Isabel Belo

Biological treatment of olive mill wastewater by non-conventional yeasts

The ability of lipolytic yeasts to grow on olive mill wastewater (OMW)-based medium and to produce high-value compounds while degrading this waste, was tested. OMW collected from three-phase olive mills from the North region of Portugal were characterized and used. OMW with COD ranging from 100 g L(-1) to 200 g L(-1) were supplemented with yeast extract and ammonium chloride. Studies of OMW consumption were carried out in batch cultures of Candida rugosa, Candida cylindracea and Yarrowia lipolytica. All strains were able to grow in the OMW-based media, without dilution, to consume reducing sugars and to reduce COD. C. cylindracea was the best strain concerning the lipase production and the reduction of phenolic compounds and COD. For all strains, the phenols degradation was quite difficult, mostly when more easily degradable carbon source is still present in the medium. Among the phenolic compounds tested catechol is the most inhibitory to the cells.

Biochemistry of lactone formation in yeast and fungi and its utilisation for the production of flavour and fragrance compounds

The consumers’ demand for natural flavour and fragrances rises. To be natural, compounds have to result from the extraction of natural materials and/or to be transformed by natural means such as the use of enzymes or whole cells. Fungi are able to transform some fatty acids into lactones that can thus be natural. Although some parts of this subject have been reviewed several times, the present article proposes to review the different pathways utilised, the metabolic engineering strategies and some current concerns on the reactor application of the transformation including scaling up data. The main enzymatic steps are hydroxylation and β-oxidation in the traditional way, and lactone desaturation or Baeyer–Villiger oxidation. Although the pathway to produce γ-decalactone is rather well known, metabolic engineering strategies may result in significant improvements in the productivity. For the production of other lactones, a key step is the hydroxylation of fatty acids. Beside the biotransformation, increasing the production of the various lactones requires from biotechnologists to solve two main problems which are the toxicity of lactones toward the producing cell and the aeration of the emulsified reactor as the biochemical pathway is very sensitive to the level of available oxygen. The strategies employed to resolve these problems will be presented.

Yarrowia lipolytica lipase production enhanced by increased air pressure

Aims:  To study the cellular growth and morphology of Yarrowia lipolytica W29 and its lipase and protease production under increased air pressures.

Growth and beta-galactosidase activity in cultures of Kluyveromyces marxianus under increased air pressure

Aims:  To investigate the effect of total air pressure raise on cell growth and intracellular β‐galactosidase activity in batch cultures of Kluyveromyces marxianus CBS 7894.

Adaptation of dinitrosalicylic acid method to microtiter plates

A microtiter plate adaptation of the well-known dinitrosalicylic acid (DNS) colorimetric method, for measurement of reducing sugars, is described. This method allows a substantial volume reduction of the reagents and a rapid analysis of a large number of samples, having an economic cost benefit and a positive impact on the environment. Therefore, it is well suited as an high-throughput technique for reducing sugars determination.

Fed‐Batch Cultivation of Saccharomyces cerevisiae in a Hyperbaric Bioreactor

Fed‐batch is the dominating mode of operation in high‐cell‐density cultures of Saccharomyces cerevisaein processes such as the production of bakerapos;s yeast and recombinant proteins, where the high oxygen demand of these cultures makes its supply an important and difficult task. The aim of this work was to study the use of hyperbaric air for oxygen mass transfer improvement on S. cerevisiaefed‐batch cultivation. The effects of increased air pressure up to 1.5 MPa on cell behavior were investigated. The effects of oxygen and carbon dioxide were dissociated from the effects of total pressure by the use of pure oxygen and gas mixtures enriched with CO2. Fed‐batch experiments were performed in a stirred tank reactor with a 600 mL stainless steel vessel. An exponential feeding profile at dilution rates up to 0.1 h−1 was used in order to ensure a subcritical flux of substrate and, consequently, to prevent ethanol formation due to glucose excess. The ethanol production observed at atmospheric pressure was reduced by the bioreactor pressurization up to 1.0 MPa. The maximum biomass yield, 0.5 g g−1 (cell mass produced per mass of glucose consumed) was attained whenever pressure was increased gradually through time. This demonstrates the adaptive behavior of the cells to the hyperbaric conditions. This work proved that hyperbaric air up to 1.0 MPa (0.2 MPa of oxygen partial pressure) could be applied to S. cerevisiaecultivation under low glucose flux. Above that critical oxygen partial pressure value, i.e., for oxygen pressures of 0.32 and 0.5 MPa, a drastic cell growth inhibition and viability loss were observed. The increase of carbon dioxide partial pressure in the gas mixture up to 48 kPa slightly decreased the overall cell mass yield but had negligible effects on cell viability.

