Approximation of continuous fermentation by semicontinuous cultures

Semicontinuous fermentations, in which a fraction of a culture is replaced with fresh media at regular intervals, have been previously used as a means of approximating continuous growth. In most cases deviations from continuous operation were erroneously estimated using Fencl's model, which is only valid when the specific growth rate is independent of the substrate concentration. An approach to modeling Semicontinuous growth that incorporates the same kinetics followed in batch and continuous growth was developed and tested for Monod's expression for the specific growth rate. A dimensionless form of the model was used to simulate Semicontinuous fermentations for comparison to continuous growth. Differences between Semicontinuous and continuous growth were found to depend on three dimensionless variables: feed concentration, replacement rate, and time between replacements. For given values of the dimensionless feed concentration and time between replacements, a range of dimensionless replacement rates can be determined over which semi-continuous cultures are approximately continuous.     

Nitrogen removal and recycling by Scenedesmus obliquus in semicontinuous cultures using artificial wastewater and a simulated light and temperature cycle

Semicontinuous cultures of Scenedesmus obliquus in artificial wastewater were maintained with 30% and 40% daily dilutions and under a 14:10 h light-dark cycle, with temperatures of 25.5 and 17 degrees C during light and dark hours. Under this regime, the production of organic biomass was 39.3 and 25.2 mg l(-1)d(-1) for the 30% and 40% dilutions, and 24.9 and 16.7 mg l(-1)d(-1) of single-cell proteins. Most of the nitrogen removal took place during the light hours, with daily totals of 9.27 and 8.45 mg l(-1) for the 30% and 40% dilutions. With the former, 43.7% of the nitrogen removed was recycled by the microalgae into proteins and other organic nitrogen cell contents, but this efficiency decreased to 26.4% when the dilutions were raised to 40%.     

Inorganic carbon sources and biomass regulation in intensive microalgal cultures

Three freshwater and one marine algal species were grown under inorganic carbon limitation in laboratory continuous cultures. Comparisons were made between HCO₃^? alkalinity and bubbled CO₂ as carbon sources. HCO₃^? alkalinity was an excellent source of inorganic carbon below specific pH levels, but chemical precipitation at high pH placed an upper limit on productivity that was far lower than potential light-limiting levels. With bubbled CO₂ it was possible to achieve light limitation. The main factor controlling productivity was the mass flux of inorganic carbon added to the culture, which is the product of gas flow rate and influent P level. Small bubbles were more efficient than large bubbles at low gas flow rates and P levels, but led to froth flotation of algal cells and concomitant reductions in productivity at high bubble rates. At 1% CO₂ productivity was still dependent on mass fluxes of added carbon, but was independent of bubble size. At high bubble rates with 1% CO₂ narcosis was evident. Maximum yields occurred at intermediate dilution rates when inorganic carbon was supplied via bubbled gas.     

Heavy metals removal by the microalga Scenedesmus incrassatulus in continuous cultures

The microalga Scenedesmus incrassatulus was grown under continuous regime in the presence of chromium(VI), cadmium(II) and copper(II), as single metal species and as mixtures of two or three metals, in a laboratory scale system. We used an artificial wastewater with low free ion activities (as determined by MINEQL+) due to the presence of EDTA (a strong chelating agent) but with total concentrations not suitable for acceptable environments. Chromium(VI) and cadmium(II) had positive interaction that increased the removal percentages of both these metals; we could not, however, detect any interaction with copper(II). S. incrassatulus was able to remove all the tested metals to some extent (25-78%), but bivalent metals were not removed as efficiently as reported in batch cultures, probably due to the high pH values there recorded. Chromium(VI) was more efficiently removed in continuous cultures than in batch culture, because the uptake of chromate could be favored by actively growing algae.     

Improved performance of anaerobic digestion ofSpirulina maxima algal biomass by addition of carbon-rich wastes

Mixtures of carbon-rich wastes andS. maxima algal biomass increase markedly the performance of anaerobic digestion. A mixture of 507 sewage sludge and algae increases the methane yield and the productivity over twofold. Peat hydrolyzate and sewage sludge, when added to algae, have shown a synergistic effect and spent sulfite liquor added at concentrations over 307 V/V has inhibited methanogenic activity.     

Microbial lipid production by oleaginous yeasts grown on Scenedesmus obtusiusculus microalgae biomass hydrolysate

Bioprocess and Biosystems Engineering - Due to increasing oil prices and climate change concerns, biofuels have become increasingly important as potential alternative energy sources. However, the...     

