Photosynthetic performance of a helical tubular photobioreactor incorporating the cyanobacterium spirulina platensis

The photosynthetic performance of a helical tubular photobioreactor ("Biocoil"), incorporating the filamentous cyanobacterium Spirulina platensis, was investigated. The photobioreactor was constructed in a cylindrical shape (0.9 m high) with a 0.25-m(2)basal area and a photostage comprising 60 m of transparent PVC tubing of 1.6-cm inner diameter (volume = 12.1 L). The inner surface of the cylinder (area = 1.32 m(2)) was illuminated with cool white fluorescent lamps; the energy input of photosynthetically active radiation(PAR, 400 to 700 nm) into the photobioreactor was 2920 kJ per day. An air-lift system ncorporating 4%CO(2) was used to circulate the growth medium in the tubing. The maximum productivity achieved in batch culture was 7.18 g dry biomass per day [0.51 g . d biomass/L . day, or 5.44 g . d biomass/m(2)(inner surface of cylindrical shape)/day] which corresponded to a photosynthetic (PAR) efficiency of 5.45%. The CO(2) was efficiently removed from the gaseous stream; monitoring the CO(2) the outlet and inlet gas streams showed a 70% removal of CO(2) from the inlet gas over an 8-h period with almost maximum growth rate. (c) 1995 John Wiley & Sons, Inc.     

Intracellular phosphorus pool of the cyanobacteriumSpirulina platensis

An intracellular phosphorus pool in a monoculture of the cyanobacteriumSpirulina platensis was assessed using radioactive and nonradioactive phosphorus. The derived dependence of specific growth rate on the intracellular content of mineral phosphorus can be presented in the form of the Droop equation. It was found that the stage of replenishment of the intracellular phosphorus pool may affect the phosphorus turnover estimation in aquatic environments from the results of short-term measurements of phosphorus uptake     

Spectroscopic study of phycocyanobilin from the cyanobacteriumSpirulina platensis

Spectroscopic characterization of phycobiliprotein (PBP) isolated fromSpirulina platensis indicated that it had a molecular formula of C₃₃H₄₀N₄O₆ with molecular ion peak at m/e 586. The PBP was rich in aliphatic and acidic amino acid residues. The specific ultra-violet absorbance, infrared transmittance, specific absorbance coefficient, nuclear magnetic resonance and mass spectral analysis revealed thatS. platensis PBP was composed mainly of C-phycocyanin and allophycocyanin.     

Culture of an autoflocculent microalga in a vertical tubular photobioreactor for phycoerythrin production

Summary A red microalgal, Rhodosorus marinus, was used to produce phycoerythrin. This autoflocculent species, grown in a vertical tubular photoreactor equipped with a gaz-lift system, achieved a growth rate of 0.029 h^-1 with a maximum biomass yield of 2 g.l^-1 dry weight. These values were close to those obtained in batch cultures of other red microalgae cultured as free cell suspensions. Results have shown that these algae could be grown efficiently in natural seawater enriched with nutrients and harvested by decantation followed by filtration.     

Ketocarotenoid production by a mutant of Chlorococcum sp. in an outdoor tubular photobioreactor

A mutant, MA-1, of Chlorococcum sp., grown in batch culture, produced about 54 mg ketocarotenoids/l with 10 mM nitrogen. The accumulation rate of these ketocarotenoids was independent of the nitrogen concentration under sunlight illumination. Fed-batch cultures showed poor growth and the average productivity of ketocarotenoids dropped from 2.6 mg/l day to 1.6 mg/l day in the two consecutive fed-batch runs.     

Neochloris oleoabundans oil production in an outdoor tubular photobioreactor at pilot scale

Journal of Applied Phycology - Oil production was tested with Neochloris oleoabundans in a 6 m3, horizontal soft sleeve tubular reactor from 22 October to 7 November in Matalascañas,...     

Action of selected heavy metal ions on the photosystem 2 activity of the cyanobacteriumSpirulina platensis

Addition of different concentrations of heavy metal ions (Hg²⁺, Cu²⁺, Ni²⁺ and Pb²⁺) inhibited the photosystem 2 catalyzed electron transport activity (H₂O→p-benzo-quinone) of the cyanobacteriumSpirulina platensis. Hg²⁺ caused the inhibition in electron transport activity in very low concentrations compared to the other metal ions. Hg²⁺ at this low concentration specifically altered the spectral properties of phycocyanin of the phycobilisomes in the intact cells ofSpirulina, whereas other heavy metal ions were ineffective in this sense.     

