Academic literature on the topic 'Total reducing sugars (TRS)'

Reducing sugars produced from agro-industrial wastes by means of hydrolysis represent a promising alternative of chemicals and energy. Yet, large scale production still struggles with several factors involving process complexity, sugars degradation, corrosion, enzyme recyclability, and economic feasibility. More recently, sub and supercritical water hydrolysis has been reported for the production of reducing sugars as a readily available alternative to acid and enzymatic biomass hydrolysis. Accordingly, in this work, the results of batch and semicontinuous lab scale subcritical water hydrolysis experiments of agro-industrial wastes of pea pot and corn stover are discussed. Experiments were carried in the temperature range 250 to 300 °C, pressures up to 3650 psi, residence times up to 30 minutes in batch mode operation, or water flowrates up to 12 mL/min in semicontinuous mode operation. Produced sugars were assessed in the effluent of each experimental run by means of dinitrosalicilic acid method (DNS). A maximum total reducing sugar (TRS) yield of 21.8% was measured for batch pea pot subcritical water hydrolysis experiments at 300°C, 15 minutes, 3650 psi, and 1:6 biomass to water mass ratio. Semicontinuous subcritical water hydrolysis of corn stover showed a maximum TRS accumulated yield of 19% at 290 °C, 1500 psi, and water flowrate of 9 mL/min. The results showed the feasibility of producing reducing sugars from agro-industrial wastes currently discarded through subcritical hydrolysis.

ABSTRACT The objective of this work was to evaluate the effect of applying mixtures of chemical ripeners on the technological quality and agricultural productivity of sugarcane. The experimental design consisted of randomized blocks arranged in split- split-plots with four blocks, the main plots being constituted by sugarcane varieties SP803280 and SP801842. The subplots consisted of the application of the following products with their respective mixtures: control - absence of ripener; Sulfometrom methyl + glyphosate; ethephon + glyphosate; glyphosate and compounds of organic carboxylic radicals + glyphosate. The sub-subplots were composed of evaluation times: 0; 15 and 30 days after applying the products. Samples from each plot were collected manually and sent to the laboratory for the determination of soluble Brix solids (% broth); Sucrose content in the broth - Pol (% broth); Reducing sugars (RS%); Total reducing sugars (TRS%); Fiber (%); Purity (%); Humidity (%) and Total recoverable sugar TRS (kg t-1). The plots were fully harvested and the stems were taken for weighing and for characteristics determination: Yield per hectare (TCH) and Yield of sugar per hectare (TAH). The SP803280 variety was more responsive to the use of mixtures of chemical ripeners. For the technological characteristics, sulfometurom methyl (0.02 kg ha-1) + glyphosate (0.15 L ha-1) presented the best results from 15 days after application. Mixtures of chemical ripeners did not increase the yields of stalks and sugar per area.

An effective and friendly method was developed for the production of reducing sugars (RS) from the hydrolysis of cellulose over the solid catalyst of Ca-montmorillonite (Mt) grafted by non-acidic ionic liquid (Mt-IL) in water. The effect of mass ratio, water dosage, reaction temperature, and time were investigated in a batch reactor. Raw Mt showed only a 7.9% total reducing sugars (TRS) yield for the catalytic hydrolysis of cellulose in water. As the Mt was grafted by -SO3H and IL, the TRS yield greatly increased under the same reaction conditions. The highest TRS yield of 35.7% was obtained on the catalyst of Mt grafted by non-acidic IL at 200 °C with the mass ratio of catalyst to cellulose of 0.2 for 120 min. The high TRS yield for Mt-IL should be attributed to the synergistic effect of the dissolution of cellulose by IL and the exposed metal ions on the layer with water. Although the yield of TRS on Mt-IL decreased gradually with recycling runs, the decrease after the first run was not very serious compared to the fresh catalyst. This work provides a promising strategy for efficient cellulose hydrolysis into fine chemicals by Mt with non-acidic IL.

