Environmentally Friendly Production of D(−) Lactic Acid by Sporolactobacillus nakayamae

The interest in the production of lactic acid has increased due to its wide range of applications. In the present study, the variables that affect fermentative D(−) lactic acid production were investigated: neutralizing agents, pH, temperature, inoculum percentage, agitation, and concentration of the medium components. An experimental design was applied to determine the optimal concentrations of the medium components and fermentation was studied using different feeding strategies. High production (122.41 g/L) and productivity (3.65 g/L·h) were efficiently achieved by Sporolactobacillus nakayamae in 54 h using a multipulse fed-batch technique with an initial medium containing 35 g/L of yeast extract (byproduct of alcohol production), 60 g/L of crystallized sugar, and 7.5 mL/L of salts. The fermentation process was conducted at 35°C and pH 6.0 controlled by NaOH with a 20% volume of inoculum and agitation at 125 rpm. The production of a high optically pure concentration of D(−) lactic acid combined with an environmentally friendly NaOH-based process demonstrates that S. nakayamae is a promising strain for D(−) lactic acid production

Biochars from Spirulina as an alternative material in the purification of lactic acid from a fermentation broth

In this study, Spirulina biochar obtained from fast pyrolysis was evaluated as an alternative to commercial activated carbon for lactic acid (LA) purification from a fermentation broth. Thermally (350 and 400 C treatment of the biochar in N2 atmosphere for 4 h) and chemically (KOH solution impregnation of the algal material and fast pyrolysis to obtain the biochar) activated Spirulina biochars were also tested. The biochars were previously characterized using SEM and FT-IR. Two purification methodologies were evaluated: filtration and stirring. The stirring method prove to be simpler, faster and chipper, with excellent purification results. All the evaluated biochars presented a performance comparable to that of activated carbon in the stirring methodology. Spirulina biochar and the KOH activated biochar were the once with the best results, with 92 and 82% LA recovery and 82 and 90% protein removal efficiencies, respectively.Fil: Piloni, Roxana Verónica. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Córdoba. Instituto de Investigaciones en Físico-química de Córdoba. Universidad Nacional de Córdoba. Facultad de Ciencias Químicas. Instituto de Investigaciones en Físico-química de Córdoba; ArgentinaFil: Coelho, Luciana Fontes. Universidade Estadual Paulista Julio de Mesquita Filho; BrasilFil: Sass, Daiane Cristina. Universidade Estadual Paulista Julio de Mesquita Filho; BrasilFil: Lanteri, Mario Nicolas. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Córdoba. Centro de Investigaciones y Transferencia de Villa María. Universidad Nacional de Villa María. Centro de Investigaciones y Transferencia de Villa María; ArgentinaFil: Bertochi, Maria Aparecida Zaghete. Universidade Estadual Paulista Julio de Mesquita Filho; BrasilFil: Moyano, Elizabeth Laura. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Córdoba. Instituto de Investigaciones en Físico-química de Córdoba. Universidad Nacional de Córdoba. Facultad de Ciencias Químicas. Instituto de Investigaciones en Físico-química de Córdoba; ArgentinaFil: Contiero, Jonas. Universidade Estadual Paulista Julio de Mesquita Filho; Brasi

Desempenho das etapas de tratamento de água, da estação de tratamento de água Poxim

A água para consumo humano deve atender aos padrões de potabilidade estabelecidos pela Portaria 2914 e Portaria de Consolidação nº 5 do Ministério da Saúde, assim cabe às Estações de Tratamento de Água (ETA) garantir que a mesma chegue ao destino final livre de contaminações. Para isso, a estação de tratamento convencional é composta por mistura rápida, floculação, decantação, filtração e saída da água clorada. Neste trabalho buscou-se avaliar o desempenho das etapas de tratamento na ETA Poxim, localizada em Sergipe, de forma a caracterizar a eficiência da qualidade da água quanto aos parâmetros cor aparente, turbidez e pH, com o intuito de verificar possíveis desvios de etapa no tratamento, de modo a proporcionar menor intervalo de tempo e consequentemente chegar na distribuição o mais rápido possível. Como resposta, verificou-se que, de modo geral, na unidade de mistura rápida e floculação, não ocorreu remoção de cor aparente e turbidez. A decantação e a filtração são as unidades do tratamento de água em que melhor ocorre a remoção desses parâmetros com eficiência significativa. Algumas amostras de água da saída do filtro não atenderam aos limites de parâmetros recomendados pela Portaria do Ministério da Saúde e os piores resultados coincidiram com o período chuvoso. Diante do exposto, não se sugere período viável em fase de tratamento da água que possa passar por desvios de etapa no tratamento de água.  http://dx.doi.org/10.18226/23185279.v7iss3p