Continuous marennin production by agar-entrapped Haslea ostrearia using a tubular photobioreactor with internal illumination

The marine diatom Haslea ostrearia was immobilized in a tubular agar gel layer introduced into a photobioreactor of original design with internal illumination for the continuous synthesis of marennin, a blue-green pigment of biotechnological interest. Marennin was produced for a long-term period (27–43 days) and the volumetric productivity was maximum (18.7 mg day⁻¹ l⁻¹ gel) at the highest dilution rate (0.25 day⁻¹) and lowest agar layer thickness (3 mm). Heterogeneous cell distribution in the agar layer revealed diffusional limitation of light and nutrients. However, the 3 mm gel thickness led to a more homogeneous cell distribution during incubation and to an increase of the whole biomass in the agar gel layer. Received: 22 October 1999 / Received revision: 14 February 2000 / Accepted: 18 February 2000     

Hydrodynamics and mass transfer in a tubular airlift photobioreactor

In photobioreactors, which are usually operated under light limitation,sufficient dissolved inorganic carbon must be provided to avoid carbonlimitation. Efficient mass transfer of CO₂ into the culture mediumisdesirable since undissolved CO₂ is lost by outgassing. Mass transferof O₂ out of the system is also an important consideration, due tothe need to remove photosynthetically-derived O₂ before it reachesinhibitory concentrations. Hydrodynamics (mixing characteristics) are afunctionof reactor geometry and operating conditions (e.g. gas and liquid flow rates),and are a principal determinant of the light regime experienced by the culture.This in turn affects photosynthetic efficiency, productivity, and cellcomposition. This paper describes the mass transfer and hydrodynamics within anear-horizontal tubular photobioreactor. The volume, shape and velocity ofbubbles, gas hold-up, liquid velocity, slip velocity, axial dispersion,Reynoldsnumber, mixing time, and mass transfer coefficients were determined intapwater,seawater, and algal culture medium. Gas hold-up values resembled those ofvertical bubble columns, and the hydraulic regime could be characterized asplug-flow with medium dispersion. The maximum oxygen mass transfer coefficientis approximately 7 h^–1. A regime analysisindicated that there are mass transfer limitations in this type ofphotobioreactor. A methodology is described to determine the mass transfercoefficients for O₂ stripping and CO₂ dissolution whichwould be required to achieve a desired biomass productivity. This procedure canassist in determining design modifications to achieve the desired mass transfercoefficient.     

Photosynthetic characterization of a mutant of Spirulina platensis

A mutant of Spirulina(Arthrospira) platensis, strain I22,obtained by mutagenesis with ethylmethanesulfonate, was partially defective inthe production of -linolenic acid. However, when compared with the wildform, the I22 mutant almost lost its capacity to grow at low temperatures,although at optimal temperature growth was unaffected. Measurement of themutant's photosynthetic characteristics, including O₂-evolution,Pmaxand light saturation values, revealed significantly lower values than for thewild type, in contrast to the higher content of photosynthetic pigments,chlorophyll and phycocyanin. Whereas the total activity of photosynthesis oftheI22 mutant was 58% lower than that of the wild type, the PS II activity of theI22 mutant was 23% higher. On the other hand, the I22 mutant was 69% lower inPSI activity, and the growth rate of this mutant was limited at high lightintensity. These results indicated that the defect in the PS I complex of theI22 mutant may reduce its ability to utilize light to generate the energy usedin diverse biochemical processes, including fatty acid desaturation.     

光生物反应器中螺旋藻培养条件的优化

利用正交实验对搅拌式光生物反应器中钝顶螺旋藻(Spirulina platensis Geitl)的培养条件即搅拌速度、通气量和光照强度进行优化.实验结果表明:当培养温度为30℃时,通过正交实验所获得的最佳培养条件为搅拌转速120 r·min-1,通气量80 L·h-1,光照强度5000lx.在最佳培养条件下,收获时螺旋藻的干重为1.922 g·L-1.根据回归模型得到相应的优化条件为:光照强度5000lx,通气量150L·h-1,搅拌转速111.70r·min-1,收获量(干重)的预测值为2.293 g·L-1.另外,10%的接种量有利于螺旋藻的生长.     

Productivity of Spirulina in a strongly curved outdoor tubular photobioreactor

 The effect of different flow rates (from 0.18 m∣s to 0.97 m∣s) on the productivity of Spirulina grown outdoors in a strongly curved tubular photobioreactor (CTP) was studied. The results were compared to those obtained with a conventional photobioreactor made with straight tubes to form a loop (STP). The cultures were operated at a biomass concentration of 10 g/l dry weight. The productivity of the culture increased by about 39% and 29% in the CTP and STP respectively when the flow rate of the culture was increased from 0.18 m/s to 0.75 m/s. A further increase of the flow rate did not result in any increase of the productivity in either of the photobioreactors. The better performance of the culture observed in the CTP was attributed to an intermittent illumination pattern resulting from a secondary flow motion generated in the bends. The power required for the induction of the same flow rate inside the two types of photobioreactor changed significantly. At a Reynolds number of 4000, the power absorbed by the CTP was 25% higher than that required for water recycling in the STP and rose by more than 40% at a Reynolds number of 20000. Received: 3 July 1995 / Received revision: 16 October 1995 / Accepted: 24 October 1995     