Batch and fed-batch cultures of E. coli TB1 at different oxygen transfer rates Effect of stirring and oxygen partial pressures on cell growth and cytochrome b5 production

Abstract Batch cultures of E. coli TB1/pUC13 were carried out at different oxygen transfer rates (OTR) enhanced by the increase of stirring rate and by the increase of air total pressure of the bioreactor. These two variables showed to have little effect on cell growth but a negative effect on cytochrome b5 (recombinant protein) production. However, this effect was more significant of high stirring rates than for values of pressure up to 0.4 MPa.The effects of stirring and pressure were also investigated for fed-batch mode operation. In this type of cell cultivation high cell densities are reached, thus a high capacity of oxygen supply of the system is required. To compare the two ways of improving OTR, cell behaviour was followed in two bioreactors at different operational conditions giving the same maximum OTR value. The first one operated at a high stirring rate (500 rpm) and at atmospheric pressure (0.1 MPa) and the other one at high air pressure (0.48 MPa) and low stirring rate. The increased pressure seemed to be a better way of ensuring an adequate oxygen supply to a culture of E. coli TB1 cells than an increased stirring rate. For the high pressure experiment a higher cellular density was reached, as well as a higher cyt.b5 expression which led to a 4-fold increase in final productivity.These experiments showed that bioreactor pressurization can be successfully used as a means of enhancing oxygen mass transfer to shear sensitive cell cultures.

The use of methyl ricinoleate in lactone production by Yarrowia lipolytica: Aspects of bioprocess operation that influence the overall performance

Abstract Yarrowia lipolytica was used to produce γ-decalactone by the degradation of methyl ricinoleate (MR). A new method for inoculating the biotransformation medium was tested, which avoided the laborious step of washing cells from the growth medium. The consequent cell hydrophobicity increase led to an enhancement of aroma production. In a study of MR concentration in shake flasks, the highest productivity (15 mg L−1 h−1) was achieved using 30 g MR L−1. Lipase and protease activities were induced but no correlation between lipase induction and aroma production was found. The effects of different aeration and agitation rates were studied in bioreactor assays. Productivity was improved to 87 mg L−1 h−1, and another compound, 3-hydroxy-γ-decalactone, was detected in large amounts. Dehydration of this lactone produced two decenolides with aroma characteristics. The direct influence of oxygen on the production of both lactones was demonstrated.

Ultrasounds pretreatment of olive pomace to improve xylanase and cellulase production by solid-state fermentation.

Olive mills generate a large amount of waste that can be revaluated. This work aim to improve the production lignocellulolytic enzymes by solid-state fermentation using ultrasounds pretreated olive mill wastes. The composition of olive mill wastes (crude and exhausted olive pomace) was compared and several physicochemical characteristics were significantly different. The use of both wastes in SSF was evaluated and a screening of fungi for xylanase and cellulase production was carried out. After screening, the use of exhausted olive pomace and Aspergillus niger led to the highest enzyme activities, so that they were used in the study of ultrasounds pre-treatment. The results showed that the sonication led to a 3-fold increase of xylanase activity and a decrease of cellulase activity. Moreover, the liquid fraction obtained from ultrasounds treatment was used to adjust the moisture of solid and a positive effect on xylanase (3.6-fold increase) and cellulase (1.2-fold increase) production was obtained.

Physiological behaviour of Saccharomyces cerevisiae under increased air and oxygen pressures

Saccharomyces cerevisiae, in a pressure batch reactor, coped with higher air (1.2-3 bar) pressures better than with pure oxygen pressures (1.2-3 bar) for an equivalent dissolved oxygen concentration. However, pure oxygen pressure enhanced ethanol production. Both pressures did not influence the type of metabolism followed by the organism which was always oxidoreductive. Growth was inhibited with the increase of air and pure oxygen pressure and almost completely inhibited with 8 bar of pure oxygen. Above 3 bar activities of mitochondrial superoxide dismutase and glutathione reductase increased with air pressure, but cytosolic superoxide dismutase and catalase increased activity only in pure oxygen pressure.