Isolamento e seleção de micro-organismos e desenvolvimento de tecnologia para produção de ácido lático

O objetivo deste trabalho foi isolar micro-organismos produtores de D-(-) e L-(+) ácido lático, os quais são utilizados na síntese de polímeros empregados na produção de diversos materiais resistentes e biodegradáveis, além de otimizar a produção de ácido lático, a partir da utilização de diversos resíduos agro-industriais. Os micro-organismos mais promissores para produção de L-(+) ácido lático foram os isolados de Keffir (Ke6, Ke11, Ke8 e Ke24) e o Lactobacillus rhamnosus B103, já para a produção de D-(-) ácido lático, os mais promissores foram os isolados de iogurte (Y15C e Y15A) e o Leuconostoc mesenteroides B512. Pode-se afirmar que os micro-organismos selecionados apresentaram grande potencial para utilização na indústria de biopolímeros e indústria de alimentos. O soro de queijo e a manipueira foram os melhores resíduos para produção de L-(+) ácido lático por Lactobacillus rhamnosus B103. Quando se utilizou 160 g/L de lactose de soro de queijo, 60 mL/L de água de maceração de milho (AMM), 2 mL/L de Tween 80 e 0,10 g/L de MnSO4, observou-se alta produção de L- (+) ácido lático (142 g/L) e baixo residual de lactose (3,2 g/L). Para a otimização com manipueira, foi obtido 41,58 g/L de L-(+) ácido lático, a partir de 50 g/L de açúcar redutor total (ART), 65,40 mL/L de AMM e 1,27 mL/L de Tween 80. Nas otimizações com Leuconostoc mesenteroides B512 foi observado produção de 60,20 g/L de D-(-) ácido lático, utilizando 116,90 g/L de ART de caldo de cana e 44,25 g/L de autolisado de levedura. Nas otimizações com L. plantarum Lmism6 observou-se uma produção de 63,40 g/L de ácido lático, 0,40 g/L de ART residual e alta conversão de substrato (99,40%), quando se utilizou 70 g/L de ART de melaço, 30,00 mL/L de AMM, 2 g/L de K2HPO4 e 1 mL/L de Tween 80The aim of this study was to isolate D-(-) and L-(+) lactic acid producers micro-organisms, which are used in the synthesis of polymers used in the production of many resistant and biodegradable materials and optimize the lactic acid production, from agro-industrial residues. The most promising micro-organisms for L-(+) lactic acid production were Lactobacillus rhamnosus B103, as well as, the isolated from Keffir (Ke6, Ke11, Ke8 Ke24) and the most promising D-(-) lactic acid producers were strains of yogurt (Y15C and Y15A) and Leuconostoc mesenteroides B512. Cheese whey and cassava wastewater (CW) were the best residues for L-(+) lactic acid production by Lactobacillus rhamnosus B103. Using 160 g/L of lactose from whey, 60 mL/L of CSL, 2 mL/L of Tween 80 and 0.10 g/L of MnSO4, there was higher production of L-(+) lactic acid (142 g/L) and low lactose residual (3.20 g/L). For optimizations with CW, it was obtained 41.58 g/L of L-(+) lactic acid from 50 g/L of reducing sugar, 65.40 mL/L and 1.27 mL of corn steep liquor (CSL) and Tween 80 respectively. Leuconostoc mesenteroides B512 produced 60.20 g/L of D-(-) lactic acid, using 116.90 g/L of sugarcane juice and 44.25 g/L of yeast autolysate. L. plantarum Lmism6 produced 63.40 g/L of lactic acid, with less residual reducing sugar (0.41 g/L) and higher substrate conversion (99.41%), by using 70 g/L of sugar reducing from molasses, 30 mL/L of CSL, 2 g/L of K2HPO4, and 1 mL/L of Tween 80Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP

Efficient Conversion of Agroindustrial Waste into D(-) Lactic Acid by Lactobacillus delbrueckii Using Fed-Batch Fermentation

Purpose. The goal of this paper is to describe the green conversion of agricultural waste products, such as molasses and corn steep liquor, into large amounts of D(-) lactic acid using a facilitated multipulse fed-batch strategy and affordable pH neutralizer. This is a very low-cost process because there is no need for hydrolysis of the waste products. The fed-batch strategy increases lactic acid productivity by avoiding inhibition caused by a high initial substrate concentration, and the selected controlling agent prevents cell stress that could be caused by high osmotic pressure of the culture media. Methods. The effects of different carbon and nitrogen sources on lactic acid production were investigated, and the best concentrations of the medium components were determined. To optimize the culture conditions of the Lactobacillus delbrueckii strain, the effects of pH control, temperature, neutralizing agent, agitation, and inoculum size in batch cultures were investigated. Fed-batch strategies were also studied to improve production and productivity. Result. A high titer of D(-) lactic acid (162g/liter) was achieved after 48 hours of fermentation. Productivity at this point was 3.37 g/L·h. The optimum conditions were a temperature of 39°C, pH 5.5 controlled by the addition of Ca(OH)2, agitation at 150 rpm, and inoculum size of 25% (v/v). Conclusion. The production of high optical purity D(-) lactic acid through L. delbrueckii fermentation with molasses and corn steep liquor is a promising economical alternative process that can be performed on the industrial scale

L-(+)-Lactic acid production by Lactobacillus rhamnosus B103 from dairy industry waste

ABSTRACT Lactic acid, which can be obtained through fermentation, is an interesting compound because it can be utilized in different fields, such as in the food, pharmaceutical and chemical industries as a bio-based molecule for bio-refinery. In addition, lactic acid has recently gained more interest due to the possibility of manufacturing poly(lactic acid), a green polymer that can replace petroleum-derived plastics and be applied in medicine for the regeneration of tissues and in sutures, repairs and implants. One of the great advantages of fermentation is the possibility of using agribusiness wastes to obtain optically pure lactic acid. The conventional batch process of fermentation has some disadvantages such as inhibition by the substrate or the final product. To avoid these problems, this study was focused on improving the production of lactic acid through different feeding strategies using whey, a residue of agribusiness. The downstream process is a significant bottleneck because cost-effective methods of producing high-purity lactic acid are lacking. Thus, the investigation of different methods for the purification of lactic acid was one of the aims of this work. The pH-stat strategy showed the maximum production of lactic acid of 143.7 g/L. Following purification of the lactic acid sample, recovery of reducing sugars and protein and color removal were 0.28%, 100% and 100%, respectively

Response surface optimization of D(-)-lactic acid production by Lactobacillus SMI8 using corn steep liquor and yeast autolysate as an alternative nitrogen source

The production of D(-) lactic acid from Lactobacillus LMI8 sp. was studied, using 2 low-cost nitrogen sources: corn steep liquor (CSL) and yeast autolysate (YA). A central composite design was used to determine maximal lactic acid production. The surface response method was used to evaluate the results of the experiments. The assays were performed in 250 mL Erlenmeyer flasks containing 100 mL of production medium maintained under refrigerated incubation at 200 rpm and a temperature of 37 +/- 1 degrees C for 48 h of fermentation. Lactic acid production was significantly affected by the isolated CSL as well as the interaction between CSL and YA. Maximal production of D(+) lactic acid was 41.42 g/L - a value located at the central point, which corresponded to 15 g/L of CSL and 5 g/L of YA.Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP