, for 48 h in 125 mL Erlenmeyer flasks containing either 25 or 50 mL of medium in order to vary initial oxygen availability. Without supplementation, complete consumption of glucose and partial consumption of xylose were observed. In this condition the maximum xylitol yield (0.67 g g-1) was obtained under reduced initial oxygen availability. Nutritional supplementation increased xylose consumption and xylitol production by up to 200% and 240%, respectively. The maximum xylitol volumetric productivity (0.34 g L-1 h-1) was reached at full supplementation and increased initial oxygen availability. The results demonstrated a combined effect of nutritional supplementation and initial oxygen availability on xylitol production from sugarcane straw hemicellulosic hydrolyzate.

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Sugarcane straw has become an available lignocellulosic biomass since the progressive introduction of the non-burning harvest in Brazil. Besides keeping this biomass in the field, it can be used as a feedstock in thermochemical or biochemical conversion processes. This makes feasible its incorporation in a biorefinery, whose economic profitability could be supported by integrated production of low-value biofuels and high-value chemicals, e.g., xylitol, which has important industrial and clinical applications. Herein, biotechnological production of xylitol is presented as a possible route for the valorization of sugarcane straw and its incorporation in a biorefinery. Nutritional supplementation of the sugarcane straw hemicellulosic hydrolyzate as a function of initial oxygen availability was studied in batch fermentation of Candida guilliermondii FTI 20037. The nutritional supplementation conditions evaluated were: no supplementation; supplementation with (NH4)2SO4, and full supplementation with (NH4)2SO4, rice bran extract and CaCl2·2H2O. Experiments were performed at pH 5.5, 30 °C, 200 rpm, for 48 h in 125 mL Erlenmeyer flasks containing either 25 or 50 mL of medium in order to vary initial oxygen availability. Without supplementation, complete consumption of glucose and partial consumption of xylose were observed. In this condition the maximum xylitol yield (0.67 g g-1) was obtained under reduced initial oxygen availability. Nutritional supplementation increased xylose consumption and xylitol production by up to 200% and 240%, respectively. The maximum xylitol volumetric productivity (0.34 g L-1 h-1) was reached at full supplementation and increased initial oxygen availability. The results demonstrated a combined effect of nutritional supplementation and initial oxygen availability on xylitol production from sugarcane straw hemicellulosic hydrolyzate.(AU)

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Sugarcane straw has become an available lignocellulosic biomass since the progressive introduction of the non-burning harvest in Brazil. Besides keeping this biomass in the field, it can be used as a feedstock in thermochemical or biochemical conversion processes. This makes feasible its incorporation in a biorefinery, whose economic profitability could be supported by integrated production of low-value biofuels and high-value chemicals, e.g., xylitol, which has important industrial and clinical applications. Herein, biotechnological production of xylitol is presented as a possible route for the valorization of sugarcane straw and its incorporation in a biorefinery. Nutritional supplementation of the sugarcane straw hemicellulosic hydrolyzate as a function of initial oxygen availability was studied in batch fermentation of Candida guilliermondii FTI 20037. The nutritional supplementation conditions evaluated were: no supplementation; supplementation with (NH4)2SO4, and full supplementation with (NH4)2SO4, rice bran extract and CaCl2·2H2O. Experiments were performed at pH 5.5, 30°C, 200rpm, for 48h in 125mL Erlenmeyer flasks containing either 25 or 50mL of medium in order to vary initial oxygen availability. Without supplementation, complete consumption of glucose and partial consumption of xylose were observed. In this condition the maximum xylitol yield (0.67gg(-1)) was obtained under reduced initial oxygen availability. Nutritional supplementation increased xylose consumption and xylitol production by up to 200% and 240%, respectively. The maximum xylitol volumetric productivity (0.34gL(-1)h(-1)) was reached at full supplementation and increased initial oxygen availability. The results demonstrated a combined effect of nutritional supplementation and initial oxygen availability on xylitol production from sugarcane straw hemicellulosic hydrolyzate.