The quality of the raw material defines the industrial potential production. The harvest of raw sugarcane promoted a favorable environment for the increase of Mahanarva fimbriolata (Stål, 1854) pest that affects the plant development. This research was undertaken to evaluate the effects of M. fimbriolata on sugarcane quality and fermentation process. For the technological analysis, four damage levels and two evaluation periods were evaluated, while four fermentation cycles and two evaluation periods were tested for microbiological analysis, with three replications. The determined parameters were Brix (soluble solids), Pol (apparent sucrose), Purity, reducing sugars (RS), total reducing sugars (TRS), Total Acidity, pH and Total Phenolic Compounds in juice. In the fermentation process cellular viability analysis, yeast sprout and bacterial concentration were carried out. The wine was submitted to alcohol content, TRRS (total residual reducing sugars) and fermentation efficiency. The treatment with 60% of damage steams exhibited the lowest averages of Brix, Pol, Purity and TRS of the juice. An increase of the RS% of the juice and content of total phenolic compounds was observed. The cellular and sprouts viability were reduced with the increase in the damages caused by M. fimbriolata. The fermentation process exhibited larger quantities of contaminators. With the damages, the wine TRRS quantity was superior and, consequently there was a decrease of the alcoholic content and fermentation efficiency. The damages caused by M. fimbriolata affected the quality of the raw material, compromising the fermentative process, and increase the production of phenolic compounds and contaminators.

This work had the purpose of evaluating the efficiency of the pretreatment with alkaline hydrogen peroxide of pineapple bagasse in order to obtain fermentable sugars by applying acid and enzymatic hydrolysis to said residue. Four experimental designs were applied to study the best conditions for the pre-treatment. Total reducing sugars (TRS) concentration was the response and hydrogen peroxide concentration, time and temperature were the independent variables. The studies were conducted using pineapple bagasse with particle sizes of 20 mesh and 48 mesh. Acid saccharification, with 2.9% sulfuric acid (v/v), following the pre-treatment, yielded TRS concentrations that reached 0.094 g of TRS/g of raw bagasse for 20 mesh and 0.101 g of TRS/g of raw bagasse for 48 mesh. The enzymatic saccharification, with 9 FPU/g cellulase and 2% (m/v) of bagasse, reached 0.063 g of TRS/g of raw bagasse for both particle sizes. The peroxide concentration showed a significant influence, the use of high concentrations reduced the TRS output in both hydrolysis. With the results found in this work, it is possible to infer the feasibility of applying pineapple bagasse as a lignocellulosic raw material.

ABSTRACT Sweet sorghum [Sorghum bicolor (L.) Moench] stands out as a complementary crop to sugarcane Saccharum spp. for the production of ethanol, since it has juicy stems with directly fermentable sugars. Due to this fact, there is a need for the analysis of sweet sorghum properties in order to meet the agro-industry demand. This work aimed to develop and study the maturation curves of seven sweet sorghum cultivars in ten harvest dates. The results showed a significant difference between cultivars and harvest dates for all parameters analysed (p≤0.01). Regarding the sugar content, the cultivars BRS508, XBWS80147 and CMSX629 showed the highest means for the total reducing sugars (TRS) and recoverable sugar (RS). In the production of ethanol per tonne of biomass (EP), the cultivars BRS508 and CMSX629 presented the best results.

Ferric (III) chloride, when prepared as an ionic solution, was used to pretreat oil palm empty fruit bunch (OPEFB) before undergoing enzymatic hydrolysis to convert into value-added products. The pretreatment was assisted with microwave irradiation to improve the degradation of recalcitrant structure of lignocellulosic materials with minimum time. The effects of salt concentration, temperature, and duration of pretreatment on the chemical composition of OPEFB and total reducing sugar (TRS) yield were investigated. The results revealed that the best pretreatment occurred at pretreatment time of 10 min, 100 °C, and ferric chloride concentration of 10 w/v%. The TRS yield achieved using the pretreated OPEFB was approximately 0.485 g/g, which was three times higher than the non-pretreated OPEFB, which was only 0.154 g/g. Thus, the ionic solution pretreatment method is a promising alternative for replacing other pretreatment methods.

Enzymatic and dilute acid processes were applied to study the orange bagasse hydrolysis. The moisture, ashes, lignin, cellulose, and hemicellulose contents, of the orange peels, were quantified. The xylanase and cellulase enzymes activities were quantified, as well as their optimum pH and temperatures. The pre dried orange peel biomass was pre-treated with calcium hydroxide, at preestablished conditions. The hydrolysis followed a central composite factorial 2³ design. The cellulase activity was 28.05x10-6 FPU (Filter Paper Units)/m3, the optimum pH was 4.8 and the temperature was 60°C. The results for xylanase were an activity of 199.58x10-3 U/Kg, pH 5.2, and temperature 50°C. The acid hydrolysis TRS (total reducing sugars) values varied from (9.328±0.68 mg)*10-3 TRS per Kg of biomass to (30.15±0.31)*10-3 mg TRS per Kg biomass, the most significant factor was the temperature and the least the time. The enzymatic hydrolysis TRS values varied from (77.33±3.82)*10-3 mg TRS per Kg biomass to (99.66±0.62)*10-3 mg TRS per Kg biomass, the most significant factor was the concentration of cellulase and the least the xylanase concentration

