Study of the removal of chemical oxygen demand of the cheese whey and wastewater from dairy industry using Spirulina platensis

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Buffalo cheese whey proteins, identification of a 24 kda protein and characterization of their hydrolysates: in vitro gastrointestinal digestion

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Wine production from cheese whey /

"Grant no. S-803863."

Comparative study of the biochemical changes and volatile compound formations during the production of novel whey-based kefir beverages and traditional milk kefir

Cheese whey (CW) and deproteinised cheese whey (DCW) were investigated for their suitability as novel substrates for the production of kefir-like beverages. Lactose consumption, ethanol production, as well as organic acids and volatile compounds formation, were determined during CW and DCW fermentation by kefir grains and compared with values obtained during the production of traditional milk kefir. The results showed that kefir grains were able to utilise lactose from CW and DCW and produce similar amounts of ethanol (7.8-8.3 g/l), lactic acid (5.0 g/l) and acetic acid (0.7 g/l) to those obtained during milk fermentation. In addition, the concentration of higher alcohols (2-methyl-1-butanol, 3-methyl-1-butanol, 1-hexanol, 2-methyl-1-propanol, and 1-propanol), ester (ethyl acetate) and aldehyde (acetaldehyde) in cheese whey-based kefir and milk kefir beverages were also produced in similar amounts. Cheese whey and deproteinised cheese whey may therefore serve as substrates for the production of kefir-like beverages similar to milk kefir. (C) 2010 Elsevier Ltd. All rights reserved.

Effects of Feed Time, Organic Loading and Shock Loads in Anaerobic Whey Treatment by an AnSBBR with Circulation

The aim of this work was to investigate the effect of different feeding times (2, 4, and 6 h) and organic loading rates (3, 6 and 12 gCOD l(-1) day(-1)) on the performance of an anaerobic sequencing batch reactor containing immobilized biomass, as well as to verify the minimum amount of alkalinity that can be added to the influent. The reactor, in which mixing was achieved by recirculation of the liquid phase, was maintained at 30 +/- 1A degrees C, possessed 2.5 l reactional volume and treated 1.5 l cheese whey in 8-h cycles. Results showed that the effect of feeding time on reactor performance was more pronounced at higher values of organic loading rates (OLR). During operation at an OLR of 3 gCOD l(-1) day(-1), change in feeding time did not affect efficiency of organic matter removal from the reactor. At an OLR of 6 gCOD l(-1) day(-1), reactor efficiency improved in relation to the lower loading rate and tended to drop at longer feeding times. At an OLR of 12 gCOD l(-1) day(-1) the reactor showed to depend more on feeding time; higher feeding times resulted in a decrease in reactor efficiency. Under all conditions shock loads of 24 gCOD l(-1) day(-1) caused an increase in acids concentration in the effluent. However, despite this increase, the reactor regained stability readily and alkalinity supplied to the influent showed to be sufficient to maintain pH close to neutral during operation. Regardless of applied OLR, operation with feeding time of 2 h was which provided improved stability and rendered the process less susceptible to shock loads.

Acidogenic digestion of effluents of the cheese industry in packed bed biofilm reactors

Dissertation for the Master degree in Biotechnology

Production of yeast extracts from whey for food use: market and technical considerations

Whey is produced in large amounts by cheese industries. This by-product can be used for biomass production by yeast cultivation, resulting in commercially attractive products. The use of yeast extracts as source of flavour enhancer consists of an expansible market, encouraged by costumer's choice for natural additives. The development of a suitable and economically viable project for the generation of valued-added by-products, may allow the dairy industry to diversify their portfolio and increase their rentability.

Correlation between acidic ninhydrin and HPLC methods to evaluate fraudulent addition of whey in milk

The acidic ninhydrin spectrophotometric method (ANSM) for quantitative determination of free and bound sialic acid of milk glycoprotein has been proved to be fast and efficient for routine detection of fraudulent addition of rennet whey to fluid milk. In this research the ANSM was compared with the high performance liquid chromatography (HPLC) method, internationally recommended for caseinomacropeptide (CMP) determination, which besides its high accuracy is more sophisticated and requires trained personnel. For several sample conditions (raw milk and milk with variable added amounts of rennet cheese whey), the methods showed an excellent linear correlation, with r = 0.981 when milk was deproteinized with a 120 g.L-1 final concentration of trichloroacetic acid (TCA) concentration. The best correlations could be seen with final concentrations of 100 g.L-1 and 80 g.L-1 TCA; respectively, r = 0.992 and 0.993.

