Modeling of photosynthesis and respiration rate for microalgae-bacteria consortia.

In this article, the influence of culture conditions (irradiance, temperature, pH, and dissolved oxygen) on the photosynthesis and the respiration rates of microalgae-bacteria consortia in wastewater treatment was analyzed. Specifically, some short photo-respirometric experiments, simulating outdoor raceway reactors, were performed to evaluate the response of microalgae, heterotrophic bacteria, and nitrifying bacteria to variations in environmental parameters. Results demonstrate that irradiance is the most dominant variable to determine microalgae photosynthesis rates. However, reduction in microalgae activity was not observed at higher irradiance, ruling out the existence of photoinhibition phenomena. Related to heterotrophic and nitrifying bacteria, their activities were strongly affected by the influence of temperature and pH. Moreover, the effect of dissolved oxygen concentrations on microalgae, and bacteria activities was studied, displaying a reduced photosynthetic rate at dissolved oxygen concentrations above 20 mg/L. Data have been used to develop an integrated model for each population (microalgae, heterotrophic bacteria, and nitrifying bacteria) based on considering the simultaneous influence of irradiance, temperature, pH, and dissolved oxygen. The models fit the experimental results in the range of culture conditions tested, and they were validated using data obtained by the simultaneous modifications of the variables. These individual models serve as a basis for developing a global biologic microalgae-bacteria model for wastewater treatment to improve the optimal design and management of microalgae-based processes, especially outdoors, where the cultures are subject to variable daily culture conditions.

The oxygen evolution methodology affects photosynthetic rate measurements of microalgae in well-defined light regimes.

Designing photobioreactors correctly is a must for the success of microalgal mass production. Optimal photobioreactor design requires a precise knowledge of photosynthesis dynamics in fluctuating light conditions and hence a method for the measurement of photosynthetic rates in specific light regimes. However, it is not uncommon in literature that experimental protocols used to obtain oxygen generation rates are described ambiguously and the reported rates of photosynthesis vary widely depending on the methodology. Additionally, quite a number of methods overlook certain aspects that can affect the estimated rates significantly, and can therefore affect photobioreactor design. We have developed a method based on oxygen evolution measurements that accurately determines photosynthetic rates under well-defined light regimes. Our experimental protocol takes into account most of the issues that can affect the rates of oxygen generation, such as depletion of nutrients during the measurements and precision of the measurements. We have focused on the basic applications in photobioreactor design and used a dynamic model of photosynthesis to analyze our results and compare them with available published data. The results suggest that our oxygen evolution method is consistent.

Biotechnological production of lutein and its applications.

Lutein is an antioxidant that has gathered increasing attention due to its potential role in preventing or ameliorating age-related macular degeneration. Currently, it is produced from marigold oleoresin, but continuous reports of lutein-producing microalgae pose the question if those microorganisms can become an alternative source. Several microalgae have higher lutein contents than most marigold cultivars and have been shown to yield productivities hundreds of times higher than marigold crops on a per square meter basis. Microalgae and marigold are opposite alternatives in the use of resources such as land and labor and the prevalence of one or the other could change in the future as the lutein demand rises and if labor or land becomes more restricted or expensive in the producing countries. The potential of microalgae as a lutein source is analyzed and compared to marigold. It is suggested that, in the current state of the art, microalgae could compete with marigold even without counting on any of the improvements in microalgal technology that can be expected in the near future.

Effect of pretreatments on biogas production from microalgae biomass grown in pig manure treatment plants.

Methane production from pretreated and raw mixed microalgae biomass grown in pig manure was evaluated. Acid and basic pretreatments provided the highest volatile solids solubilisation (up to 81%) followed by alkaline-peroxide and ultrasounds (23%). Bead milling and steam explosion remarkably increased the methane production rate, although the highest yield (377 mL CH4/g SV) was achieved by alkali pretreatment. Nevertheless, some pretreatments inhibited biogas production and resulted in lag phases of 7-9 days. Hence, experiments using only the pretreated solid phase were performed, which resulted in a decrease in the lag phase to 2-3 days for the alkali pretreatment and slightly increased biomass biodegradability of few samples. The limiting step during the BMP test (hydrolysis or microbial inhibition) for each pretreatment was elucidated using the goodness of fitting to a first order or a Gompertz model. Finally, the use of digestate as biofertilizer was evaluated applying a biorefinery concept.

Improvement of stability and carotenoids fraction of virgin olive oils by addition of microalgae Scenedesmus almeriensis extracts.

Humans are not capable of synthesizing carotenoids de novo and thus, their presence in human tissues is entirely of dietary origin. Consumption of essential carotenoids is reduced due to the lower intake of fruits and vegetables. Microalgae are a good source of carotenoids that can be exploited. In the present work, carotenoids rich extracts from Scenedesmus almeriensis were added to extra-virgin olive oils at different concentrations (0.1 and 0.21 mg/mL) in order to enhance the consumption of these bioactives. Extracts brought changes in olive oils color, turning them orange-reddish. Quality of olive oils was improved, since peroxidation was inhibited. Olive oils fatty acids and tocopherols were not affected. ß-carotene and lutein contents increase considerably, as well as oxidative stability, improving olive oils shelf-life and nutritional value. Inclusion of S. almeriensis extracts is a good strategy to improve and enhance the consumption of carotenoids, since olive oil consumption is increasing.

Assessment of the production of 13C labeled compounds from phototrophic microalgae at laboratory scale.

An integrated process for the indoor production of 13C labeled polyunsaturated fatty acids (PUFAs) from Phaeodactylum tricornutum is presented. The core of the process is a bubble column photobioreactor operating with recirculation of the exhaust gas using a low-pressure compressor. Oxygen accumulation in the system is avoided by bubbling the exhaust gas from the reactor in a sodium sulfite solution before returning to it. To achieve a high 13C enrichment in the biomass obtained, the culture medium is initially stripped of carbon, and labeled 13CO(2) is automatically injected on-demand during operation for pH control and carbon supply. The reactor was operated in both batch and semicontinuous modes. In semicontinuous mode, the reactor was operated at a dilution rate of 0.01 h(-1), resulting in a biomass productivity of 0.1 g l(-1) per day. The elemental analysis of the inlet and outlet flows of the reactor showed that 64.9% of carbon was turned into microalgal biomass, 34.9% remained in the supernatant mainly as inorganic compounds. Only 3.8% of injected carbon was effectively fixed as the target labeled product (EPA). Regarding the isotopic composition of fatty acids, results showed that fatty acids were not labeled in the same proportion, the higher the number of carbons the lower the percentage of 13C. Isotopic composition of EPA ranged from 36.5 to 53.5%, as a function of the methodology used (GC-MS, EA-IRMS or gas chromatography-combustion-isotope ratio mass spectrometry (GC-IRMS)). The low carbon uptake efficiency combined with the high cost of 13CO(2) make necessary to redefine the designed culture system to increase the efficiency of the conversion of 13CO(2) into the target product. Therefore, the possibility of removing 12C from the fresh medium, and recovering and recirculating the inorganic carbon in the supernatant and the organic carbon from the EPA depleted biomass was studied. The inorganic carbon of the fresh medium was removed by acidification and stripping with N(2). The inorganic carbon of the supernatant was recovered also by acidification and subsequent stripping with N(2). The operating conditions of this step were optimized for gas flow rate and type of contactor. A carbon recovery step for the depleted biomass was designed based on the catalytic oxidation to CO(2) using CuO (10 wt.%) as catalyst with an oxygen enriched atmosphere (80% O(2) partial pressure). In this way, the carbon losses reduced an 80.2% and the efficiency of the conversion of carbon in EPA was increased to 19.5%, which is close to the theoretical maximum. Further increase in 13CO(2) use efficiency is only possible by additionally recovering other labeled by-products present in the biomass: proteins, carbohydrates, lipids, and pigments.

Obtaining lutein-rich extract from microalgal biomass at preparative scale.