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From the scientific viewpoint, the word ?uncertainty? expresses doubt about an analytic result. The implementation of the concept of uncertainty of measurement is a crucial step that the Brazilian laboratories must take in the process for obtaining the certification of the ability to perform essays in accordance with the Brazilian technical norm ABNT NBR ISO/IEC 17025. Regardless the technical area of application, the determination of the uncertainty of measurement associated with the result of an analysis is extremely important, especially in the food industry. The expanded uncertainty is related with the degree of reliability of an analytical result, and by means of this information it is possible to evaluate if the result of an analysis is consistent, i.e., if the uncertainty associated to the measurement remains inside an acceptable range. When the percentage of uncertainty exceeds a threshold, it is necessary to find the process variables that more intensely contribute to increasing the uncertainty and, in the sequence, to take corrective actions in order to minimize the impact caused for those variables over the uncertainty of measurement. The aim of this study was to detect the uncertainty of measurement associated with the analysis of total reducing sugars (TRS) by the Lane-Eynon method. The equipments used were analytical and semi analytical balances, burettes with 10mL and 25mL, and the food matrix studied was wild honey. To perform the calculations of the standard uncertainty, u, information about the uncertainty of the laboratory materials used in the analysis ? obtained from the certificate of calibration. The combined uncertainty, uc, was obtained by deriving the influence factors and considering, if necessary, the effective degree of freedom, ?eff, as stated in the Welch-Satterthwaite equation. The expanded uncertainty, U, was obtained by multiplying uc by the appropriate coverage factor, k = 2 (at level of confidence of 95,45%). The results showed that the expanded uncertainty obtained for the analysis of TRS was less than 2,0% when the analytical balance was used. The process variable having the greatest impact was the volume (close to 80,0%), followed by the title (close to 20,0%). The analysis of the expanded uncertainty obtained for the analysis of TRS when the semi analytical balance, and 10mL as well as 25mL burettes were used provided reliable results. However, care must be taken in such a combination of equipments, especially when using the 25mL burettes, since the percentage of uncertainty was great than 3,5%, too close to the limit established by the Codex Alimentarius, 4,0%. It was observed that, in this case, the variable having the greatest impact on the uncertainty was the title, with 79,82% (10mL burettes), and 87,10% (25mL burettes).
Do ponto de vista t?cnico-cient?fico, a palavra ?incerteza? expressa a d?vida em rela??o a um resultado anal?tico. A aplica??o do conceito de incerteza de medi??o ? fundamental para os laborat?rios brasileiros que almejam obter o reconhecimento da capacidade de realiza??o de ensaios em conformidade com a norma ABNT NBR ISO/IEC 17025. Independentemente da ?rea de atua??o, ? de extrema import?ncia o estudo e o conhecimento da incerteza de medi??o associada a um resultado de an?lise, em particular quando aplicado ? ind?stria de alimentos. A incerteza expandida informa o grau de confiabilidade de um resultado anal?tico e, atrav?s dela, ? poss?vel avaliar, a um n?vel de abrang?ncia estabelecido, se o resultado de uma an?lise transmite credibilidade, ou seja, se o valor da incerteza est? em uma faixa de concentra??o aceit?vel ou n?o. Quando o percentual de incerteza ultrapassa o limite aceit?vel, ? necess?rio conhecer quais as vari?veis do m?todo que mais contribuem para a incerteza e executar as medidas corretivas a fim de minimizar este impacto e, consequentemente, reduzir a incerteza total. O objetivo geral deste trabalho foi determinar a incerteza expandida associada ? an?lise titulom?trica de a??cares redutores totais (ART) pelo m?todo de Lane-Eynon, tendo como matriz uma amostra de mel, utilizando balan?a anal?tica e semi anal?tica e buretas de 10mL e 25mL. Para o c?lculo da incerteza padr?o (u), utilizaram-se os dados obtidos nos certificados de calibra??o de equipamentos e vidrarias empregados na an?lise. A incerteza combinada ( ) foi obtida derivando os fatores de influ?ncia e considerando, quando necess?rio, o grau de liberdade efetivo (?eff), dado pela Equa??o de Welch-Satterthwaite. Obteve-se a incerteza expandida (U) multiplicando-se por 2 (dois) o valor de para um n?vel de confian?a de 95,45%. Os resultados obtidos mostraram que a incerteza expandida de ART utilizando balan?a anal?tica n?o foi significativa (<2%) e que a vari?vel que mais influenciou foi o volume de amostra gasto (~80%), seguido do T?tulo (~20%). A an?lise da incerteza expandida de ART obtida com balan?a semi anal?tica e buretas de 10mL e 25mL gerou resultados confi?veis. No entanto, deve haver cautela neste caso, especialmente ao se utilizar bureta de 25mL, visto que o valor percentual de incerteza superou 3,5%. Observa-se que a vari?vel que mais contribui para a incerteza foi o T?tulo com 79,82% (bureta de 10mL) e 87,10% (bureta de 25mL).