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The use of hemicellulosic hydrolysates in bioprocesses requires supplementation as to ensure the best fermentative performance of microorganisms. However, in light of conflicting data in the literature, it is necessary to establish an inexpensive and applicable medium for the development of bioprocesses. This paper evaluates the fermentative performance of Scheffersomyces (Pichia) stipitis and Candida guilliermondii growth in sugarcane bagasse hemicellulosic hydrolysate supplemented with different nitrogen sources including rice bran extract, an important by-product of agroindustry and source of vitamins and amino acids. Experiments were carried out with hydrolysate supplemented with rice bran extract and (NH4)2SO4; peptone and yeast extract; (NH4)2SO4, peptone and yeast extract and non-supplemented hydrolysate as a control. S. stipitis produced only ethanol, while C. guilliermondii produced xylitol as the main product and ethanol as by-product. Maximum ethanol production by S. stipitis was observed when sugarcane bagasse hemicellulosic hydrolysate was supplemented with (NH4)2SO4, peptone and yeast extract. Differently, the maximum xylitol formation by C. guilliermondii was obtained by employing hydrolysate supplemented with (NH4)2SO4 and rice bran extract. Together, these findings indicate that: a) for both yeasts (NH4)2SO4 was required as an inorganic nitrogen source to supplement sugarcane bagasse hydrolysate; b) for S. stipitis, sugarcane hemicellulosic hydrolysate must be supplemented with peptone and yeast extract as organic nitrogen source; and: c) for C. guilliermondii, it must be supplemented with rice bran extract. The present study designed a fermentation medium employing hemicellulosic hydrolysate and provides a basis for studies about value-added products as ethanol and xylitol from lignocellulosic materials.

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The use of hemicellulosic hydrolysates in bioprocesses requires supplementation as to ensure the best fermentative performance of microorganisms. However, in light of conflicting data in the literature, it is necessary to establish an inexpensive and applicable medium for the development of bioprocesses. This paper evaluates the fermentative performance of Scheffersomyces (Pichia) stipitis and Candida guilliermondii growth in sugarcane bagasse hemicellulosic hydrolysate supplemented with different nitrogen sources including rice bran extract, an important by-product of agroindustry and source of vitamins and amino acids. Experiments were carried out with hydrolysate supplemented with rice bran extract and (NH4)2SO4; peptone and yeast extract; (NH4)2SO4, peptone and yeast extract and non-supplemented hydrolysate as a control. S. stipitis produced only ethanol, while C. guilliermondii produced xylitol as the main product and ethanol as by-product. Maximum ethanol production by S. stipitis was observed when sugarcane bagasse hemicellulosic hydrolysate was supplemented with (NH4)2SO4, peptone and yeast extract. Differently, the maximum xylitol formation by C. guilliermondii was obtained by employing hydrolysate supplemented with (NH4)2SO4 and rice bran extract. Together, these findings indicate that: a) for both yeasts (NH4)2SO4 was required as an inorganic nitrogen source to supplement sugarcane bagasse hydrolysate; b) for S. stipitis, sugarcane hemicellulosic hydrolysate must be supplemented with peptone and yeast extract as organic nitrogen source; and: c) for C. guilliermondii, it must be supplemented with rice bran extract. The present study designed a fermentation medium employing hemicellulosic hydrolysate and provides a basis for studies about value-added products as ethanol and xylitol from lignocellulosic materials.

Assuntos

RESUMO

The use of hemicellulosic hydrolysates in bioprocesses requires supplementation as to ensure the best fermentative performance of microorganisms. However, in light of conflicting data in the literature, it is necessary to establish an inexpensive and applicable medium for the development of bioprocesses. This paper evaluates the fermentative performance of Scheffersomyces (Pichia) stipitis and Candida guilliermondii growth in sugarcane bagasse hemicellulosic hydrolysate supplemented with different nitrogen sources including rice bran extract, an important by-product of agroindustry and source of vitamins and amino acids. Experiments were carried out with hydrolysate supplemented with rice bran extract and (NH4)2SO4; peptone and yeast extract; (NH4)2SO4, peptone and yeast extract and non-supplemented hydrolysate as a control. S. stipitis produced only ethanol, while C. guilliermondii produced xylitol as the main product and ethanol as by-product. Maximum ethanol production by S. stipitis was observed when sugarcane bagasse hemicellulosic hydrolysate was supplemented with (NH4)2SO4, peptone and yeast extract. Differently, the maximum xylitol formation by C. guilliermondii was obtained by employing hydrolysate supplemented with (NH4)2SO4 and rice bran extract. Together, these findings indicate that: a) for both yeasts (NH4)2SO4 was required as an inorganic nitrogen source to supplement sugarcane bagasse hydrolysate; b) for S. stipitis, sugarcane hemicellulosic hydrolysate must be supplemented with peptone and yeast extract as organic nitrogen source; and: c) for C. guilliermondii, it must be supplemented with rice bran extract. The present study designed a fermentation medium employing hemicellulosic hydrolysate and provides a basis for studies about value-added products as ethanol and xylitol from lignocellulosic materials.

