Extracellular polysaccharide production in outdoor mass cultures of Porphyridium sp. in flat plate glass reactors

This work concerns an attempt to develop large scalecultivation of Porphyridium sp. outdoors. Theimpact on cell growth and production of solublesulphated polysaccharides of light-path length (LP)was studied in flat plate glass reactors outdoors. TheLP of the plate reactors ranged from 1.3–30 cm,corresponding to culture volumes of 3–72 L. The sidewalls of all reactors were covered, ensuring similarilluminated surfaces for all reactors. Maximal daytemperature was maintained at 26 ±1 ^°C.Growth conditions of pH (7.5), stirring (withcompressed air) and mineral nutrients, were optimal.Maximal volumetric concentration of the soluble sulfated polysaccharide (1.32 g L^-1) was obtained in winter with the smallest light-pathreactor (1.3 cm ) at a cell density of 1.37 ×10¹¹cells L^-1. Under these conditions, theviscosity of the culture medium was also highest,being inversely proportional to the culture'slight-path. Highest areal concentration of solublepolysaccharides (60 g m^-2) and areal cell density(3.01 × 10¹²m^-2) was recorded in the 20 cmLP reactor, progressively lower values being obtainedas the light path became shorter. A similar patternwas obtained for the areal productivity ofpolysaccharides, the highest being 4.15 g m^-2day^-1 (considering the total illuminated reactorsurface), produced in the 20-cm LP reactor.The main sugar composition (i.e. xylose, galactose andglucose) of the sulfated polysaccharides was similarin all reactors. As viscosity increased with timeduring culture growth, there was a substantial declinein bacterial population. Cultivation throughout mostof the year provided good evidence that a light pathlength of 20 cm in flat plate reactors under theseconditions is optimal for maximal areal solublepolysaccharide production of Porphyridium sp.     

A new tubular reactor for mass production of microalgae outdoors

A novel reactor for outdoor production of microalgae is described. Air-lift is used for circulation of the culture in transparent tubes lying on the ground and interconnected by a manifold. Dissolved O₂ is removed through a gas-separator placed 2.0 m above the tubes and water-spray is used for cooling. The manifold permits short-run durations between leaving the gas separator and re-entering it, preventing thereby damaging accumulation of dissolved oxygen. Day temperature control in summer is attained using water-spray. In winter, temperature in the tubes rises rapidly in the morning, as compared to an open raceway even if placed in a greenhouse. The number of hours along which optimal temperature prevails in the culture throughout the year increased significantly. Very high daily productivity computed on a volumetric basis (e.g. 550 mg dry wt l^–1 culture) was obtained and preliminary observations indicate that a significantly higher output, e.g. 1500 mg dry wt l^–1 d^–1 is attainable. Much more research is required to assess the year-round, sustained productivity attainable in this reactor.     

Growth medium recycling in Nannochloropsis sp. mass cultivation

During cell division Nannochloropsis releases the thick and multilayered parent cell wall [Phycologia 35 (1996) 253]. The excretion of autoinhibitory substances in Nannochloropsis cultures has been also reported [J. Appl. Phycol. 11 (1999) 123]. Both wall remains and autoinhibitors may negatively affect culture growth and limit the recycling of the exhaust culture medium, a necessity in commercial microalgae plants to reduce production costs. The effect of medium recycling on growth and productivity of Nannochloropsis sp. cultures grown in 120 l annular reactors was investigated. The use of exhaust medium replenished with nutrients decreased significantly culture productivity. The partial removal of the cell walls alleviated, but did not solve the problem. In addition, medium recycling caused a massive formation of cell aggregates accompanied by a progressive deterioration of the culture. The structure of these aggregates was investigated by transmission electron microscopy. The images showed that the aggregates were held together by cell wall remains, which entrapped cells, bacteria and debris resulting from cell decay. Thus, in high density Nannochloropsis cultures, cell walls might play a key role in reducing productivity, favoring contamination and making the biomass unsuitable as aquaculture feed.     

