Simulação da dinâmica operacional de um processo industrial de abate de aves

Este trabalho foi conduzido com o objetivo de implementar um modelo computacional empregando a linguagem de simulação EXTEND TM para: a) simular a dinâmica de atividades de um matadouro-frigorífico de aves; e b) conduzir experimentos de análise de sensibilidade. Para tanto, foi implementado um modelo dinâmico, estocástico e discreto. O sistema real modelado está localizado na região sudoeste do Paraná, onde são abatidas cerca de 500000 aves por dia, empregando três linhas de processamento operando em três turnos diários. Na validação do modelo foram coletados dados relativos a três turnos e comparadas as variáveis de saída obtidas a partir do sistema real e as geradas pelo modelo, as quais foram: i) tempo de processamento; ii) peso vivo total; iii) peso vivo aproveitado; iv) peso de subproduto; v) peso da produção total; vi) peso do frango inteiro; e vii) peso total dos cortes. O modelo implementado demonstrou ser aplicável, uma vez que os erros médios percentuais foram inferiores a 1,13%. O experimento de análise de sensibilidade conduzido, mediante as alterações das velocidades de processamento das linhas em 7000, 8000 e 9000 frangos h-1, apresentou os seguintes valores médios para a variável tempo de processamento: 8,69; 7,86 e 7,86 horas, respectivamente. Além disso, o experimento demonstrou que a velocidade de processamento de 9000 frangos h-1 não implica na direta redução do tempo de processamento, pois a cadência de chegada das cargas pode ter ocasionado períodos de ociosidade do matadouro-frigorífico.

Esterilização de farinha de subprodutos animais em esterilizador industrial

As farinhas de subprodutos animais se apresentam como uma fonte praticamente completa da maioria dos aminoácidos requeridos para uma alimentação equilibrada. Estas farinhas são amplamente usadas para corrigir as deficiências nutricionais, que ocorrem em outras matérias-primas para rações, como os farelos de origem vegetal. No entanto, constituem um ambiente favorável à proliferação de microrganismos, tanto durante o processamento quanto na estocagem. A Portaria SARC 002 de 13/02/2003 no Anexo I da Instrução Normativa Número 15 do Ministério da Agricultura, Pecuária e Abastecimento propõe que a etapa de esterilização das farinhas poderá ser realizada antes do processo de cocção dos subprodutos ou na própria farinha, contanto que seja empregado vapor saturado direto a uma temperatura mínima de 133 °C por um tempo mínimo de 20 minutos. Industrialmente, o que se deseja é obter um produto final com padrões higiênicos sanitários aceitáveis, com teor proteico o mais alto possível. Nesse sentido, o objetivo deste trabalho foi investigar diferentes estratégias de processamento da farinha de subprodutos de indústria de aves, observando aquela mais eficiente para a esterilização: se no subproduto antes da digestão ou se na própria farinha. Foram realizados testes em escala piloto com capacidade para 150 kg e em escala industrial com capacidade de 3.000 kg. O processo de esterilização em escala industrial apresentou um melhor desempenho comparado com o processo piloto. O teor de proteína aumentou em todos os testes e a digestibilidade final da farinha foi de aproximadamente 92%, o que eleva seu valor de mercado. Com relação à eliminação de microrganismos, o processo industrial foi eficiente, uma vez que não foi verificada contagem em nenhum dos três testes realizados.

Evaluation of process parameters in the industrial scale production of fish nuggets

This work reports the use of experimental design for the assessment of the effects of process parameters on the production of fish nuggets in an industrial scale environment. The effect of independent factors on the physicochemical and microbiological parameters was investigated through a full 24 experimental design. The studied factors included the temperature of fish fillet and pulp in the mixer, the temperature of the added fat, the temperature of water and the ratio of protein extraction time to emulsion time. The physicochemical analyses showed that the higher temperature of the pulp and fillet of fish, the lower the protein in the final product. Microbiological analyses revealed that the counting of Staphylococcus coagulase positive, total and thermo-tolerant coliforms were in accordance with the current legislation.

Commercial spices and industrial ingredients: evaluation of antioxidant capacity and flavonoids content for functional foods development

The aim of this work was to evaluate spices and industrial ingredients for the development of functional foods with high phenolic contents and antioxidant capacity. Basil, bay, chives, onion, oregano, parsley, rosemary, turmeric and powdered industrial ingredients (β-carotene, green tea extract, lutein, lycopene and olive extract) had their in vitro antioxidant capacity evaluated by means of the Folin-Ciocalteu reducing capacity and DPPH scavenging ability. Flavonoids identification and quantification were performed by High Performance Liquid Chromatography (HPLC). The results showed that spices presented a large variation in flavonoids content and in vitro antioxidant capacity, according to kind, brand and batches. Oregano had the highest antioxidant capacity and parsley had the highest flavonoid content. The industrial ingredient with the highest antioxidant capacity was green tea extract, which presented a high content of epigalocatechin gallate. Olive extract also showed a high antioxidant activity and it was a good source of chlorogenic acid. This study suggests that oregano, parsley, olive and green tea extract have an excellent potential for the development of functional foods rich in flavonoids as antioxidant, as long as the variability between batches/brands is controlled.