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Objetivo: Avaliar a influência do grau de ativação na deformação plástica de elásticos ortodônticos em cadeia em função do tempo que permaneceram estirados. Método: Foram testadas 72 amostras de cadeia elástica da marca Morelli, tamanho médio cristal, que foram mantidas em um jig confeccionado, especialmente, para este fim, com diferentes graus de ativação, 30%, 50% e 70% dos seus comprimentos iniciais, sendo avaliadas 24 cadeias elásticas para cada grau de ativação. Os elásticos foram mantidos em suas embalagens plásticas originais, como recomendado pelo fabricante, até serem testados. O jig com os elásticos foram conservados em um recipiente plástico contendo saliva artificial e mantidos em uma estufa artesanal com temperatura controlada de 37ºC ± 1ºC por todo o tempo do experimento, sendo removidos deste ambiente somente ao final de 3 semanas de ativação. As medidas dos comprimentos iniciais e finais de seis elos de cada cadeia elástica foram realizadas utilizando-se um paquímetro digital de precisão e o percentual de deformação plástica foi calculado em relação ao comprimento inicial. A comparação entre os valores médios de deformação plástica sofrida pelos elásticos nos diferentes graus de ativação foi realizada estatisticamente com o auxílio do programa SPSS (Statistical Package for Social Sciences), versão 15.0. Resultados: Os valores médios encontrados, 13,89%, 20,66% e 30,68% de deformação plástica, para os diferentes graus de ativação, respectivamente, foram submetidos a teste estatístico análise de variância (ANOVA) com nível de significância de 5%, tendo sido encontrada significância estatística entre os mesmos. Conclusão: O grau de ativação influenciou de forma significativa a deformação plástica sofrida pelos elásticos testados.

Objective: To evaluate the influence of the degree of activation on the plastic deformation of orthodontic elastic chains according to the stretching duration. Methods: Seventy-two samples of medium size crystal orthodontic elastic chains from the commercial brand Morelli were maintained in a custom-made jig with different degrees of activation (30%, 50% and 70%) of their initial lengths, being 24 elastic chains for each degree of activation. The elastics were maintained in their original plastic packages, as recommended by the manufacturer, until the moment of testing. The jig with the elastics were kept in a plastic recipient containing artificial saliva and stored in an artisanal stove with controlled temperature of 37§C ñ 1§C during the whole experiment, being removed only after 3 weeks of activation. The initial and final lengths of 6 rings of each elastic chain were measured using a precision digital caliper and the percentage of plastic deformation in relation to the initial length was calculated. Comparison among the mean values of plastic deformation suffered by the elastics with the different degrees of activation was performed using the SPSS (Statistical Package for Social Sciences) software, version 15.0. Data were analyzed statistically by ANOVA with significance level of 5%. Results: The mean values of plastic deformation for the 30%, 50% and 70% degrees of activation were 13.89%, 20.66% and 30.68%, respectively, with statistically significant difference (p<0.05) among them. Conclusion: The degree of activation influenced significantly the plastic deformation suffered by the elastics evaluated in this study.