Factors controlling eicosapentaenoic acid production in semicontinuous cultures of marine microalgae

Three marine microalgal species with a high content of eicosapentaenoic acid (EPA), Phaeodactylum tricornutum, Isochrysis galbana and Porphyridium cruentum, were cultured semicontinuously in order to study the effect of renewal rate on EPA productivity. The percentage of EPA in total fatty acids increased with increasing renewal rates in nitrogen limited cultures, but while for Phaeodactylum tricornutum and Isochrysis galbana a plateau around 20–25% of total fatty acids was reached with renewal rates that were not nitrogen-limiting, in Porphyridium cruentum EPA percentage increased continuously with increasing renewal rate even for those cultures that were nitrogen sufficient. Maximal EPA productivities of4.6 mg L^-1 day^-1 for Isochrysis galbana and 5.2 mg L^-1 day^-1 for Phaeodactylum tricornutum were achieved with renewal rates of 20% and 30% respectively. On the other hand for Porphyridium cruentum maximal EPA productivity, 5.3 mg L^-1 day^-1, was obtained with the maximal renewal rate tested. Results indicate that different culture strategies should be adopted for the production of a particular polyunsaturated fatty acid depending on the microalgal species being used. This revised version was published online in August 2006 with corrections to the Cover Date.     

Exopolysaccharide, pigment and protein production by the marine microalga Chroomonas sp. in semicontinuous cultures

The marine microalga Chroomonas sp. isolated from Venezuela was grown in semicontinuous culture in order to study the effect of renewal rate and nutrient concentration on alloxanthin, chlorophyll a, carotenoid, carbohydrate, exopolysaccharide, protein and cell productivity. Maximal cell productivity of 8.43 ± 1.8 and 8.81 ± 2.3 × 10⁹ cell l^–1 day^–1 were achieved with renewal rates of 30 and 40%. Maximal protein and chlorophyll productivity of 64.64 ± 2.3 and 2.72 ± 0.3 mg l^–1 day^–1 were obtained with renewal rate of 20 and 30%. Biochemical composition of Chroomonas sp. was influenced by renewal rate. Nutrient concentration seems not to affect cell, protein, chlorophyll and carotenoid productivity. However, carbohydrate and exopolysaccharide productivity of 7.56 ± 0.4 and 9.57 ± 1.2 mg l^–1 day^–1 were increased at 12 mM NaNO₃(P < 0.05). Also, alloxanthin and chlorophyll a production analysed by HPLC, were higher between 8 and 12 mM NaNO₃ at a renewal rate of 30%. Results demonstrated that a renewal rate of 30% and nutrient concentration at 8 mM NaNO₃ optimize the cell, protein, carbohydrate, chlorophyll a, and exopolysaccharide productivity in semicontinuous cultures of Chroomonas. This microalga, as biological source of commercially valuable compounds, shows high capacity for changing its productivity and biochemical composition in semicontinuous system on the basis of nutrient concentration and the renewal rate.     

Potential of biogas recirculation to enhance biomass accumulation on supporting media

Two lab-scale anaerobic hybrid reactors (AHR) were operated to investigate the effect of recirculated biogas on the development of biomass on supporting media during the start-up. The reactor comprised of two distinct zones; sludge bed on the bottom and packed bed using nylon fiber as the media on the upper half of the reactor. Both reactors were continuously fed with cassava starch wastewater. The organic loading rate (OLR) was increased from 0.3 to 5.5 g COD/L/day by gradually decreasing the hydraulic retention time (HRT) from 37 to 3.5 days in two months. The biogas at 2.6 L/L/day was recirculated merely in the first month of the operation in order to allow the attached biomass to grow according to the organic matters present in the reactor at the final stage of the start up. Chemical oxygen demand (COD) removal efficiency of over 80% was achieved throughout the study. The result demonstrated a better COD removal efficiency for the reactor with biogas recirculation, especially at low HRTs. The amounts of biomass accumulated on the media in both reactors were slightly different with 11.9 gVSS found on the one with biogas recirculation compared to 9.8 gVSS on the other. In addition, 16.3% increase of the sludge bed was achieved with biogas recirculation as opposed to 9% in the control one. The attached biomass activity test indicated a greater amount and more favorable ratio of the methanogenic bacterial group on the media with the recirculation correlating well to a relatively higher methane content in biogas. As a result, the recirculation of biogas has a potential of improving the characteristics of the AHR especially in terms of biomass accumulation.     

Improved nutrient medium for biomass and valepotriate production in extended period stock cultures of Valeriana glechomifolia

Valeriana glechomifolia, a southern Brazilian endemic species commonly known as Valerian, accumulates the bioactive terpene derivatives valepotriates in all of its organs. In vitro growth of V. glechomifolia on solid Murashige and Skoog (MS) without phytohormones at full, 75% (MS 75), or on a modified formulation (M Δ) was compared in stock cultures kept for up to 9 mo. without subculture. Changes in biomass accumulation, development of roots and shoots, and the production of the valepotriates acevaltrate, didrovaltrate, and valtrate were monthly evaluated. The highest biomass accumulation and root development was observed in plants grown on M Δ, whereas better leaf development was detected in M-Δ- and MS-medium-grown plants after 8 and 9 mo. of culture, respectively. Maximal didrovaltrate and valtrate yields were observed in M-Δ-grown plants harvested after 5 and 6 mo. of culture, respectively, whereas acevaltrate concentration was highest on M-Δ- and MS-75-grown plants after 7 mo. of culture. Plants grown for 6 mo. without subculture in M Δ were successfully propagated, showing stable growth and valepotriate yields three- to sixfold higher that those observed in field-grown plants. The results showed a positive effect of combined moderate reduction in salt concentration and increases in selected micronutrients and myo-inositol amounts on both growth and valepotriate yields of extended period stock cultures of V. glechomifolia.     