Mestrado em Engenharia Agronómica - Instituto Superior de Agronomia
This work was conducted in an olive grove near Santarém and its main objective was the determination of soluble carbohydrates content in roots (R), trunk (T), branches over three years (R+), branches of three years (R3) and branches of two years (R2) in cultivar Cobrançosa to integrate a model of olive growth and development. Samples were taken from six plants randomly chosen, three with high crop load (CA) and three with low crop load (CB) in four time points. Sugars contents were determined by three methods, 2- cyanoacetamide (reducing sugars), Somogyi-Nelson (reducing sugars) and anthrone (total soluble sugars) in samples derived from ethanolic extracts (low molecular weight carbohydrates) and from aqueous extracts (high molecular weight carbohydrates). Crop load effect showed weak influence. Regarding carbohydrates contents in each sample, R2 and R3 showed highest sugar content (aproximately 2 mg/100 mg dry weight), and R+ showed lowest content (approximately 1,7 mg/100 mg dry weight). Carbohydrate content increased during growth cycle in all organs, with highest values achieved at endocarp hardening. 2-cyanoacetamide detection showed best results

The aim of this diploma thesis is the assay of total alkaloids in different tobacco types. To measure the content of total alkaloids are utilized types of tobacco used for preparation of tobacco blends and consecutive production of cigarettes. The samples of analyzed tobacco include various countries of cultivation and different crop years. There is described tobacco as a plant, in it contained alkaloids and the utilization of tobacco in the theoretical part. In more detail it deals with the production and construction of cigarettes which is closely related to the content monitoring of total alkaloids in tobacco. The contents of total alkaloids are determined by the continuous flow analyzer- SKALAR. On this spectrophotometer are set the contens of reducing sugars as well. The comparison of total alkaloids contents and reducing sugars from the perspective of single tobacco types, countries of cultivation and crop years is clearly summarized in the experimental part of the thesis that was performed in the company Philip Morris ČR, a.s.