Photosynthetic performance of a cyanobacterium in a vertical flat-plate photobioreactor for outdoor microalgal production and fixation of CO2

A vertical flat-plate photobioreactor was developed for the outdoor culture of microalgae using sunlight as the light source. The ability for biomass production and CO₂ fixation was evaluated by using a cyanobacterium, Synechocystis aquatilis SI-2. The average areal productivity was 31 g biomass m^–2 d^–1, which corresponded to a CO₂ fixation rate of 51 g CO₂ m^–2 d^–1, sustainable in the northern region of Japan during the winter time (January and February). The relationships between the efficiency of solar energy utilization of the reactor and its effect factors (cell concentration and irradiation) were investigated.     

Role of light and photosynthesis on the acclimation process of the cyanobacteriumSpirulina platensis to salinity stress

The response ofSpirulina platensis cells to salinity stress was studied. Once adapted to the higher osmoticum, photosynthetic parameters such as the maximum rate of photosynthesis under saturating irradiance (P_max) and the initial slope of the P-I curve () are reduced by 15% and 25% in 0.5 M NaCl grown cells, respectively. Salt-adapted cells have a modified biochemical composition; reduced protein and chlorophyll content, and an increased level of carbohydrates. The reduction in the photosynthetic capacity of the salt-adaptedSpirulina cells reflects a lower ability to utilize light energy and results in an increase in the susceptibility of the stressed cells to photoinhibition. This conclusion is supported by the finding that cultures exposed to salt stress show not only a decrease in growth rate (), but lose the ability to respond to increased irradiance with an increase in growth. The use of variable fluorescence as a fast and reliable measurement to follow the changes in PSII of salt-stressesSpirulina cells enables following the early events of salinity shock. It indicates that as soon as the cells are exposed to salt, a protection mechanism is induced. This mechanism does not require any protein synthesis and may take place even in the dark, though at somewhat reduced effectiveness. The significance of the result in providing a better understanding of the interaction between two environmental stresses — light and salinity — and their application in the outdoor mass cultivation ofSpirulina are discussed.Author for correspondence     

Scale-up and design of a pilot-plant photobioreactor for the continuous culture of Spirulina platensis

Scale-up of bioreactors has the intrinsic difficulty of establishing a reliable relationship among physical parameters involved in the design of the new bioreactor and the physiology of the cultured cells. This is more critical in those cases where a more complex operation of the bioreactor is needed, such as in photobioreactors. A key issue in the operation of photobioreactors is establishing a quantification for the interaction between external illumination, internal light distribution and cell growth. In this paper an approach to the scale-up of a photobioreactor for the culture of Spirulina platensis, based on a mathematical model describing this interaction, and the operation of a previous reactor 10 times smaller is presented. The paper describes the approach followed in the scale-up, the analysis of different design constraints, the physical realization of the new bioreactor design, innovative use of plastic material walls to improve reactor safety, and finally the corroboration of its satisfactory operation.     

A new approach to ammonium sulphate feeding for fed‐batch Arthrospira (Spirulina) platensis cultivation in tubular photobioreactor

Arthrospira platensis was cultivated in tubular photobioreactor using different photosynthetic photon flux densities (PPFD) and protocols of (NH₄)₂SO₄ fed‐batch supply. Results were evaluated by variance analysis selecting maximum cell concentration (X_m), cell productivity (P_x), nitrogen‐to‐cell conversion factor (Y_X/N) and biomass, protein and lipid contents as responses. At PPFD of 120 and 240 μmol‐photons/m² s, a parabolic profile of (NH₄)₂SO₄ addition aiming at producing biomass with 7% nitrogen content ensured X_m values (14.1 and 12.2 g/L, respectively) comparable to those obtained with NaNO₃. At PPFD of 240 μmol‐photons/m² s, P_x (1.69 g/Ld) was 36% higher, although the photosynthetic efficiency (3.0%) was less than one‐half that at PPFD of 120 μmol‐photons/m² s. Biomass was shown to be constituted by about 35% proteins and 10% lipids, without any dependence on PPFD or kind of nitrogen source. These results highlight the possible use of (NH₄)₂SO₄ as alternative, cheap nitrogen source for A. platensis cultivation in tubular photobioreactors. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Impact of ammonia concentration on Spirulina platensis growth in an airlift photobioreactor