Lipid accumulation and growth of Chlorella zofingiensis in flat plate photobioreactors outdoors

Culturing microalgae using natural sunlight is an effective way to reduce the cost of microalgae-based biodiesel production. In order to evaluate the feasibility of culturing Chlorella zofingiensis outdoors for biodiesel production, effects of nitrogen limitation and initial cell concentration on growth and lipid accumulation of this alga were investigated in 60 L flat plate photobioreactors outdoors. The highest μmax and biomass productivity obtained was 0.994 day(-1) and 58.4 mg L(-1)day(-1), respectively. The lipid content was much higher (54.5% of dry weight) under nitrogen limiting condition than under nitrogen sufficient condition (27.3%). With the increasing initial cell concentrations, the lipid contents declined, while lipid concentrations and productivities increased. The highest lipid content, lipid concentration, and lipid productivity obtained was 54.5%, 536 mg L(-1) and 22.3 mg L(-1)day(-1), respectively. This study demonstrated that it was possible to culture C. zofingiensis under outdoor conditions for producing biodiesel feedstock.     

Investigation of continuous-batch mode of two-stage culture of Nannochloropsis sp. for lipid production

Microalgal lipid induction through nitrogen stress often suffers from a contradiction between biomass productivity and lipid content, i.e., either high biomass productivity with low lipid content or vice versa. A two-stage nitrogen-replete and nitrogen-deplete (NR–ND) culture was suggested to be an option to attain high lipid productivity. In this study, the effects of culture conditions and modes on biomass productivity and lipid productivity of Nannochloropsis sp. in the two stages were comprehensively investigated. The optimal culture conditions for the two stages, aiming to high biomass productivity and lipid productivity respectively, were consistent, i.e., CO₂ content in aeration (1 %), phosphorus concentration in medium (181 μmol/L), incident light intensity (150 μE/(m²s)), temperature (25 °C). Different culture modes of the two stages were compared. The overall lipid productivity of the two-stage continuous-batch mode achieved 0.123 g/(L day), which was 60.3, 48.2, 34.9 and 13.5 % higher than that of single nitrogen-replete batch, single nitrogen-limited batch, continuous nitrogen-replete culture and two-stage batch–batch culture, respectively, and also higher than most reported values. This contribution provides fundamental data for the two-stage NR–ND cultivation process design of Nannochloropsis sp.     

Growth characteristics and eicosapentaenoic acid production by Nannochloropsis sp. in mixotrophic conditions

Nannochloropsis sp. was grown under mixotrophic conditions with 30 mM glucose as carbon source, reaching 507 mg dry wt l(-1) after 8 d. This was 1.4-fold of that obtained under photoautotrophic conditions. Under mixotrophic and photoautotrophic cultivations, the net photosynthetic rate of Nannochloropsis sp. did not change but the respiratory rate increased in the mixotrophic cultivation. The yield of eicosapentaenoic acid was 22 mg l(-1) in the mixotrophic cultivation and 20 mg l(-1) under the photoautotrophic cultivation.     

Open systems for the mass production of photoautotrophic microalgae outdoors: physiological principles

The major physiological principles involved in mass production of photoautotrophic microalgae outdoors relate to sustained trapping of solar energy in as high an efficiency as possible throughout the year.The tactics that should be employed for this goal include the improvement of suitable species, as well as developing culturing devices and proper management protocol aimed to facilitate efficient exploitation of the supper saturating photon flux densities existing outdoors.The most common system used today in industry for outdoor production of microalgae is the open raceway, in which stirring is provided by a paddle wheel. This mode of production suffers usually from many weaknesses, since it does not permit a satisfactory response to the two major variables that limit productivity outdoors — i.e.- solar irradiance and ambient temperature. Sustained production of algal mass the year round requires constant monitoring of the state of the culture and adjusting imputs accordingly. The readily controllable variables relate to mineral nutrients and carbon balance as well as to turbulent streaming in the culture and to the population density.The drawbacks of the open system relate in essence to the lack of temperature control and the long light-path which dictates maintenance of disadvantageously low cell concentrations. The open raceway thus falls short of the requirements necessary to insure sustained, year round high productivity outdoors.It is thus proposed that in the future, closed reactors may become the major production mode of microalgae outdoors.This paper was presented at the Symposium on Applied Phycology at the Fourth International Phycological Congress, Duke University.     

