182 resultados para Tetraselmis suecica
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The primary requirements for high-biomass-concentration microalgal cultivation include a photon source and distribution, efficient gas exchange and suitable growth medium composition. However, for mass outdoor production of microalgae, growth medium composition is a major controlling factor as most of the other factors such as light source and distribution are virtually uncontrollable. This work utilises an elemental balance approach between growth medium and biomass compositions to obtain high-density microalgal cultures in an open system. F medium, commonly used for the cultivation of marine microalgae such as Tetraselmis suecica was redesigned on the basis of increasing the biomass capacity of its major deficient components to support high biomass concentrations (τ ∼ 5.0 % for N, S and τ ∼ 10 % P), and the entire formulation was dissolved in 0.2 um sterile filtered natural seawater. Results show that the new medium (F') displayed a maximum biomass concentration and total lipid concentration of 1.29 g L 1 and 108.7 mg L 1 respectively, which represents over 2-fold increase compared to that of the F medium. Keeping all variables constant except growth medium, and using F medium as the base case of 1 medium cost (MC) unit mg -1 lipid, the F' medium yielded lipid at a cost of only 0.35 MC unit mg -1 lipids. These results show that greater amounts of biomass and lipids can be obtained more economically with minimal extra effort simply by using an optimised growth medium.
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Carotenoids prevent different degenerative diseases and improve human health. Microalgae are commercially exploited for carotenoids, including astaxanthin and β-carotene. Two commercially important microalgae, Dunaliella salina and Tetraselmis suecica, were treated with plant hormones salicylic acid (SA) and methyl jasmonate (MJ), or by UV-C radiation (T. suecica only) and a combination thereof. Significant increases in total carotenoids were found for D. salina and T. suecica after treatment with MJ (10 μmol/L) and SA (70–250 μmol/L), respectively. T. suecica also had significant increases in total carotenoids following UV-C radiation compared to control cultures. Among the carotenoids, lutein was the highest induced carotenoid. A combination of these two treatments also showed a significant increase in total carotenoids and lutein for T. suecica, when compared to controls. Plant hormones and UV-C radiation may be useful tools for increasing carotenoid accumulation in green microalgae although the responses are species- and dose-specific and should be trialed in medium to large scale to explore commercial production.
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The experimental cultures of the marine microalgae Isochrysis galbana Green (variety T. Iso) and Tetraselmis suecica (Kylin) Butch for feeding mussel larvae are described in detail.
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As fossil fuel prices increase and environmental concerns gain prominence, the development of alternative fuels from biomass has become more important. Biodiesel produced from microalgae is becoming an attractive alternative to share the role of petroleum. Currently it appears that the production of microalgal biodiesel is not economically viable in current environment because it costs more than conventional fuels. Therefore, a new concept is introduced in this article as an option to reduce the total production cost of microalgal biodiesel. The integration of biodiesel production system with methane production via anaerobic digestion is proved in improving the economics and sustainability of overall biodiesel stages. Anaerobic digestion of microalgae produces methane and further be converted to generate electricity. The generated electricity can surrogate the consumption of energy that require in microalgal cultivation, dewatering, extraction and transesterification process. From theoretical calculations, the electricity generated from methane is able to power all of the biodiesel production stages and will substantially reduce the cost of biodiesel production (33% reduction). The carbon emissions of biodiesel production systems are also reduced by approximately 75% when utilizing biogas electricity compared to when the electricity is otherwise purchased from the Victorian grid. The overall findings from this study indicate that the approach of digesting microalgal waste to produce biogas will make the production of biodiesel from algae more viable by reducing the overall cost of production per unit of biodiesel and hence enable biodiesel to be more competitive with existing fuels.
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Background: Conventional biodiesel production relies on trans-esterification of lipids extracted from vegetable crops. However, the use of valuable vegetable food stocks as raw material for biodiesel production makes it an unfeasibly expensive process. Used cooking oil is a finite resource and requires extra downstream processing, which affects the amount of biodiesel that can be produced and the economics of the process. Lipids extracted from microalgae are considered an alternative raw material for biodiesel production. This is primarily due to the fast growth rate of these species in a simple aquaculture environment. However, the dilute nature of microalgae culture puts a huge economic burden on the dewatering process especially on an industrial scale. This current study explores the performance and economic viability of chemical flocculation and tangential flow filtration (TFF) for the dewatering of Tetraselmis suecicamicroalgae culture. Results: Results show that TFF concentrates the microalgae feedstock up to 148 times by consuming 2.06 kWh m-3 of energy while flocculation consumes 14.81 kWhm-3 to concentrate the microalgae up to 357 times. Economic evaluation demonstrates that even though TFF has higher initial capital investment than polymer flocculation, the payback period for TFF at the upper extreme ofmicroalgae revenue is ∼1.5 years while that of flocculation is ∼3 years. Conclusion: These results illustrate that improved dewatering levels can be achieved more economically by employing TFF. The performances of these two techniques are also compared with other dewatering techniques.