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This work aims to evaluate the fermentability of cellulosic hydrolysates obtained by enzymatic saccharification of sugarcane bagasse pretreated by hydrothermal processing using Candida guilliermondii FTI 20037 yeast. The inoculum was obtained from yeast culture in a medium containing glucose as a carbon source supplemented with rice bran extract, CaCl(2)·2H(2)O and (NH(4))(2)SO(4) in 50 mL Erlenmeyer flasks, containing 20 mL of medium, initial 5.5 pH under agitation of an orbital shaker (200 rpm) at 30°C for 24 h. The cellulosic hydrolysates, prior to being used as a fermentation medium, were autoclaved for 15 min at 0.5 atm and supplemented with the same nutrients employed for the inoculum, except the glucose, using the same conditions for the inoculum, but with a period of 48 h. Preliminary results showed the highest consumption of glucose (97%) for all the hydrolysates, at 28 h of fermentation. The highest concentration of ethanol (20.5 g/L) was found in the procedure of sugarcane bagasse pretreated by hydrothermal processing (195°C/10 min in 20 L reactor) and delignificated with NaOH 1.0% (w/v), 100°C, 1 h in 500 mL stainless steel ampoules immersed in an oil bath.

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The evaluation of hexose and pentose in pre-cultivation of Candida guilliermondii FTI 20037 yeast on xylose reductase (XR) and xylitol dehydrogenase (XDH) enzymes activities was performed during fermentation in sugarcane bagasse hemicellulosic hydrolysate. The xylitol production was evaluated by using cells previously growth in 30.0 gl(-1) xylose, 30.0 gl(-1) glucose and in both sugars mixture (30.0 gl(-1) xylose and 2.0 gl(-1) glucose). The vacuum evaporated hydrolysate (80 gl(-1)) was detoxificated by ion exchange resin (A-860S; A500PS and C-150-Purolite®). The total phenolic compounds and acetic acid were 93.0 and 64.9%, respectively, removed by the resin hydrolysate treatment. All experiments were carried out in Erlenmeyer flasks at 200 rpm, 30°C. The maximum XR (0.618 Umg (Prot) (-1)) and XDH (0.783 Umg (Prot) (-1)) enzymes activities was obtained using inoculum previously growth in both sugars mixture. The highest cell concentration (10.6 gl(-1)) was obtained with inoculum pre-cultivated in the glucose. However, the xylitol yield and xylitol volumetric productivity were favored using the xylose as carbon source. In this case, it was observed maximum xylose (81%) and acetic acid (100%) consumption. It is very important to point out that maximum enzymatic activities were obtained when the mixture of sugars was used as carbon source of inoculum, while the highest fermentative parameters were obtained when xylose was used.

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The enzymatic bioconversion of xylose into xylitol by xylose reductase (XR) is an alternative for chemical and microbiological processes. The partial purified XR was obtained by using the following three procedures: an agarose column, a membrane reactor or an Amicon Ultra-15 50K Centrifugal Filter device at yields of 40 percent, 7 percent and 67 percent, respectively.

A bioconversão enzimática da xilose em xilitol pela xilose redutase (XR) é uma alternativa para as vias química e microbiológica. Avaliouse a purificação parcial da XR, utilizando os três seguintes procedimentos: uma coluna de agarose, um reator com membrana ou tubos de ultracentrifugação Amicon Ultra-15 50K, com rendimento de 40 por cento, 7 por cento ou 67 por cento, respectivamente.

RESUMO

The effect of glycerol on xylose-to-xylitol bioconversion by Candida guilliermondii was evaluated by its addition (0.7 and 6.5 g/l) to semidefined media (xylose as a substrate). The glycerol concentrations were chosen based on the amounts produced during previous studies on xylitol production by C. guilliermondii. Medium without glycerol addition (control) and medium containing glycerol (53 g/l) in substitution to xylose were also evaluated. According to the results, the addition of 0.7 g/l glycerol to the fermentation medium favored not only the yield (Y(P/S)=0.78 g/g) but also the xylitol productivity (Q(P)=1.13 g/l/h). During the xylose-to-xylitol bioconversion, the formation of byproducts (glycerol and ethanol) was observed for all conditions employed. In relation to the cellular growth, glycerol as the only carbon source for C. guilliermondii was better than xylose or xylose and glycerol mixtures, resulting in a maximum cellular concentration (5.34 g/l).

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The enzymatic bioconversion of xylose into xylitol by xylose reductase (XR) is an alternative for chemical and microbiological processes. The partial purified XR was obtained by using the following three procedures: an agarose column, a membrane reactor or an Amicon Ultra-15 50K Centrifugal Filter device at yields of 40%, 7% and 67%, respectively.