Performance of a flat plate,air-lift reactor for the growth of high biomass algal cultures

A flat plate, multi-pass air lift reactor (FPALR) for the culture of photosynthetic organisms was constructed from twin wall acrylic sheet and its performance characterised. When operated at an air input of 2.01 min⁻¹ the multi-pass system had a Reynolds number of 5200 indicating fully turbulent flow. Chlorella vulgaris 211/11c was found to have a stationary phase biomass of 1.48 g 1⁻¹ when grown in the flat plate air lift reactor (FPALR) at 100 μmol m⁻²s⁻¹ compared to 1.11 g 1⁻¹ when cultured in the continually stirred tank reactor (CSTR) at the same PFD (photon flux density). The same organism cultured at 200 μmol m⁻²s⁻¹ achieved a stationary phase biomass of 1.71 g 1⁻¹ in the FPALR. In contrast, Scenedesmus sp. produced a stationary phase biomass of 2.27 g1⁻¹ and 1.27 g1⁻¹, when cultured at 100 μmol m⁻²s⁻¹ in the FPALR and the CSTR respectively. The growth rates of both organisms were also higher in the PFALR.     

Enhanced lipid production in Nannochloropsis sp. using fluorescence‐activated cell sorting

To advance the utilization of microalgae as a viable feedstock for biodiesel production, the intracellular lipid content of three strains of the marine microalgae Nannochloropsis sp. was enhanced using flow cytometry (FC) coupled with cell sorting. Total lipid content was doubled to 55% (biomass dry weight) in the sorted, daughter cells of Nannochloropsis (strain 47) after consecutive three rounds of cell sorting, and this trait was maintained for approximately 100 subsequent cell generations. In addition, daughter cells had a fatty acid profile similar to that of the parent, wild‐type strain. The study demonstrates that FC coupled with cell sorting is a powerful tool for the enhancement of intracellular lipid content in microalgae exploited for biodiesel feedstock.     

Optimization of eicosapentaenoic acid production byPhaeodactylum tricornutumin the flat panel airlift (FPA) reactor

Biomass and eicosapentaenoic acid (EPA) productivities were investigated in a flat panel airlift loop reactor ideally mixed by static mixers. Growth with ammonium, urea and nitrate as nitrogen source were performed at different aeration rates. Cultures grew on ammonium but the decay of pH strongly inhibited biomass increase. On urea biomass productivity reached 2.35 g L^–1d^–1at an aeration rate of 0.66 vvm (24 h light per day, 1000 mol photon m^–2s^–1). Aeration rates between 0.33 vvm and 0.66 vvm and maximal productivities on urea were linearly dependent. Productivity on nitrate never exceeded 1.37 g L^–1d^–1. In the range of maximum productivity photosynthesis efficiency of 10.6% was reached at low irradiance (250 mol photon m^–2s^–1). Photosynthesis efficiency decreased to 4.8% at 1000 mol photon m^–2s^–1. At these high irradiances the flat panel airlift reactor showed a 35% higher volume productivity than the bubble column. At continuous culture conditions the influence of CO₂concentration in the supply air was tested. Highest productivities were reached at 1.25% (v/v) CO₂where the continuous culture yielded 1.04 g L^–1d^–1(16 h light per day, 1000 mol photon m^–2s^–1). The average EPA content amounted to 5.0% of cell dry weight, that resulted in EPA productivities of 52 mg L^–1d^–1(continuous culture, 16 h light per day) or 118 mg L^–1d^–1(batch culture, 24 h light per day).     