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A novel technique was developed for the flocculation of marine microalgae commonly used in aquaculture. The process entailed an adjustment of pH of culture to between 10 and 10.6 using NaOH, followed by addition of a non-ionic polymer Magnafloc LT-25 to a final concentration of 0.5 mg L-1. The ensuing flocculate was harvested, and neutralised giving a final concentration factor of between 200- and 800-fold. This process was successfully applied to harvest cells of Chaetoceros calcitrans, C. muelleri, Thalassiosira pseudonana, Attheya septentrionalis, Nitzschia closterium, Skeletonema sp., Tetraselmis suecica and Rhodomonas salina, with efficiencies >=80%. The process was rapid, simple and inexpensive, and relatively cost neutral with increasing volume (cf. concentration by centrifugation). Harvested material was readily disaggregated to single cell suspensions by dilution in seawater and mild agitation. Microscopic examination of the cells showed them to be indistinguishable from corresponding non-flocculated cells. Chlorophyll analysis of concentrates prepared from cultures of Concentrates of T. pseudonana prepared using pH-induced flocculation gave better growth of juvenile Pacific oysters (Crassostrea gigas) than concentrates prepared by ferric flocculation, or centrifuged concentrates using a cream separator or laboratory centrifuge. In follow up experiments, concentrates prepared from 1000 L Chaetoceros muelleri cultures were effective as supplementary diets to improve the growth of juvenile C. gigas and the scallop Pecten fumatus reared under commercial conditions, though not as effective as the corresponding live algae. The experiments demonstrated a proof-of-concept for a commercial application of concentrates prepared by flocculation, especially for use at a remote nursery without on-site mass-algal culture facilities.
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Carotenoids are associated with various health benefits, such as prevention of age-related macular degeneration, cataract, certain cancers, rheumatoid arthritis, muscular dystrophy and cardiovascular problems. As microalgae contain considerable amounts of carotenoids, there is a need to find species with high carotenoid content. Out of hundreds of Australian isolates, twelve microalgal species were screened for carotenoid profiles, carotenoid productivity, and in vitro antioxidant capacity (total phenolic content (TPC) and ORAC). The top four carotenoid producers at 4.68-6.88 mg/g dry weight (DW) were Dunaliella salina, Tetraselmis suecica, Isochrysis galbana, and Pavlova salina. TPC was low, with D. salina possessing the highest TPC (1.54 mg Gallic Acid Equivalents/g DW) and ORAC (577 μmol Trolox Equivalents/g DW). Results indicate that T. suecica, D. salina, P. salina and I. galbana could be further developed for commercial carotenoid production.
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El objetivo de este trabajo es contribuir al conocimiento de las necesidades nutricionales en ácidos grasos poliinsaturados del pez marino dentón (Dentex dentex, L.). Para ello se realizaron cuatro experimentos en los cuales se suministraron a larvas de dentón dietas con diferentes contenidos de ácidos grasos poliinsaturados (PUFA) utilizando como vehículo de introducción presas vivas (rotífero y Artemia). Posteriormente se evaluó el efecto de dichas dietas sobre la calidad y supervivencia final de las larvas. En el Experimento I, se alimentaron larvas de corta edad hasta los 22 días posteclosión (dph) con el rotífero (Brachionus plicatilis). Dichos rotíferos fueron sometidos a una serie de tratamientos de enriquecimiento con varias especies de microalgas (Chlorella sp., Nannochloropsis gaditana, Tetraselmis suecica e Isochrysis galbana) y un enriquecedor comercial (Protein - Selco®), con diferentes contenidos en PUFA. En el tratamiento con Protein – Selco se alcanzaron valores significativamente superiores (ρ < 0.05) de talla y peso de las larvas, mientras que en el tratamiento con la microalga Isochrysis galbana, las larvas alcanzaron mayores valores de biomasa y supervivencia final con respecto a las larvas de los otros tratamientos. En los Experimentos II y III se partió de larvas de mayor edad (desde 22 hasta 48 dph) que fueron alimentadas con el crustáceo Artemia sp. La Artemia, se enriqueció con una serie de emulsiones experimentales (ICES®) con diferentes contenidos de PUFA. En el Experimento II, se encontró que las larvas a las