RESUMO

The enzymatic bioconversion of xylose into xylitol by xylose reductase (XR) is an alternative for chemical and microbiological processes. The partial purified XR was obtained by using the following three procedures: an agarose column, a membrane reactor or an Amicon Ultra-15 50K Centrifugal Filter device at yields of 40%, 7% and 67%, respectively.

A bioconversão enzimática da xilose em xilitol pela xilose redutase (XR) é uma alternativa para as vias química e microbiológica. Avaliouse a purificação parcial da XR, utilizando os três seguintes procedimentos: uma coluna de agarose, um reator com membrana ou tubos de ultracentrifugação Amicon Ultra-15 50K, com rendimento de 40%, 7% ou 67%, respectivamente.

RESUMO

UNLABELLED: The hormonal changes that occur in a short time span promote modifications all over the woman's body, with physical and emotional manifestations which are frequently observed. AIM: to evaluate the activity of the external ciliated cells in women during their menstrual cycle, observing the effect of hormonal changes caused by the cycle in their 3 phases. METHODS: this is a longitudinal prospective study where 21 women between 20 and 35 years old who did not take any contraceptive medicine were assessed. Transient otoacoustic emissions were evaluated by distortion product during the 3 phases of the menstrual cycle (luteal, follicular and ovulatory phases). The SPSS 13.0 software was used to analyze the data. RESULTS: the phases of menstrual cycle do not alter the amplitude and reproducibility values of the transient otoacoustic emissions. We noticed a difference between the ears in the frequency of 1.5 KHz in the amplitude of emissions by distortion product, and the right ear showed the highest values. CONCLUSION: There are no significant differences in transient otoacoustic emissions and distortion products in the phases of the menstrual cycle.

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As alterações hormonais ocorridas em pouco espaço de tempo promovem modificações em todo o organismo da mulher, com manifestações físicas e emocionais muitas vezes evidentes. OBJETIVO: O objetivo deste estudo foi avaliar a atividade das células ciliadas externas em mulheres durante o ciclo menstrual, observando os efeitos das alterações hormonais impostas pelo ciclo em suas três fases. MATERIAL E MÉTODO: Trata-se de um estudo longitudinal prospectivo que avaliou 21 mulheres entre 20 e 35 anos que não faziam uso de medicamento contraceptivo (dados obtidos em anamnese). Foi realizada avaliação das emissões otoacústicas transientes e por produto de distorção durante as três fases do ciclo hormonal (lútea, folicular e ovulatória). Para análise geral dos dados foi utilizado o programa SPSS 13.0, RESULTADOS: As três fases do ciclo hormonal não alteram os valores de amplitude e reprodutibilidade das emissões otoacústicas transientes e por produto de distorção. Foi verificada diferença entre as orelhas na freqüência de 1,5 kHz na amplitude das emissões por produto de distorção, tendo a orelha direita os maiores valores. CONCLUSÃO: Com a realização deste estudo pôde-se concluir que não há diferenças significantes das emissões otoacústicas transientes e por produto de distorção entre as fases do ciclo hormonal.

The hormonal changes that occur in a short time span promote modifications all over the woman’s body, with physical and emotional manifestations which are frequently observed. AIM: to evaluate the activity of the external ciliated cells in women during their menstrual cycle, observing the effect of hormonal changes caused by the cycle in their 3 phases. METODS: this is a longitudinal prospective study where 21 women between 20 and 35 years old who did not take any contraceptive medicine were assessed. Transient otoacoustic emissions were evaluated by distortion product during the 3 phases of the menstrual cycle (luteal, follicular and ovulatory phases). The SPSS 13.0 software was used to analyze the data. RESULTS: the phases of menstrual cycle do not alter the amplitude and reproducibility values of the transient otoacoustic emissions. We noticed a difference between the ears in the frequency of 1.5 KHz in the amplitude of emissions by distortion product, and the right ear showed the highest values. CONCLUSION: There are no significant differences in transient otoacoustic emissions and distortion products in the phases of the menstrual cycle.

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