Mass cultivation of Nannochloropsis sp. in annular reactors

A study was made on the mass cultivation of Nannochloropsis sp. in newly designed annular reactors operated under natural, artificial or combined illumination. The annular reactor consists of two 2-m-high Plexiglas cylinders of different diameter placed vertically one inside the other so as to form an annular culture chamber. Artificial illumination is supplied by lamps placed inside the inner cylinder. Two annular reactors of different diameter (50 and 91 cm), light path (4.5 and 3.0 cm) and illuminated surface area (5.3 and 9.3 m²) were experimented with. The effect of two different artificial light sources (fluorescent tubes and metal halide lamps) on culture productivity was investigated in both systems. The highest productivity on a per reactor basis (about 34 g (d. wt) reactor^–1 24 h^–1) was achieved with the larger reactor illuminated by a 400-W metal halide lamp. From February to May a 91-cm reactor illuminated only with natural light was operated in parallel with a 91-cm reactor subjected to combined illumination. Under natural illumination productivity increased from 16.6 g (d. wt) reactor^–1 d^–1 in February to 34.1 g (d. wt) reactor^–1 d^–1 in May. Under combined illumination productivity was 41.3 g (d. wt) reactor^–1 d^–1 in February and increased up to 48.3 g (d. wt) reactor^–1 d^–1 in May. Although the culture exposed to combined illumination always attained higher yields, the productivity gap between the two cultures decreased gradually along the season as solar radiation and minimum night temperatures increased. A 1200-L plant made of ten 50-cm annular reactors was set up and operated for two years with combined illumination yielding an average of 270 g of dry Nannochloropsis sp. biomass per day. More than 2000 L of concentrate suspension (50 g (d. wt) L^–1) of Nannochloropsis sp. were produced and successfully used by fish hatcheries as live feed for rotifers and for rearing seabream larvae with the green-water technique. This study indicates that the annular reactor can be profitably used for long-term cultivation of Nannochloropsis in temperate climates. Besides reliability and ease of operation, the main advantage of the system is that it can be used under natural illumination, yet artificial light can be also supplied to maintain high productivity levels in winter or on cloudy days.     

A Modular Flat Panel Photobioreactor (MFPP) for indoor mass cultivation of Nannochloropsis sp. under artificial illumination

Nannochloropsis sp. was grown in a Modular FlatPanel Photobioreactor (MFPP) consisting of sixalveolar panels each with 20.5 L culture volume and3.4 m² illuminated surface area. The panelsformed a closely-packed unit with illuminationprovided by banks of fluorescent tubes placed betweenthe panels. The whole unit was contained in athermoregulated cabinet. Continuous illumination ofone side of the panels with 115 molphoton m^-2 s^-1 attained a mean volumetricproductivity of 0.61 g (d. wt) L^-1 24 h^-1,increasing to 0.97 g (d. wt) L^-1 24 h^-1 whenthe same irradiance was provided on both sides of thepanels. With 230 mol photon m^-2 s^-1 onone side of the panel, a mean productivity of 0.85 g(d. wt) L^-1 24 h^-1 was achieved, whichreached 1.45 g (d. wt) L^-1 24 h^-1 when bothsides were illuminated. Increasing the amount of lightprovided to the culture (either by increasingirradiance or the illuminated surface area) decreasedpigment and enhanced the total fatty acid content, butdid not change significantly the content ofeicosapentaenoic acid. A MFPP of the presentdimensions could produce sufficient microalgae tosupport a hatchery producing 6 million sea breamfingerlings annually.     

Serratia sp. PS-2产几丁质酶发酵条件研究

采用平板透明圈法,从海洋红树林根泥筛选得到一株产几丁质酶较强沙雷氏菌株Serratia sp. PS-2.为实现工业化生产几丁质酶,考察了以几丁质为诱导剂,碳源、氮源、NaCl 浓度、培养温度、时间、培养液酸碱度、通气量和搅拌速度等对产酶的影响,得到了优化的发酵条件.5L发酵罐实验表明,该菌株可在发酵72h内达到产酶高峰,最高酶活力可达到0.68 U/mL.     

Optimization of sulphur production in a biotechnological sulphide-removing reactor

A new biotechnological process for sulphide removal is proposed. The principle of this process is that sulphide is converted into elemental sulphur, which can be removed by sedimentation. In this article, investigations on the optimization of the sulphur production are reported. It seems that less than 10% sulphate is produced at low oxygen concentration, when the sulphide concentration in the reactor exceeds 10 mg/L. At sulphide concentrations higher than 20 mg/L only 5% of the incoming sulphide is converted to sulphate even at high oxygen concentrations. An immobilized biomass on recticulated polyurethane produced more sulphate than a free cell suspension at the same oxygen and sulphide concentration.     