Evaluation of antioxidant activity of agro-industrial waste of acerola (Malpighia emarginata D.C.) fruit extracts

This study was carried out to evaluate the antioxidant capacity of the agro-industrial waste from acerola. Hydroacetone, hydroethanolic, and hydromethanolic extracts were obtained using the sequential extraction process, and they were screened for their free radical DPPH• (1,1-diphenyl-2-picrilhidrazil) and ABTS•+ (2,2'-azino-bis-(3-etilbenzotiazolin 6-sulfonic acid) scavenging activity and their effect on the linoleic acid peroxidation by the ferric thiocyanate method. Soybean oil with the addition of the extracts (200 ppm) was submitted to Schaal oven test (60 °C, 28 days), in which the samples were analyzed for peroxide value and conjugated dienes. Hydroethanolic and hydromethanolic extracts exhibited good DPPH scavenging activity (low value of EC50 and TEC50 and high value of AE), good ABTS scavenging capacity (1445.1 and 1145.5 µMol TEAC.g-1, respectively), and high percentage inhibition of peroxidation of linoleic acid (96.12 and 91.84%, respectively) and showed the ability to retard the formation of peroxides and conjugated dienes.

Study of the enthalpy-entropy mechanism from water sorption of orange seeds (C. sinensis cv. Brazilian) for the use of agro-industrial residues as a possible source of vegetable oil production

Orange seeds are a promising agroindustry-waste which can be implemented in the extraction and production of vegetable oil. The relationship between moisture content and water activity provides useful information for the processing and storage of this waste item. The aim of this study was to determine the mechanism of water sorption enthalpy-entropy of orange seeds (C. sinensis cv. Brazilians) according to the moisture content. Therefore, desorption isotherms were determined at five different temperature (30, 40, 50, 60, and 70 ºC) under a wide range of moisture content (0.005-0.057 kg kg-1 d.b.) and water activity (0.02-0.756). Theoretical and empirical models were used for modeling the desorption isotherms. An analytical solution of the Clausius-Clapeyron equation was proposed to compute the isosteric heat of sorption, the differential entropy, and Gibbs free energy using the Oswin model when the effect of temperature on the hygroscopic equilibrium was considered.

Alterations of palm oil (Elaeis guineensis) in the continuous industrial par frying of breaded chicken snacks

The physical and chemical alterations in palm oil during continuous industrial par frying of breaded chicken snacks were evaluated using a pseudo first-order kinetic model. The acidity index, refractive index, concentration of polar compounds, viscosity, color, and absorbance (232 and 268 nm) of 238 samples of the frying oil collected during 26 days of production were analyzed. For all of the analyses, the results of the oil were below the limits recommended for oil disposal, indicating that the processing conditions were safe and that under these experimental conditions the oil remained suitable for frying. The linear regressions were significant for refractive index, content of polar compounds, and lightness (L*). The content of polar compounds was determined using a cooking oil tester, and it had the best fit to the proposed model and can be used as an effective index for monitoring palm oil during the continuous par frying of breaded chicken snacks. The high turnover rate of the oil was important for maintaining the oil in good running conditions.

Assessing environmental impacts using a comparative LCA of industrial and artisanal production processes: "Minas Cheese" case

This study uses the Life Cycle Assessment (LCA) methodology to evaluate and compare the environmental impacts caused by both the artisanal and the industrial manufacturing processes of "Minas cheese". This is a traditional cheese produced in the state of Minas Gerais (Brazil), and it is considered a "cultural patrimony" in the country. The high participation of artisanal producers in the market justifies this research, and this analysis can help the identification of opportunities to improve the environmental performance of several stages of the production system. The environmental impacts caused were also assessed and compared. The functional unit adopted was 1 kilogram (Kg) of cheese. The system boundaries considered were the production process, conservation of product (before sale), and transport to consumer market. The milk production process was considered similar in both cases, and therefore it was not included in the assessment. The data were collected through interviews with the producers, observation, and a literature review; they were ordered and processed using the SimaPro 7 LCA software. According to the impact categories analyzed, the artisanal production exerted lower environmental impacts. This can be justified mainly because the industrial process includes the pasteurization stage, which uses dry wood as an energy source and refrigeration.

Optimization of the extraction process of polyphenols from cashew apple agro-industrial residues

The goal of this study was to determine the chemical composition of cashew apples agro-industrial residue and optimize the process of polyphenols extraction in this residue. The extraction process conditions were defined using a 24-1 fractional factorial experimental design using acetone and methanol as solvents. The independent variables were: time (30 to 90 min), temperature (30 to 50 °C), solvent concentrations (50% to 90%), agitation speed (100 to 300 rpm); the dependent variables were: total phenolic content and DPPH scavenging capacity. The optimized process was carried out by applying the Central Composite Rotational Design (CCRD) considering the results obtained with the 24-1 fractional factorial experimental design. The residue presented bioactive compounds in its composition, with emphasis on the content of total phenolic compounds (1975.64 mg/ 100 g). The extraction process was not affected by methanol; however, acetone affected the amounts of extracted phytochemicals. Extracts with high levels of polyphenols and strong DPPH scavenging capacity (> 80%) were obtained using 55% acetone, 30 minutes, 30 °C, and 150 rpm. The results showed that cashew apple residue is a potential natural source of bioactive compounds with strong antioxidant capacity. These compounds could be used partially or totally to replace synthetic antioxidants.