Fermentative production of ribonucleotides from whey by Kluyveromyces marxianus: effect of temperature and pH

Ribonucleotides have shown many promising applications in food and pharmaceutical industries. The aim of the present study was to produce ribonucleotides (RNA) by Kluyveromyces marxianus ATCC 8,554 utilizing cheese whey, a dairy industry waste, as a main substrate under batch fermentation conditions. The effects of temperature, pH, aeration rate, agitation and initial cellular concentration were studied simultaneously through factorial design for RNA, biomass production and lactose consumption. The maximum RNA production (28.66 mg/g of dry biomass) was observed at temperature 30°C, pH 5.0 and 1 g/l of initial cellular concentration after 2 h of fermentation. Agitation and aeration rate did not influence on RNA concentration (p >0.05). Maximum lactose consumption (98.7%) and biomass production (6.0 g/l) was observed after 12 h of incubation. This study proves that cheese whey can be used as an adequate medium for RNA production by K. marxianus under the optimized conditions at industrial scale.

Effect of specific feed volume on the performance of an anaerobic sequencing batch biofilm reactor (AnSBBR) with circulation treating different wastewaters under different organic loads

The objective of this research was to study the behavior of two anaerobic sequencing batch reactors, containing immobilized biomass (AnSBBR), as a function of the ratio of the volume of treated medium in each cycle to the total volume of reaction medium. The reactors, in which mixing was accomplished by recirculation of the liquid phase, were maintained at 30 +/- 1 degrees C and treated different wastewaters in 8-h cycles. The operational conditions imposed had the objective to investigate whether maintenance of a residual volume in the reactor would affect, at the end of each cycle, process efficiency and stability, as well as to verify the intensity of the effect for different types of wastewaters and organic loading rates. The first reactor, with work volume of 2.5 L, treated reconstituted cheese whey at an organic loading rate of 12 g COD.L(-1).d(-1) and presented similar effluent quality for the four conditions under which it was operated: renewal of 100, 70, 50 and 25 % of its work volume at each cycle. Despite the fact that reduction in the renewed volume did not significantly affect effluent quality, in quantitative terms, this reduction resulted in an increase in the amount of organic matter removed by the first reactor. The second reactor, with work volume of 1.8 L, treated synthetic wastewater at organic loading rates of 3 and 5 g COD.L(-1).d(-1) and operated under two conditions for each loading: renewal of 100 and 50 % of its work volume. At the organic loading rate of 3 g COD.L(-1).d(-1), the results showed that both effluent quality and amount of organic matter removed by the second reactor were independent of the treated volume per cycle. At the organic loading rate of 5 g COD.L(-1).d(-1), although the reduction in the renewed volume did not affect the amount of organic matter removed by the reactor, effluent quality improved during reactor operation with total discharge of its volume. In general, results showed process stability under all conditions, evidencing reactor flexibility and the potential to apply this technology in the treatment of different types of wastewater.