Optical properties of Nannochloropsis sp and their application to remote estimation of cell mass

The absorption and scattering coefficients and reflectance spectra of ultra-high density Nannochloropsis occulata cultures were investigated in detail to identify the optical properties of the cultures and devise algorithms for remote estimation of dry cell mass in ultra-high cell density cultures. High-spectral resolution measurements of apparent absorption and attenuation as well as reflectance from 400 to 900 nm were carried out in relation to the dry weight, cell count, and pigment concentration in outdoor cultures. Indices calculated as (R(NIR) - R(red))/(R(NIR) + R(red)) and R(NIR)/R(red), in which R(NIR) is reflectance in the range from 750 to 800 nm and R(red) is reflectance in the range 670-680 nm, were used for remote assessment of dry cell mass. Remote estimation in the range 1 to 8 g/L was accomplished with an error of less than 0.66 g/L. A different index, i.e., (R(NIR) - R(red)) was employed for estimation of cell-chlorophyll concentration. This is the first report of in vivo specific absorption coefficient of chlorophyll-a and specific scattering coefficient per dry algal weight of Nannochloropsis sp., providing a basis for remote monitoring of dense phytoplankton masses.     

Optimization of a free-fall reactor for the production of fast pyrolysis bio-oil

A central composite design of experiments was performed to optimize a free-fall reactor for the production of bio-oil from red oak biomass. The effects of four experimental variables including heater set-point temperature, biomass particle size, sweep gas flow rate and biomass feed rate were studied. Heater set-point temperature ranged from 450 to 650 °C, average biomass particle size from 200 to 600 μm, sweep gas flow rate from 1 to 5 sL/min and biomass feed rate from 1 to 2 kg/h. Optimal operating conditions yielding over 70 wt.% bio-oil were identified at a heater set-point temperature of 575 °C, while feeding red oak biomass sized less than 300 μm at 2 kg/h into the 0.021 m diameter, 1.8 m tall reactor. Sweep gas flow rate did not have significant effect on bio-oil yield over the range tested.     

响应面法对微拟球藻产微藻蛋白的发酵条件优化

以稳定期微藻蛋白浓度为评价指标,利用响应面设计对微拟球藻(Nannochloropsis gaditana)的分批发酵条件进行优化。在单因素试验的基础上,选取温度、p H、搅拌速度及通气量为影响因子,采用四因素三水平的Box-Benhnken中心组合法设计试验。结果表明:微拟球藻的最佳发酵条件为温度30℃、p H 6.9、搅拌速度340 r/min以及通气量0.65 vvm,在此优化条件下得到微藻蛋白浓度为6.18 g/L,与模型预测值基本相符,较优化前提高了9.18%。     

血栓溶解酶产生菌及其培养条件的研究

通过对根霉１２号发酵液的分析及发酵条件的研究,发现其发酵液中含有能溶解血栓的物质,但不能分解血细胞。它在麸皮胰蛋白胨培养基（ｐＨ５．１）上３０℃振荡培养４８～６０ｈ,ｐＨ值达到７．４左右时产生血栓溶解酶的活力最高。     

裂殖壶菌Schizochytrium sp. 20888产DHA培养条件优化

【目的】为了优化裂殖壶菌产DHA的培养条件,提高油脂中DHA含量。【方法】采用单因素试验和正交设计试验方案,针对分批培养时间、培养基碳、氮源的种类和浓度以及培养温度开展试验,采用重量法测定生物量、采用索氏提取法测定油脂总量,采用气相色谱法测定油脂DHA含量,考察培养条件对细胞油脂DHA含量的影响。【结果】最适培养时间为4 d,培养温度23°C,最优碳氮源组成为(g/L):葡萄糖65、甘油80、蛋白胨6、酵母粉4和谷氨酸钠8。【结论】裂殖壶菌Schizochytrium sp.20888在葡萄糖和甘油组成的复合碳源和由蛋白胨、酵母粉和谷氨酸钠组成的复合氮源的培养基中可以得到最优的DHA产量,细胞DHA含量能达到33.68%。