872 resultados para soybean acid oil


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Biofuels derived from industry waste have potential to substitute fossil fuels (Diesel and Gasoline) in internal combustion (IC) engines. Use of waste streams as fuels would help to reduce considerably life-cycle greenhouse gas emissions and minimise waste processing costs. In this study an investigation into the fuel properties of two waste derived biofuels were carried out, they are: (i) Glidfuel (GF) biofuel - a waste stream from paper industry, and (ii) Palm Oil Mill Effluent (POME) biodiesel - biodiesel produced from palm oil industry effluent through various treatment and transesterification process. GF and POME was mixed together at various proportions and separately with fossil diesel (FD) to assess the miscibility and various physical and chemical properties of the blends. Fuel properties such as kinematic viscosity, higher heating value, water content, acid number, density, flash point temperature, CHNO content, sulphur content, ash content, oxidation stability, cetane number and copper corrosion ratings of all the fuels were measured. The properties of GF, POME and various blends were compared with the corresponding properties of the standard FD. Significance of the fuel properties and their expected effects on combustion and exhaust emission characteristics of the IC engine were discussed. Results showed that most properties of both GF and POME biodiesel were comparable to FD. Both GF and POME were miscible with each other, and also separately with the FD. Flash point temperatures of GF and POME biodiesel were 40.7°C and 158.7°C respectively. The flash point temperature of GF was about 36% lower than corresponding FD. The water content in GF and FD were 0.74 (% wt) and 0.01 (% wt) respectively. Acidity values and corrosion ratings of both GF and POME biodiesel were low compared to corresponding value for FD. The study concluded that optimum GF-POME biofuel blends can substitute fossil diesel use in IC engines.

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Provide healthier meat to consumers of pig farmers has required an adjustment of nutrition and feed management. Nutrition is a primary factor in defining the qualitative aspects of pork, because through it we can modify the fatty acid profile. The objective of this study was to analyze the effects of adding bran bagasse cashew (FBC) in diets for finishing pigs, on carcass traits and meat quality. 20 crossbred barrows with an average initial weight of 57.93 ± 3.67 kg / BW were used Diets were formulated based on corn and soybean meal containing vegetable oil, commercial core and different levels of inclusion of the bran bagasse cashew ( 0.0, 7.5 % , 15.0 % , 22.5 % and 30.0 % ) . The experimental design was a randomized block with 5 treatments and 4 replications. Quantitative, qualitative, fatty acid profile of the longissimus muscle and fat area parameters were evaluated. It was observed that with the inclusion of FBC, the parameters of carcass yield, backfat thickness, fat area had a negative linear effect relationship and meat / fat positive effect. Regarding the profile of fatty acids in fat area, the content of linoleic fatty acid level of 30 % of FBC was 18.2 % higher ( P < 0.05 ) at the level of 0.0 % and the arachidonic level of 22.5 % was higher than 33.3 % and 37.5 % at levels of 0.0 % and 15.0 % ( FBC ) respectively. It is concluded that finishing pigs may be food diets containing up to 30 % of FBC, improving the quality of housing for lower fat deposition and modification in the fatty acid profile.

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The main driver for the investigation of fast pyrolysis oil marine fuel blends is EU directive 2012/33/EU which aims to cut the sulphur content of marine fuel and thereby reduce air pollution caused by marine vessels. The aim of this study was to investigate the miscibility of 3- and 4- component blends containing pyrolysis oil, 1-butanol, biodiesel (RME) and/or marine gas oil (MGO). The ideal blend would be a stable homogenous product with a minimum amount of butanol, whilst maximising the amount of pyrolysis oil. A successful blend would have properties suitable for use in marine engines. In order to successfully utilise a marine fuel blend in commercial vessels it should meet minimum specification requirements such as a flash point ≥60°C. Blends of pyrolysis oil, RME, MGO and 1-butanol were evaluated and characterised. The mixed blends were inspected after 48 hours for homogeneity and the results plotted on a tri-plot phase diagram. Homogenous samples were tested for water content, pH, acid number, viscosity and flash point as these give indicate a blend’s suitability for engine testing. The work forms part of the ReShip Project which is funded by Norwegian industry partners and the Research Council of Norway (The ENERGIX programme).