Thesis (Doctor of Engineering in Chemical Engineering)--Cape Peninsula University of Technology, 2018.
Lignocellulosic biomass (agro-waste) has been recommended as the most promising feedstock for the production of bioalcohols, in the biofuel industry. Furthermore, agro-waste is well-known as the most abundant organic matter in the agricultural and forestry product processing industry. However, the challenge with utilizing agro-waste as a feedstock is its highly recalcitrant structure, which limits hydrolysis to convert the holocelluloses into fermentable sugars. Conventional pre-treatment methods such as dilute acid, alkaline, thermal, hot water and enzymatic, have been used in previous studies. The challenge with these conventional methods is the generation of residual toxicants during the pretreatment process, which inhibits a high bioalcohol yield, by reducing the microbial populations’ (fermenter) ability to be metabolically proficient during fermentation. Numerous studies have been developed to improve the engineered strains, which have shown to have an ability to reduce the inhibition and toxicity of the bioalcohols produced or by-products produced during pre-treatment, while enhancing the bioalcohol production. In the present study (chapter 5), evaluation of common conventional methods for the pretreatment of the mixed agro-waste, i.e. (˃45µm to <100µm) constituted by Citrus sinensis, Malus domestica peels, corn cobs from Zea mays and Quercus robur (oak) yard waste without a pre-rinsing step at a ratio of 1:1 at 25% (w/w) for each waste material, was undertaken, focusing on hot water pre treatment followed by dilute acid (H2SO4) pre-treatment. To further pretreat the mixed agro-waste residue, cellulases were used to further hydrolyse the pre-treated agro-waste in a single pot (batch) multi-reaction process. The TRS concentration of 0.12, 1.43 and 3.22 g/L was achieved with hot water, dilute acid and cellulases hydrolysis as sequential pretreatment steps, respectively, in a single pot multi-reaction system. Furthermore, a commercial strain was used to ascertain low (C1 to C3) and high carbon content (C4+) bioalcohol production under aerobic conditions. Multiple bioproducts were obtained within 48 to 72 h, including bioethanol and 1-Butanol, 3-methyl, which were major products for this study. However, undesirable bio-compounds such as phenolics, were detected post fermentation. Since multiple process units characterised by chemical usage and high energy intensivity have been utilized to overcome delignification and cellulolysis, a sustainable, environmental benign pretreatment process was proposed using N. mirabilis “monkey cup” fluids (extracts) to also reduce fermenter inhibitors from the delignification of mixed agrowaste; a process with minimal thermo physical chemical inputs for which a single pot multi-reaction system strategy was used. Nepenthes mirabilis extracts shown to have ligninolytic, cellulolytic and xylanolytic activities, were used as an enzyme cocktail to pretreat mixed agro-waste, subsequent to the furtherance of TRS production from the agro-waste, by further using cellulase for further hydrolysis. N. mirabilis pod extracts were determined to contained carboxylesterases (529.41±30.50 U/L), β-glucosidases (251.94±11.48 U/L) and xylanases (36.09±18.04 U/L), constituting an enzymatic cocktail with a significant potential for the reduction in total residual phenolic compounds (TRPCs). Furthermore, the results indicated that maximum concentration of TRS obtainable was 310±5.19 mg/L within 168 h, while the TRPCs were reduced from 6.25±0.18 to 4.26 ±0.09 mg/L, which was lower than that observed when conventional methods were used. Overall N. mirabilis extracts were demonstrated to have an ability to support biocatalytic processes for the conversion of agro-waste to produce fermentable TRS in a single unit facilitating multiple reactions with minimised interference with cellulase hydrolysis. Therefore, the digestive enzymes in N. mirabilis pods can be used in an integrated system for a second generation biorefinery.