Diagnóstico ambiental de uma queijaria e proposta de melhorias

O presente trabalho tem como objectivo o diagnóstico ambiental da empresa Lacticinios do Paiva, S.A, a avaliação da água do processo e da ETARI e o estudo da fermentação do soro de queijo com o intuito de produção de bioetanol. No diagnóstico ambiental da empresa, observou-se que 18.227.731 litros de leite usados anualmente geram 5.031 ton/ano de queijo, 7.204 ton/ano de soro de queijo, 74.201 m3/ano de efluente liquido, 14 ton/ano de plástico e 20 ton/ano de cartão. Os principais problemas com necessidade de optimização são a recuperação de água das lavagens, avaliação da produção de biogás no digestor anaeróbio, recuperação do volume de leite que é desperdiçado na produção de queijo fresco de longa duração, avaliação da eficiência energética da empresa, valorização das natas e do soro de queijo. Decidiu-se neste trabalho avaliar a possibilidade de reciclagem das águas de lavagem, avaliar o funcionamento da ETARI face à legislação existente e estudar a possibilidade de valorização do soro de queijo. Na avaliação das águas de processo das lavagens para posterior reciclagem, verifica-se que relativamente ao pH e aos sólidos suspensos não existe problema, podendo encarar-se a hipótese de reciclagem directa. No entanto, no que respeita à carga orgânica das águas de lavagem do sistema de ultrafiltração do queijo fresco de longa duração, constata-se que esta não poderia ser utilizada novamente, uma vez que apresenta valores elevados de CQO. Para a sua reutilização, será necessário remover a CQO, hipótese que se estudou com resultados positivos. Verificou-se que, um tratamento por adsorção em carvão activado precedido de microfiltração, reduz a CQO de forma significativa permitindo admitir a hipótese de reciclagem da água, nomeadamente para as 1ª e 3ª águas de lavagem. As outras águas teriam necessidade de mais tempo de contacto com o carvão activado. No sentido de avaliar o funcionamento da ETARI, foram analisadas várias correntes da mesma, em particular a do efluente final, no que respeita a parâmetros como: pH, Sólidos Suspensos Totais, Carência Química de Oxigénio, Carência Bioquímica de Oxigénio, Turvação, Nitratos, Fósforo Total, Azoto Kjeldalh, Azoto Amoniacal e Cloretos. Observou-se que os valores para o efluente final da ETARI são os seguintes: pH compreendido entre [7,21 – 8,69], SST entre [65,3 – 3110] mg/L, CQO entre [92,5 – 711,5] mg/L, CBO5 entre [58 – 161] mg/L, NO3- entre [10,8 – 106,7] mg/L, fósforo total entre [8,3 – 64,3] mg/L, turvação entre [67,7 – 733,3] FTU e cloretos entre [459,9 – 619,81] mg/L; pode-se dizer que os parâmetros analisados se encontram quase sempre dentro da gama de valores impostos pela Câmara Municipal de Lamego pelo que o efluente pode ser lançado no Colector Municipal de Cambres. Relativamente à fermentação alcoólica do soro de queijo, verifica-se que a levedura Kluyveromyces Marxianus consegue degradar praticamente todo o açúcar presente no permeado produzindo assim uma quantidade razoável de etanol. Quando se utilizou a levedura Saccharomyces Cerevisiae, a produção de etanol foi muito reduzida, como esperado, dado que esta levedura apresenta dificuldades na metabolização da lactose. Constatou-se assim que a melhor levedura para a fermentação do permeado do soro de queijo é a Kluyveromyces Marxianus, estimando-se em 150 mg a produção de etanol por L de soro.

Food waste valorization through the production of polyhydroxyalkanoates by mixed microbial cultures

Dissertação para obtenção do Grau de Mestre em Engenharia Química e Bioquímica

Investigation of the regulation mechanisms for bioplastics production from industrial residues

Dissertação para obtenção do Grau de Mestre em Biotecnologia

Production of chitin-glucan complex by Pichia pastoris

Dissertation for the Degree of Master in Biotechnology

Effects of residues on the degradation of PHA produced from mixed microbial cultures and processed in extrusion

Thermal degradation upon melting is one of the major drawbacks reported for polyhydroxyalkanoates (PHA). However, the role of residues originating from the fermentation and the extraction steps on the thermal stability of this class of biopolymers still needs to be clarified. In the particular case of PHA produced from mixed microbial cultures (MMC), this topic is even less documented in the literature. Here, two polyhydroxy(butyrate-co-valerate) (PHBV) produced from MMC enriched in PHA accumulating organisms and fed with cheese whey were studied. A micro extrusion line is used to produce filaments and assess the processability and the degradation of processed PHBV. The prototype micro extrusion line allows for studying grams of materials. The two PHBV contain 18 mol% HV. PHBV was recovered with 11 wt% residues, and further submitted to a purification procedure resulting in a second biopolyester containing less than 2 wt% impurities. The thermorheological characterization of the two PHBV is first presented, together with their semicrystalline properties. Then the processing windows of the two biopolyesters are presented. Finally, the properties of extruded filaments are reported and the thermomechanical degradation of PHBV is extensively studied. The structure was assessed by wide angle X-ray diffraction, mechanical and rheological properties are reported, thermal properties are studied with differential scanning calorimetry and thermogravimetric analysis, whereas Fourier Transform Infrared spectroscopy was used to assess the impact of the extrusion on PHBV chemical structure. All results obtained with the two PHBV are compared to assess the effects of residues on both PHBV processability and degradation.