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The soybean is the grain in which greater food dependency has Mexico, reason why as of 2008, the government has promoted his culture, granting excellent subsidies, as much to producers as to buyers of the grain, thus contributing to a recent process of expansion in certain states, as it happens in Campeche. The objetive of this article is the analysis of the characteristics and effects of those supports, as well as of the rest of factors that until today they have taken to the producers of the mentioned state to initiate or to expand the cultivation of the soybean. The findings of the investigation reveal that although the producers have improved their levels of income, the process is vulnerable, as it depends on variables like the governmental supports, the international prices of the soybean and exchange rate. Although the study of the negative effects of genetically modified soybeans (GM) in other areas (environment, biodiversity, deforestation, human and animal health) is not the purpose of this investigation, some information will be provided, as on the conflict between soybean producers and beekeepers in the state of Campeche.

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In the past decade, several major food safety crises originated from problems with feed. Consequently, there is an urgent need for early detection of fraudulent adulteration and contamination in the feed chain. Strategies are presented for two specific cases, viz. adulterations of (i) soybean meal with melamine and other types of adulterants/contaminants and (ii) vegetable oils with mineral oil, transformer oil or other oils. These strategies comprise screening at the feed mill or port of entry with non-destructive spectroscopic methods (NIRS and Raman), followed by post-screening and confirmation in the laboratory with MS-based methods. The spectroscopic techniques are suitable for on-site and on-line applications. Currently they are suited to detect fraudulent adulteration at relatively high levels but not to detect low level contamination. The potential use of the strategies for non-targeted analysis is demonstrated.

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The objective was the development a methodology to label organic compounds with radioactive iodine (123I) from the reaction of organic compound with iodine nomochloride (ICL). The process begins with the production of 123ICl from the oxidation of potassium iodate in acid medium. The ICL labeled with 123I is extracted from aqueous phase using diethyl ether and then mixed with the organic compound to be labeled and the process is based on adding the radioactive iodine to the Carbon-Carbon double bonds of the organic compound. To measure the efficiency of the labeling process, in all stages samples were collected and the total activity of 123I was measure. The results show a production yield of 82% for lubricant oil and 85% for gasoline and diesel.

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Obesity is positively correlated to dietary lipid intake, and the type of lipid may play a causal role in the development of obesity-related pathologies. A major protein secreted by adipose tissue is adiponectin, which has antiatherogenic and antidiabetic properties. The aim of this study was to evaluate the effects of four different high-fat diets (enriched with soybean oil, fish oil, coconut oil, or lard) on adiponectin gene expression and secretion by the white adipose tissue (WAT) of mice fed on a selected diet for either 2 (acute treatment) or 60 days (chronic treatment). Additionally, 3T3-L1 adipocytes were treated for 48 h with six different fatty acids: palmitic, linoleic, eicosapentaenoic (EPA), docosahexaenoic (DHA), lauric, or oleic acid. Serum adiponectin concentration was reduced in the soybean-, coconut-, and lard-enriched diets in both groups. Adiponectin gene expression was lower in retroperitoneal WAT after acute treatment with all diets. The same reduction in levels of adiponectin gene expression was observed in epididymal adipose tissue of animals chronically fed soybean and coconut diets and in 3T3-L1 cells treated with palmitic, linoleic, EPA, and DHA acids. These results indicate that the intake of certain fatty acids may affect serum adiponectin levels in mice and adiponectin gene expression in mouse WAT and 3T3-L1 adipocytes. The effects appear to be time dependent and depot specific. It is postulated that the downregulation of adiponectin expression by dietary enrichment with soybean oil or coconut oil may contribute to the development of insulin resistance and atherosclerosis.

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Background Dietary lipids are directly related to the composition of adipose tissue, aetiology of obesity and arousal of obesity-related pathologies, like chronic inflammation states. Haptoglobin is an acute phase protein secreted by the liver and white adipose tissue, and its blood levels vary according to the volume of fat in the body. Aim of the study To investigate the effect of diets enriched with large amounts of dietary fats, which differ in their fatty acid composition, on the haptoglobin gene expression by visceral and subcutaneous adipose tissue of mice fed for 2 days or 8 weeks. 3T3-L1 cells were treated with fatty acids that are found in those types of dietary fats. Methods Mice were treated acutely (for 2 days) or chronically (for 8 weeks) with diets enriched with soybean oil, fish oil, coconut oil or lard. 3T3-L1 cells were treated with six different fatty acids. Haptoglobin gene expression was quantified by northern blotting. Results Both chronic and acute treatment with lard, which is rich in long chain saturated fatty acids, increased the haptoglobin mRNA expression in the retroperitoneal and epidydimal white adipose tissues. Chronic treatment with coconut oil, which is rich in medium chain saturated fatty acids, increased the haptoglobin expression in the epidydimal and subcutaneous depots. In 3T3-L1, palmitic acid increased the haptoglobin gene expression. Conclusion The type of lipids in the diet can differently modulate the white adipose tissue gene expression of haptoglobin, and saturated fatty acids play a major role in promoting a pro-inflammatory environment. This response is fat pad specific and dependant on the duration of treatment.