que se les suministró mayores contenidos de PUFA, presentaron valores significativamente superiores (ρ < 0.05) en supervivencia y biomasa final. En el Experimento III, se observó que en las larvas a las que se les suministró el menor nivel de PUFA, se obtuvieron resultados significativamente menores (ρ < 0.05) en peso, talla, biomasa y supervivencia final. No se encontraron grandes diferencias en peso y talla entre las larvas a las que se les suministraron los PUFA en forma de triglicéridos o de etilésteres. En el Experimento IV se estudió la variación de contenidos de ácidos grasos a lo largo de un periodo de puestas (abril, mayo y junio) y durante cuatro fases de desarrollo endotrófico: huevo, huevo embrionado, larvas recién eclosionadas y larvas con apertura de la boca. Se evaluó la repercusión de estas variaciones de contenidos de ácidos grasos sobre los parámetros de calidad de huevos y larvas. También se compararon los contenidos de ácidos grasos de estas fases endotróficas con los contenidos encontrados durante las fases de alimentación con rotífero y Artemia. No se observaron grandes diferencias a lo largo del periodo de puesta en cuanto a contenidos de ácidos grasos y a las proporciones entre ellos, aunque si se observaron cambios en los parámetros que indicaban calidad de las puestas. Por el contrario, se observaron diferencias significativas (ρ < 0.05) en el grado de saturación de ácidos grasos, contenido de PUFA y ácidos grasos de 18 carbonos entre las larvas en fase de apertura de la boca con respecto a las otras fases de desarrollo endotrófico.
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Há uma crescente procura por alimentos mais saudáveis e seguros para atender uma população cada vez maior e mais exigente. Nos últimos anos o interesse por surfactantes de origem microbiana tem aumentado significativamente em decorrência de serem naturalmente biodegradáveis diminuindo assim o impacto ambiental. Uma grande variedade de microorganismos produz biossurfactantes, sendo que o tipo, a quantidade e a qualidade do biossurfactante são influenciados pelos constituintes do meio, tais como, fontes de carbono, nitrogênio e sais inorgânicos, além das condições de cultivo, como pH, temperatura, agitação e disponibilidade de oxigênio. Os biossurfactantes são metabólitos microbianos de superfície ativa que apresentam uma vasta aplicação no setor industrial. Os objetivos deste trabalho foram selecionar microalgas com potencial para produzir biossurfactantes e estudar a produção por microalgas em diferentes fotobiorreatores e condições nutricionais. O trabalho foi dividido em quatro etapas: 1) cultivo autotrófico e mixotrófico de microalgas para produção de biossurfactantes; 2) Seleção de microalgas para produção de biossurfactantes; 3) Produção de biossurfactantes por microalgas em diferentes fotobiorreatores e 4) Cultivo outdoor da microalga marinha Tetraselmis suecica OR para produção de biossurfactantes. Na primeira etapa Spirulina sp. LEB-18, Synechococcus nidulans LEB-25, Chlorella vulgaris LEB-106, Chlorella minutissima LEB-108 e Chlorella homosphaera foram cultivadas com glicose (cultivo mixotrófico). Spirulina sp. LEB-18 apresentou concentrações máximas de biomassa (2,55 g.L-1 ) quando foi utilizada 5 g.L-1 de glicose no meio de cultivo. A tensão superficial dos meios das microalgas foi reduzida de 70 para 43 mN.m-1 para as microalgas estudadas utilizando glicose como fonte de carbono. Resultados da segunda etapa mostraram que a microalga Scenedesmus sp. 3PAV3 apresentou valor de atividade emulsificante óleo em água (AE o/a) superior (339,8 UE.g-1 ) ao encontrado para as demais microalgas. Os menores valores de tensões superficiais variaram de 27,4 a 31,2 mN.m-1 . Na terceira etapa verificou-se que a microalga Chlorella sp. PROD1 apresentou valor de AE o/a semelhante (258,2 UE g -1 ) ao encontrado para o emulsificante comercial lecitina de soja (257,0 UE g -1 ) e ambas as microalgas estudadas alcançaram valores de tensões superficiais abaixo de 30 mN.m -1 . Na última etapa, Tetraselmis suecica OR cultivada em fotobiorreator do tipo Green Wall Panel apresentou menores valores de tensões superficiais para cultura com limitação de nitrogênio. Os resultados demonstraram a potencialidade das microalgas estudadas na produção de biossurfactantes, tanto pela redução da tensão superficial e interfacial, como pelo aumento da atividade emulsificante, confirmando uma possível aplicação como emulsificante, detergente, lubrificante, estabilizante, entre outras.