CAPES - Coordenação de Aperfeiçoamento de Pessoal de Nível Superior
CNPq - Conselho Nacional de Desenvolvimento Científico e Tecnológico
FAPEMIG - Fundação de Amparo a Pesquisa do Estado de Minas Gerais
Atualmente, tem-se estudado diversos tipos de pré- tratamentos para reduzir a recalcitrância da biomassa lignocelulósica com intuito de aumentar sua digestibilidade química/enzimática, para que esta possa ser utilizada na produção de etanol e/ou outros bioprodutos de valor agregado. Neste estudo avaliou-se o efeito do pré-tratamento de explosão a vapor catalisada por ácido cítrico e hidróxido de sódio, e do pré-tratamento de deslignificação alcalina nas propriedades químicas e estruturais do bagaço de cana-de-açúcar (BCA), bem como sobre o processo de hidrólise enzimática. O pré-tratamento de explosão a vapor foi realizado em reator de 1,4L sob temperatura de 180 °C com tempo de retenção de 5 min. A etapa de deslignificação com NaOH (2% m:m) foi realizada a 120 °C, sob refluxo de 4h. A caracterização química e estrutural da biomassa in natura e pré-tratada foi realizada por FTIR, MEV, DRX. A hidrólise enzimática foi realizada com volume final de 20 mL constituído de 3% de BCA (massa seca), tampão de citrato de sódio 50 mM (pH=5,0) e 10 FPU do complexo enzimático Cellic® CTec 3. Os frascos foram mantidos sob agitação de 150 rpm a 50ºC por 72 h. Retirou-se alíquotas de 1,5 mL após 0, 12, 24, 36, 48 e 72h para determinação de açúcares redutores totais (ART) pelo método do ácido 3,5-dinitrosalicílico (DNS). O bagaço de cana-de-açúcar apresentou 24,22% de lignina, 27,61% de hemiceluloses e 42,77% de celulose, no entanto após o pré-tratamento de explosão a vapor catalisado com ácido cítrico, obteve-se uma biomassa com menor quantidade de hemiceluloses (16,16%) e com formação de fissuras na parede celular da fibra. O bagaço pré-tratado por explosão a vapor com NaOH apresentou completa desestruturação da fibra, remoção de 65% da lignina e preservação da fração hemicelulósica. Depois de submeter à biomassa lignocelulósica sem tratamento e pré-tratada por explosão a vapor ao processo de deslignificação alcalina observou-se a completa desestruturação da matriz lignocelulósica e a solubilização de 85-90% da lignina em todas as amostras. O índice de cristalinidade da biomassa após os prétratamentos teve uma aumento quando comparado ao material in natura, podendo este ser associado à remoção de componentes amorfos, como a lignina e hemiceluloses, e também da fração amorfa da celulose. Frente ao percentual mássico de biomassa utilizada no processo de hidrólise enzimática valor teórico correspondente a 100% de sacarificação equivale, aproximadamente, a 33,0 g.L-1. Após a hidrólise enzimática (72h) da biomassa in natura e pré-tratada por explosão a vapor obteve-se uma maior concentração de ART e um maior percentual de sacarificação para o bagaço de cana obtido a partir da explosão a vapor com NaOH (23,05 g.L-1, 69,15% de sacarificação). Já na hidrólise da biomassa in natura após processo de deslignificação alcalina a concentração de ART aumentou em 18,33 g.L-1, enquanto que para o bagaço pré-tratado por explosão a vapor com água, ácido cítrico e NaOH seguido da deslignificação alcalina o aumento de ART, correspondeu a 19,67 g.L-1, 19,93 g.L-1 e 6,87 g.L-1. Diante da produção de ART após deslignificação notou-se que o percentual de sacarificação para a biomassa sem tratamento elevou-se de 11,88% para 69,15%, enquanto que para o bagaço após explosão a vapor e deslignificação este percentual ficou entre 82,05% - 89,79%. Por fim, cabe ressaltar que no BCA previamente pré-tratado por explosão a vapor com NaOH, a remoção de lignina após o segundo pré-tratamento teve um acréscimo de apenas 20% e a concentração de ART de 6,87 g.L-1. Dessa forma, acredita-se que ao aumentar a concentração da solução de NaOH para realizar a explosão a vapor poderia-se não necessitar da realização da etapa de deslignificação.
Nowadays, there is various types of studied pre-treatments to reduce the lignocellulosic biomass recalcitrance in order to increase its chemical / enzymatic digestibility, so that it can be used in ethanol production and / or other bioproducts value. This study evaluated the effect of steam explosion pretreatment catalyzed by citric acid and sodium hydroxide, and alkaline delignification pretreatment over chemical and structural properties of sugarcane bagasse, as well as the enzymatic hydrolysis process. Steam explosion pretreatment was conducted in a 1.4 L reactor at temperature of 180 °C and 5 min hold time. The delignification step with NaOH (2% m:m) was performed at 120 °C under reflux for 4 hours. Chemical and structural characterization of raw and pretreated biomass was performed by FTIR, SEM and XRD. Enzymatic hydrolysis was performed with final volume of 20 mL consisting 3% SCB on dryweight basis, sodium citrate buffer 50 mM (pH = 5.0) and 10 FPU of Cellic® Ctec 3 enzyme complex. Flasks were kept under agitation of 150 rpm at 50 °C during 72 h. It was analyzed 1.5 mL aliquots after 0, 12, 24, 36, 48 and 72 hours to determinate total reducing sugars (TRS) by acid 3,5-dinitrosalicílic method (DNS). Sugarcane bagasse showed 24.22% lignin, 27.61% hemicelluloses and 42.77% of cellulose, however after steam explosion pretreatment catalyzed by citric acid, it was obtained a biomass with lesser hemicelluloses amount (16.16%) and cracks formation on fiber cell wall were observed. The bagasse pretreated by steam explosion by NaOH showed complete destructuring of fiber and lignin removal was 65%, while hemicellulosic fraction was preserved. After submitting untreated and pretreated lignocellulosic biomass by steam explosion to alkaline delignification process, complete destructuring and solubilization of the lignocellulosic matrix was observed with 85-90% lignin removal in all samples. The crystallinity index of biomass after pretreatments increased when compared to raw material and this could be associated to amorphous components removal, such as lignin and hemicelluloses, and also the amorphous cellulose fraction. The theoretical value corresponding to 100% of saccharification corresponds to approximately 33.0 g·L-1, compared to the mass percentage of biomass used in the enzymatic hydrolysis process. After 72 h enzymatic hydrolysis of raw and pretreated biomass by steam explosion, the highest concentration of total reducing sugars (TRS) and the highest percentage of saccharification were obtained for sugarcane bagasse (23.05 g·L-1, 69,15% saccharification). In in nature biomass hydrolysis, after alkaline delignification process, ART concentration increased 18.33 g·L-1, while pretreated biomass by steam explosion with water, citric acid and NaOH followed by alkaline delignification increase TRS to 19.67 g·L-1, 19.93 g·L-1 and 6.87 g·L-1. After delignification, it was noted that saccharification percentage for untreated biomass increased from 11.88% to 69.15%, while for bagasse after steam explosion and delignification this percentage was between 82.05% - 89.79%. Lastly, it should be noted that in biomass previously pretreated by NaOH steam explosion, lignin solubilization after the second pretreatment had an increase of only 20% and TRS concentration of 6.87 g·L-1. Thus, it is believed that increasing NaOH solution concentration to perform steam explosion could not need to implement delignification step.
Dissertação (Mestrado)