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Metabolism in an environment containing of 21% oxygen has a high risk of oxidative damage due to the formation of reactive oxygen species. Therefore, plants have evolved an antioxidant system consisting of metabolites and enzymes that either directly scavenge ROS or recycle the antioxidant metabolites. Ozone is a temporally dynamic molecule that is both naturally occurring as well as an environmental pollutant that is predicted to increase in concentration in the future as anthropogenic precursor emissions rise. It has been hypothesized that any elevation in ozone concentration will cause increased oxidative stress in plants and therefore enhanced subsequent antioxidant metabolism, but evidence for this response is variable. Along with increasing atmospheric ozone concentrations, atmospheric carbon dioxide concentration is also rising and is predicted to continue rising in the future. The effect of elevated carbon dioxide concentrations on antioxidant metabolism varies among different studies in the literature. Therefore, the question of how antioxidant metabolism will be affected in the most realistic future atmosphere, with increased carbon dioxide concentration and increased ozone concentration, has yet to be answered, and is the subject of my thesis research. First, in order to capture as much of the variability in the antioxidant system as possible, I developed a suite of high-throughput quantitative assays for a variety of antioxidant metabolites and enzymes. I optimized these assays for Glycine max (soybean), one of the most important food crops in the world. These assays provide accurate, rapid and high-throughput measures of both the general and specific antioxidant action of plant tissue extracts. Second, I investigated how growth at either elevated carbon dioxide concentration or chronic elevated ozone concentration altered antioxidant metabolism, and the ability of soybean to respond to an acute oxidative stress in a controlled environment study. I found that growth at chronic elevated ozone concentration increased the antioxidant capacity of leaves, but was unchanged or only slightly increased following an acute oxidative stress, suggesting that growth at chronic elevated ozone concentration primed the antioxidant system. Growth at high carbon dioxide concentration decreased the antioxidant capacity of leaves, increased the response of the existing antioxidant enzymes to an acute oxidative stress, but dampened and delayed the transcriptional response, suggesting an entirely different regulation of the antioxidant system. Third, I tested the findings from the controlled environment study in a field setting by investigating the response of the soybean antioxidant system to growth at elevated carbon dioxide concentration, chronic elevated ozone concentration and the combination of elevated carbon dioxide concentration and elevated ozone concentration. In this study, I confirmed that growth at elevated carbon dioxide concentration decreased specific components of antioxidant metabolism in the field. I also verified that increasing ozone concentration is highly correlated with increases in the metabolic and genomic components of antioxidant metabolism, regardless of carbon dioxide concentration environment, but that the response to increasing ozone concentration was dampened at elevated carbon dioxide concentration. In addition, I found evidence suggesting an up regulation of respiratory metabolism at higher ozone concentration, which would supply energy and carbon for detoxification and repair of cellular damage. These results consistently support the conclusion that growth at elevated carbon dioxide concentration decreases antioxidant metabolism while growth at elevated ozone concentration increases antioxidant metabolism.