Spirulina platensis was cultivated in a bench-scale airlift photobioreactor using synthetic wastewater (total nitrogen 412 mg L(-1), total phosphorous 90 mg L(-1), pH 9-10) with varying ammonia/total nitrogen ratios (50-100% ammonia with balance nitrate) and hydraulic residence times (15-25 d). High average biomass density (3500-3800 mg L(-1)) and productivity (5.1 g m(-2) d(-1)) were achieved when ammonia was maintained at 50% of the total nitrogen. Both high ammonia concentrations and mutual self-shading, which resulted from the high biomass density in the airlift reactor, were found to partially inhibit the growth of S. platensis. The performance of the airlift bioreactor used in this study compared favorably with other published studies. The system has good potential for treatment of high strength wastewater combined with production of algae for biofuels or other products, such as human and animal food, food supplements or pharmaceuticals.     

Improving mass transfer in an inclined tubular photobioreactor

The mass transfer and hydrodynamics of two outdoor tubular photobioreactor designs were compared, a Tredici-design near-horizontal tubular photobioreactor (NHTR) and an enhanced version of this reactor (ENHTR), for the purpose of improving algal growth via improved hydrodynamics. The enhancements included addition of vertical bubble columns at the sparger end and a larger degasser with a diffuser. Gas-liquid mass transfer and other performance measures were assessed for a range of gas sparging rates. The ENHTR modifications proved to be very successful, increasing oxygen stripping and carbon dioxide dissolution by 120–220 % and 0–50 %, respectively. There was an increase in axial mixing and a fourfold decrease in total mixing time. Experiments were conducted to determine that approximately 50 % of the mass transfer occurred in the vertical bubble columns, while 85–90 % of the mass transfer in the near-horizontal tubes occurred in the lower half of the tubes. These improvements can lead to increased algae productivity depending upon culture-specific parameters. The theoretical maximum productivity of a hypothetical algal culture would be 1.6 g m^?2 h^?1 in the NHTR, and we have previously achieved a maximum of 1.5 g m^?2 h^?1 growing Arthrospira at densities up to 7.5 g L^?1 in this reactor. Due to enhanced mass transfer in the ENHTR, the predicted maximum productivity should increase to 4.75 g m^?2 h^?1. The potential for further improvements in productivity due to various additional enhancements is described.     

Photosynthetic Electron Transfer in Preparations of the Cyanobacterium Spirulina platensis

Electron transfer activity in intact trichomes of Spirulina platensis (Nordst.) Geitl. can be observed with either CO₂ or methylviologen as the Hill acceptor. Ferricyanide cannot penetrate the intact trichomes, but photoreduction of this oxidant can be observed when mediated by lipophilic oxidants such as p-phenylenediamine or 2,5-dimethyl-p-benzoquinone. The insensitivity of these reactions to dibromothymoquinone indicates that they are due largely to the activity of photosystem II. Direct photoreduction of ferricyanide can be observed in spheroplasts of Spirulina, indicating that such preparations have altered permeability properties when compared with intact trichomes. Preparation of these spheroplasts, which are osmotically fragile, requires that intact trichomes be washed with KCl and EDTA to induce lysozyme sensitivity and thereby allow digestion of the cell wall. The KCl/EDTA washing procedure used for spheroplast preparation alters the permeability of Spirulina trichomes, as evidenced by the ability of these preparations to photoreduce ferricyanide. This photoreduction reaction is insensitive to dibromothymoquinone, and is stimulated by high concentrations of divalent cations. During assays, the reaction is inhibited by the inclusion of polyethyleneglycol as an osmotic protectant. Photoreduction of methylviologen and NADP⁺ is also observed in the washed trichomes, along with an endogenously catalyzed photoreduction of O₂ to H₂O₂. Photophosphorylation cannot be observed in the washed preparations, but cyclic photophosphorylation with phenazinemethosulfate is observed after mild sonication. These results indicate that KCl/EDTA-washed trichomes of S. platensis retain the full range of energy transducing capacities associated with thylakoid membranes of the intact trichomes; the washing procedure facilitates spheroplast formation and alters, but does not abolish, permeability barriers in these preparations.     

Productivity of outdoor algal cultures in enclosed tubular photobioreactor

At quasi-steady-state outdoor cyclic fed batch cultures of Chlorella pyrenoidosa, the growth irradiance incidented on the tubular photobioreactor increased about fivefold between 9:00 a.m. and noon. Overheating of the cultures was observed, resulting in decreasing biomass output rate when culture temperature went above 40 degrees C. In cultures with temperature control, the quasi-steady-state output rate of all cultures increased throughout the day and leveled off in the late afternoon in high-density cultures. The daily area output rate was proportional to the density of the cultures. The specific growth rate of the light-limited cultures increased only marginally (20%) in the morning. (c) 1992 John Wiley & Sons, Inc.