Diploma thesis is focused on the chemical analysis of the juices of black, red and white currant and jostaberry (Ribes a Ribes x culverwellii). The theoretical part is focused to the definition of fruit, fruit importance in human nutrition, description of Ribes and Ribes x culverwellii genuses, active substances in the currants and the jostaberry, description of selected chemical parameters and the determination of some of them. The procedures of determining for the following chemical parameters are described in the experimental section: determination of reducing sugars, determination of total and soluble solids, formol number, pH, titratable acidity, determination of total phenols and anthocyanins and determination of vitamin C in two samples jostaberry, six varieties of black currants, one variety of white currant and two varieties of red currants. Based on the evaluation of the obtained results, the comparison was made with different varieties and the thesis that "overall comparison of the different varieties in the content of phenolic compounds, vitamin C and anthocyanins appears to be the most promising variety of blackcurrant demon. It should however be noted that the highest content of phenolics and anthocyanins were determined in jostaberry„ has been suggested.

The effect of enzymes with amylolytic activity on the degree of hydrolysis of white corn flour in order to improve the quality of gluten-free bread for special nutrition was studied. Starch was hydrolyzed using mushroom α-amylase and glucoamylase in an amount of 0.005 % and 0.03 % by weight of flour, respectively. As a result, the number of sugars increased to 5.0 % - 5.5 %. The optimal pH value of 4.7 for the action of enzymes was set by adding 0.065 % citric acid. Hydrolysis was subjected to 50 % of white corn flour from the total amount, the humidity of the hydrolyzate was 65%. In addition to mono-and disaccharides, the hydrolysate accumulated 3.5 % on THE basis of dextrins, of which-1.3 % - achro-and maltodextrins, reducing the degree of stale bread.

Enhanced reductive dechlorination (ERD) has rapidly become a remedy of choice for use on chlorinated solvent contamination when site conditions allow. With this approach, solutions of an organic substrate are injected into the affected aquifer to stimulate biological growth and the resultant production of reducing conditions in the target zone. Under the reducing conditions, hydrogen is produced and ultimately replaces chlorine atoms on the contaminant molecule causing sequential dechlorination. Under suitable conditions the process continues until the parent hydrocarbon precursor is produced, such as the complete dechlorination of trichloroethylene (TCE) to ethene. The process is optimized by use of a substrate that maximizes hydrogen production per unit cost. When natural biota are not present to promote the desired degradation, inoculates can be added with the substrate. The in-situ method both reduces cost and accelerates cleanup. Successful applications have been extended from the most common chlorinated compounds perchloroethylene (PCE) and TCE and related products of degradation, to perchlorate, and even explosives such as RDX and trinitrotoluene on which nitrates are attacked in lieu of chloride. In recent work, the process has been further improved through use of beverage industry wastewaters that are available at little or no cost. With material cost removed from the equation, applications can maximize the substrate loading without significantly increasing total cost. The extra substrate loading both accelerates reaction rates and extends the period of time over which reducing conditions are maintained. In some cases, the presence of other organic matter in addition to simple sugars provides for longer performance times of individual injections, thereby working in a fashion similar to emulsified vegetable oil. The paper discusses results of applications at three different sites contaminated with chlorinated ethylenes. The applications have included wastewaters of both natural fruit juices and corn syrup solutions from carbonated beverages. Cost implications include both the reduced cost of substrate and the cost avoidance of needing to pay for treatment of the wastewater.