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A modificação estrutural de óleos e gorduras é uma das principais áreas de interesse de pesquisa em diferentes setores industriais. No caso da indústria de alimentos, a interesterificação é empregada para melhorar propriedades nutricionais e funcionais, em que se obtêm compostos diferentes dos que lhes deram origem. As lipases microbianas são os biocatalisadores mais utilizados industrialmente, por serem mais estáveis, específicas e com propriedades bem mais diversificadas que as lipases de outras fontes. Este trabalho objetivou, primeiramente, a caracterização da gordura da pele de frango (GPF) e sua comparação com óleo de soja, como referência, visando a utilização de GPF em reações de interesterificação. Para isto foram caracterizados quanto aos índices de rancidez hidrolítica e oxidativa, bem como de matéria insaponificável, índices de saponificação, refração e iodo. Foi realizado ainda o fracionamento e perfil de ácidos graxos destes lipídios e suas frações, com o cálculo de seus índices nutricionais. Foi verificado que a GPF apresentou qualidade satisfatória devido aos baixos índices de acidez (0,65 g ácido oleico.100 g -1 ), peróxido (2,14 meq.kg-1 ), p-anisidina (0,70 unidades de absorvância.g-1 ), além de fonte de ácidos graxos mono-insaturados (40%), sendo fonte promissora para estudos de interesterificação. Em um segundo momento o objetivo foi produzir lipídios modificados ricos em ácidos graxos essenciais a partir da gordura da pele de frango e ácidos graxos ramificados, utilizando lipase sn-1,3 específica e interesterificação do tipo acidólise. Foram estudados os fatores concentração de enzima, adição de água, proporção de substratos e tempo, segundo um planejamento experimental fatorial completo 2 4 . As separações analíticas foram executadas em placas de cromatografia de camada delgada, sendo as frações posteriormente extraídas, ressuspensas e injetadas no cromatógrafo a gás. Foi verificado que a adição de água ao meio reacional apresentou efeito significativo (p<0,05) para todos ácidos graxos avaliados dos triacilgliceróis, sendo que para o ácido essencial linoleico (C18:2) o efeito do tempo de reação também foi significativo, sendo verificado que quanto maior o tempo de reação, menor a quantidade de água a ser adicionada. Em um terceiro momento, o objetivo foi produzir éster fenólico a partir do DHCA, além de realizar reações de transesterificação deste éster com tricaprilina. Para a reação de transesterificação, foi utilizado um delineamento composto central rotacional (DCCR) variando a quantidade de enzima, tempo de reação e temperatura sobre a resposta (%) dos reagentes consumidos. A lipase Novozym® 435 de Candida antarctica foi utilizada como catalisador de todas reações. Foi verificado que a maior produção de éster (50%) ocorreu em oito dias. Nas reações de transesterificação, as relações molares em que houve maior consumo do éster produzido foram 1:5 e 1:10, sendo obtidos 21,1% e 29,6% de residual de dihidrocafeato de octila, respectivamente em 24 h. Foi observado que em altas temperaturas e tempo superior a 26 h, houve o menor residual de dihidrocafeato de octila (18,2%). Foram identificados três diferentes compostos fenólicos, contendo em sua estrutura dihidrocafeato de octila e ácido caprílico.

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O presente trabalho visa o desenvolvimento de um processo para a produção de biodiesel partindo de óleos de alta acidez, aplicando um processo em duas etapas de catálise homogênea. A primeira é a reação de esterificação etílica dos ácidos graxos livres, catalisada por H2SO4, ocorrendo no meio de triglicerídeos e a segunda é a transesterificação dos triglicerídeos remanescentes, ocorrendo no meio dos ésteres alquílicos da primeira etapa e catalisada com álcali (NaOH) e álcool etílico ou metílico. A reação de esterificação foi estudada com uma mistura modelo consistindo de óleo de soja neutro acidificado artificialmente com 15%p de ácido oleico PA. Este valor foi adotado, como referência, devido a certas gorduras regionais (óleo de mamona advinda de agricultura familiar, sebos de matadouro e óleo de farelo de arroz, etc.) apresentarem teores entre 10-20%p de ácidos graxos livres. Nas duas etapas o etanol é reagente e também solvente, sendo a razão molar mistura:álcool um dos parâmetros pesquisados nas relações 1:3, 1:6 e 1:9. Outros foram a temperatura 60 e 80ºC e a concentração percentual do catalisador, 0,5, 1,0 e 1,5%p, (em relação à massa de óleo). A combinatória destes parâmetros resultou em 18 reações. Dentre as condições reacionais estudadas, oito atingiram acidez aceitável inferior a 1,5%p possibilitando a definição das condições para aplicação ótima da segunda etapa. A melhor condição nesta etapa ocorreu quando a reação foi conduzida a 60°C com 1%p de H2SO4 e razão molar 1:6. No final da primeira etapa foram realizados tratamentos pertinentes como a retirada do catalisador e estudada sua influência sobre a acidez final, utilizando-se de lavagens com e sem adição de hexano, seguidas de evaporação ou adição de agente secante. Na segunda etapa estudaram-se as razões molares de óleo:álcool de 1:6 e 1:9 com álcool metílico e etílico, com 0,5 e 1%p de NaOH assim como o tratamento da reação (lavagem ou neutralização do catalisador) a 60°C, resultando em 16 experimentos. A melhor condição nesta segunda etapa ocorreu com 0,5%p de NaOH, razão molar óleo:etanol de 1:6 e somente as reações em que se aplicaram lavagens apresentaram índices de acidez adequados (<1,0%p) coerentes com os parâmetros da ANP.