Lutein extracts are in increasing demand due to their alleged role in the prevention of degenerative disorders such as age-related macular degeneration (AMD). Lutein extracts are currently obtained from plant sources, but microalgae have been demonstrated to be a competitive source likely to become an alternative. The extraction of lutein from microalgae posesses specific problems that arise from the different structure and composition of the source biomass. Here is presented a method for the recovery of lutein-rich carotenoid extracts from microalgal biomass in the kilogram scale.

Development of a process for large-scale purification of C-phycocyanin from Synechocystis aquatilis using expanded bed adsorption chromatography.

In this paper a large and scaleable method for purification of C-phycocyanin (C-PC) from the cyanobacteria Synechocystis aquatilis has been developed. Phycobiliproteins are extracted from the cells by osmotic shock and separated by passing the centrifuged cell suspension through an expanded bed adsorption chromatography (EBAC) column using Streamline-DEAE as adsorbent. The eluted C-PC rich solution is finally purified by packed-bed chromatography using DEAE-cellulose. Optimal extraction is achieved using phosphate 0.05 M buffer pH 7.0 twice. The operation of EBAC is optimized on a small scale using a column of 15 mm internal diameter (I.D.). The optimal conditions are a sample load of 4.9 mg C-PC/mL adsorbent, an expanded bed volume twice the settled bed volume and a sample viscosity of 1.020 mP. The EBAC process is then scaled up by increasing the column I.D. (15, 25, 40, 60 and 90 mm) and the success of the scale-up process is verified by determining the protein breakthrough capacity and product recovery. The yield of the EBAC step is in the range of 90-93% for every column diameter. To obtain pure C-PC, conventional ion-exchange chromatography with DEAE-cellulose is utilized and a yield of 74% is obtained. The overall yield of the process, comprising all steps, is 69%. The purification steps are monitored using SDS-PAGE and the purity of recovered C-PC is confirmed by absorption and emission spectroscopy and RP-HPLC. Results show that EBAC method is a scalable technology that allows large quantities of C-PC to be obtained without product loss, maintaining a high protein recovery while reducing both processing cost and time.

Stability of carotenoids in Scenedesmus almeriensis biomass and extracts under various storage conditions.

Scenedesmus almeriensis biomass is a source of carotenoids, particularly lutein, and is considered to be promising as an alternative source to marigold. One key question concerning alternative sources of lutein is the loss of carotenoids that takes place between harvesting and processing, which in the case of marigold is frequently up to 50%. The work described here involved a study into the stability of the main carotenoids (lutein, violaxanthin, and beta-carotene), as well as other components, under different storage conditions. The experiments were carried out with biomass in three forms: frozen, freeze-dried, and spray-dried. The stability of extracts of Scenedesmus biomass in acetone and olive oil was also studied. The results show that the most important factor in retaining carotenoids is a low temperature. At -18 degrees C the loss of carotenoids was negligible after the storage period, regardless of the biomass form used (frozen, freeze-dried, or spray-dried). On the other hand, the carotenoid content and fatty acid profile was increasingly affected with increasing temperature. However, the protein content is unaffected by storage conditions.

Recovery of lutein from microalgae biomass: development of a process for Scenedesmus almeriensis biomass.

In this work an optimized method for the extraction of lutein from microalgae biomass is presented. It has been developed using dry biomass of the lutein-rich microalga Scenedesmus almeriensis. The method comprises three steps, cell disruption, alkaline treatment, and solvent extraction, and renders a carotenoid extract rich in lutein. The results demonstrate that cell disruption is necessary and that the best option among the treatments tested with regard to industrial applications is the use of a bead mill with alumina in a 1:1 w/w proportion as disintegrating agent for 5 min. With regard to the alkaline treatment, the optimal conditions were obtained using 4% w/v KOH with a biomass concentration of 100 g/L for 5 min. Longer alkaline treatments or the use of higher KOH concentrations reduced the yield of the process. Finally, extraction with hexane is optimized. Using a 1:1 ratio hexane to sample volume, a total of eight extraction steps are necessary to recover 99% of lutein contained in the processed biomass. However, the optimal number of extraction steps is six, 95% of the lutein being recovered. In summary, the developed method allows the efficient recovery of lutein from microalgae biomass, it being a scaleable and industrially applicable method.