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Sediment samples were taken from Lake Langans in Sweden and fossilised diatoms analysed. Sample methods and environmental factors are discussed. Species with a characteristic occurrence are described. The article discusses diatom-thanatocoenoses as indicators of environment.
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A transient transformation system for the unicellular marine green alga, Platymonas subcordiformis, was established in this study. We introduced the pEGFP-N1 vector into P. subcordiformis with a glass bead method. P. subcordiformis was incubated in cell wall lytic enzymes (abalone acetone powder and cellulase solutions) to degrade the cell wall. The applicable conditions for production of viable protoplasts were pH 6.5, 25 degrees C, and 3 h of enzyme treatment. The protoplast yield was 61.2% when P. subcordiformis cells were added to the enzyme solution at a concentration of 10(7) cell ml(-1). The protoplasts were immediately transformed with the pEGFP-N1 vector using glass-bead method. The transformation frequency was about 10(-5), and there was no GFP activity observed in either the negative or the blank controls. This study indicated that GFP was a sensitively transgenic reporter for P. subcordiformis, and the method of cell wall enzymolysis followed by glass bead agitation was applicable for the transformation of P. subcordiformis.
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This paper describes the development and application of an RP HPLC method using a C(18) monolithic stationary phase for the separation and quantification of extra- and intracellular amino acids in a batch cultivation of the marine alga Tetraselmis gracilis. Fluorimetric detection was made after separation of the o-phthaldialdehyde 2-mercaptoethanol (OPA-2MCE) derivatives using a binary gradient elution. Separation of 19 amino acids was achieved with resolution >1.5 in about 39 min at a flow rate of 1.5 mL/min. RSD of analyses in seawater medium ranged from 0.36% for Orn (0.50 mu mol/L) to 12% for Ile (0.10 mu mol/L). The main constituents of the intracellular dissolved free amino acids (DFAAs) in the exponential growth phase were arginine (Arg), asparagine (Asn), alanine (Ala), aspartic acid (Asp), glutamic acid (Glu), serine (Ser), glycine (Gly), glutamine (Gln), and leucine (Leu). The major amino acids excreted to the media were valine (Val), Ala, Ser, and Gly. The monolithic phase facilitates the analysis by shortening the separation time and saving solvents and instrumentation costs (indeed conventional HPLC instrumentation can be used, running at lower pressures than those ones used with packed particle columns).
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The concept of sequential injection chromatography (SIC) was exploited to automate the fluorimetric determination of amino acids after pre-column derivatization with ophthaldialdehyde (OPA) in presence of 2-mercaptoethanol (2MCE) using a reverse phase monolithic C(18) stationary phase. The method is low-priced and based on five steps of isocratic elutions. The first step employs the mixture methanol: tetrahydrofuran: 10 mmol L(-1) phosphate buffer (pH 7.2) at the volumetric ratio of 8:1:91; the other steps use methanol: 10 mmol L-1 phosphate buffer (pH 7.2) at volumetric ratios of 20:80, 35:65, SO:SO and 65:35. At a flow rate of 10 mu L s(-1) a 25 mm long-column was able to separate aspartic acid (Asp), glutamic acid (Glu), asparagine (Asn), serine (Ser), glutamine (Gln), glycine (Gly), threonine (Thr), citruline (Ctr), arginine (Arg), alanine (Ala), tyrosine (Tyr), phenylalanine (Phe), ornithine (Orn) and lysine (Lys) with resolution >1.2 as well as methionine (Met) and valine (Val) with resolution of 0.6. Under these conditions isoleucine (Ile) and leucine (Leu) co-eluted. The entire cycle of amino acids derivatization, chromatographic separation and column conditioning at the end of separation lasted 25 min. At a flow rate of 40 mu L s(-1) such time was reduced to 10 min at the cost of resolution worsening for the pairs Ctr/Arg and Orn/Lys. The detection limits varied from 0.092 mu mol L(-1) for Tyr to 0.51 mu mol L(-1) for Orn. The method was successfully applied to the determination of intracellular free amino acids in the green alga Tetraselmis gracilis during a period of seven days of cultivation. Samples spiked with known amounts of amino acids resulted in recoveries between 94 and 112%. (C) 2008 Elsevier B.V. All rights reserved.
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)