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No presente trabalho foi utilizado o processo de produção de biodiesel a partir da transesterificação de blendas de óleo de mamona e soja com etanol empregando-se como catalisador NaOH e posterior adição de H2SO4 para a neutralização do catalisador, visando a quebra de sabões e a melhor separação do biodiesel de seus co-produtos. Foi investigada a reação de transesterificação em blendas de óleo de mamona:soja nas proporções de 10:90, 20:80, 30:70, 40:60, 50:50, 60:40, 70:30, 80:20 e 90:10, sendo que as proporções que apresentaram melhores rendimentos foram 30:70, 60:40 e 80:20. O biodiesel obtido das blendas como melhor rendimento foram submetidos a medições viscosimétricas, sendo a proporção 30:70 a que apresentou a viscosidade mais próxima à especificada pela ANP (6,12 mm2 /s). O biodiesel etílico produzido com a blenda 30:70 obtido na transesterificação foi submetido a esterificação para diminuir o índice de acidez, utilizando H2SO4 como catalisador em concentrações de 5% e 10% em relação a massa de ácidos graxos livres, com álcool etílico numa razão molar de 60:1 e 80:1 álcool:ácido graxo. Para a reação de transesterificação, também foi estudada, a influência da concentração do catalisador no rendimento de biodiesel etílico e na formação de sabão. A quantidade de sabão formado no processo variou de 5,70% a 9,54% para 1% a 2% de catalisador, respectivamente.

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No presente trabalho foi investigada a transesterificação de blendas dos óleos de soja e de tungue com metanol ou etanol empregando catalisador alcalino (NaOH ou KOH). Foi investigado o tempo reacional, a proporção da blenda, a concentração e o tipo de catalisador, tipo de álcool e razão molar, temperatura e metodologia empregada no tratamento da reação. Nas reações com metanol obtiveram-se melhores conversões com tempo reacional de 1,5h; temperatura de 60°C; proporção blenda dos óleos de soja e de tungue de 90:10 (m/m); concentração de NaOH de 0,5% em relação a massa da blenda e razão molar metanol:blenda de 6:1. O tratamento dos ésteres metílicos produzidos na reação foi realizado por lavagem com água a 60°C após o processo de decantação das fases, metodologia C. O rendimento de ésteres metílicos foi superior a 96% e, o teor de mono-, di- e triacilglicerídeos, glicerol livre e total ficou abaixo dos limites estabelecidos pela ANP, indicando boa conversão (> 96,5%). Nas reações com etanol verificou-se que as melhores condições reacionais foram com uma concentração de catalisador de 0,8% de NaOH em relação a massa da blenda, razão molar etanol:blenda de 9:1, tempo de 1,5h e temperatura de 60°C. O tratamento dos produtos da reação foi realizado por lavagem com água a 60°C após o processo de remoção do etanol e decantação das fases, metodologia D. A concentração do catalisador foi um fator determinante na separação das fases. Uma maior concentração de catalisador favorece a saponificação, dificultando a separação das fases e afetando o rendimento do biodiesel sintetizado, tanto para o metílico quanto o etílico. O índice de acidez, tanto para o biodiesel metílico como o etílico, para qualquer proporção da blenda dos óleos de soja e tungue, ficaram dentro das normas da ANP, com valores abaixo de 0,5 mg.g-1 de KOH.

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No Brasil o biodiesel é utilizado em misturas com óleo diesel em proporções de 5%, sem que haja modificações nos motores. Com o intuito de diversificar a utilização de oleaginosas não comestíveis no ramo dos biocombustíveis, e ainda vincular a produção com agricultura sustentável, uma alternativa para o RS é a utilização do óleo de tungue para a produção de biodiesel. A caracterização e quantificação de ácidos graxos do biodiesel de tungue, torna-se importante devido à seu exclusivo perfil graxo. Neste trabalho, foi estudado o desenvolvimento e validação de método para a determinação do perfil graxo do biodiesel metílico de tungue e blendas com soja utilizando GC-MS. Os parâmetros de validação considerados foram: curva analítica, linearidade, seletividade, limite de detecção e quantificação, robustez, precisão e exatidão. Para determinar as melhores condições cromatográficas, foram testadas diferentes programações de temperatura no forno cromatográfico; fluxo de gás; temperatura do injetor, detector e interface; e modo de injeção. As condições do GCMS após a otimização foram: injeção de 1 µL com injeção em alta pressão (300 kPa), T do injetor: 250 ºC, injeção split 1:30, fluxo de 1 mL min-1, coluna Rtx-5MS com dimensões 30 m x 0,25 mm x 0,25 µm, T forno: isoterma de 2 min a 130 ºC, aumento de 20 ºC/min até 220 ºC, aumento de 0,5ºC/min até 223ºC, aumento de 7 ºC/min até 250 ºC e isoterma em 250 ºC por 3 min, resultando em 20 min de análise. A temperatura da fonte e interface foram de 200 ºC e 250 ºC, respectivamente, com o MS no modo full scan, ionização por impacto eletrônico a 70 eV, e intervalo de massas de 30 a 500 u.m.a. A identificação do α-eleosteárico foi baseada na fragmentação característica do composto, pela comparação com o espectro do ácido linolênico, e ainda pelo tempo de retenção do composto. Na validação, as curvas analíticas apresentaram valores de r maiores que 0,99. O LD e LQ foram adequados, permitindo a quantificação de ésteres na concentração mínima de 0,6%. Os valores de exatidão ficaram entre 86 e 117%, com RSD% menores que 8%. O efeito matriz também foi avaliado, sendo que esse efeito foi considerado médio para a maioria dos compostos, ficando entre ± 20 e 50%. Durante a aplicação do método, o mesmo se mostrou adequado para amostras de biodiesel metílico de tungue e blendas com soja, nas proporções de 15:85, 20:80 e 25:75 (T:S, v/v). A aplicabilidade do método também foi testada para o biodiesel de soja, obtendo resultados satisfatórios, mostrando-se assim, além de tudo, ser um método robusto.

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Deep-fat frying is susceptible to induce the formation of undesirable products as lipid oxidation products and acrylamide in fried foods. Plantain chips produced by small-scale producers are sold to consumers without any control. The objective of this study was to evaluate the quality of plantain chips from local producers in relation to production process parameters and oils, and to identify the limiting factors for the production of acrylamide in plantain chips. Samples of frying oils and plantain chips prepared with either palm olein or soybean oil were collected from 10 producers in Yaoundé. Quality parameters determined in this study were: fatty acid composition of the oils, determined by gas chromatography (GC) of free acid methyl ester; trans fatty acids, determined by Fourier transform infra-red spectroscopy; Tocopherols and tocotrienols as markers of nutritional quality were analyzed by High Performance Liquid Chromatography in isocratic mode. Free fatty acids and acylglycerols as markers of lipid hydrolysis were analyzed by GC of trimethylsilyl derivatives of glycerides. Conjugated dienes, Anisidine value and viscosity as markers of lipid oxidation and thermal decomposition of the oils; acrylamide which is formed through Maillard reaction and identified as a toxic compound in various fried products. Asparagine content of the raw fresh plantain powder was also determined. Fatty acid composition of palm oleins was stable within a day of intermittent frying. In soybean oils, about 57% and 62.5% of linoleic and linolenic acids were lost but trans fatty acids were not detected. Soybean oils were partly hydrolysed leading to the formation of free fatty acids, monoacylglycerols and diacylglycerols. In both oils, tocopherols and tocotrienols contents decreased significantly by about 50%. Anisidine value (AV) and polymers contents increased slightly in fried palm oleins while conjugated hydroperoxides, AV and polymers greatly increased in soybean oils. Acrylamide was not detected in the chips. This is explained by the absence of asparagine in the raw plantains, the other acrylamide precursors being present. This study shows that the plantain chips prepared at the small-scale level in Yaounde with palm olein are of good quality regarding oxidation and hydrolysis parameters and the absence of acrylamide. In contrast, oxidation developed with soybean oil whose usage for frying should be questioned. Considering that asparagine is the limiting factor for the formation of acrylamide in plantain chips, its content depending on several factors such as production parameters and maturity stage should be explored.