Kinetic studies of paclitaxel production by Taxus canadensis cultures in batch and semicontinuous with total cell recycle

Suspension cultures of Taxus canadensis were elicited with methyl jasmonate (MJ) under defined headspace ethylene concentrations. Kinetic studies of growth, nutrient consumption, pH variation, and paclitaxel accumulation were conducted in batch cultures and semicontinuous culture with total cell recycle. A dramatic increase of paclitaxel was obtained when the cultures were elicited with 100 microM MJ, but cell growth was thereby arrested. Supplementation of acetyl-CoA and MJ to the culture proved to be another way to improve paclitaxel yields. Using semicontinuous culture with total cell recycle, paclitaxel accumulation was increased by a factor of 4.0 relative to that in the batch culture during 35 days of cultivation.     

Technoeconomic analysis of semicontinuous bioreactor production of biopharmaceuticals in transgenic rice cell suspension cultures

Biopharmaceutical protein production using transgenic plant cell bioreactor processes offers advantages over microbial and mammalian cell culture platforms in its ability to produce complex biologics with simple chemically defined media and reduced biosafety concerns. A disadvantage of plant cells from a traditional batch bioprocessing perspective is their slow growth rate which has motivated us to develop semicontinuous and/or perfusion processes. Although the economic benefits of plant cell culture bioprocesses are often mentioned in the literature, to our knowledge no rigorous technoeconomic models or analyses have been published. Here we present technoeconomic models in SuperPro Designer® for the large-scale production of recombinant butyrylcholinesterase (BChE), a prophylactic/therapeutic bioscavenger against organophosphate nerve agent poisoning, in inducible transgenic rice cell suspension cultures. The base facility designed to produce 25 kg BChE per year utilizing two-stage semicontinuous bioreactor operation manufactures a single 400 mg dose of BChE for $263. Semicontinuous operation scenarios result in 4–11% reduction over traditional two-stage batch operation scenarios. In addition to providing a simulation tool that will be useful to the plant-made pharmaceutical community, the model also provides a computational framework that can be used for other semicontinuous or batch bioreactor-based processes.     

Improved podophyllotoxin production by transformed cultures of Linum album

Various cell and hairy root cultures of L. album were developed and analyzed for podophyllotoxin content. Transformed callus and hairy root cultures developed from infection of stem portions of in vitro-germinated L. album plant with Agrobacterium rhizogenes NCIM 5140 strain were selected on the basis of high podophyllotoxin content and growth. Based on the integration of Ri T(L)-DNA and T(R)-DNA, integration of only the ags and not the rol gene in transformed cell culture indicated fragmented integration pattern. The effect of different cultivation media and carbon source on growth and podophyllotoxin production were studied in shake-flask suspension cultures. Detailed batch growth and production kinetics with sugar consumption profile were also established. Maximum volumetric productivity of 4.40 and 2.75 mg/L per day was obtained in cell suspension and hairy root cultures, respectively.     

Use of industrial wastewater from olive-oil extraction for biomass production of Scenedesmus obliquus

The use of rinse water (RW) from two-phase centrifugation in the olive-oil extraction industry has been studied in relation to the production of the microalga Scenedesmus obliquus (CCAP 276/3A). The characterization of the wastewater indicates that it is N deficient. The highest value of maximum specific growth rate, 0.044 h(-1) was registered in the culture with 5% RW. However, biomass productivity proved greater in the culture with 100% RW. The specific growth rates were adjusted to a model of inhibition by substrate. The content in normalized chlorophyll diminished with the duration of the cultures, reaching a minimum CHL'(min) value, which showed an inhibition type similar to that of the specific growth rate. The yield in protein indicates that the cultures were limited by N to approximately 50% RW. The greater specific rate of protein synthesis during the exponential phase was 3.7 mg/gh to 50% RW. It was found that the composition of the lipid fraction of the biomass depended on the percentage of wastewater used as the nutrient medium, reaching the highest percentages of monounsaturated, polyunsaturated, and essential fatty acids in the culture with 100% RW.     

Key parameters for outdoor biomass production of Scenedesmus obliquus in solar tracked photobioreactors

The biomass productivity of Scenedesmus obliquus was investigated outdoors during all seasons in solar tracked flat panel photobioreactors (PBR) to evaluate key parameters for process optimization. CO₂ was supplied by flue gas from an attached combined block heat and power plant. Waste heat from the power plant was used to heat the culture during winter. The parameters pH, CO₂, and inorganic salt concentrations were automatically adjusted to nonlimiting levels. The optimum biomass concentration increased directly with the photosynthetic active radiation (PAR) from 3 to 5 g dry weight (DW)?L^?1 for a low PAR of 10 mol photons m^?2 day^?1 and high PAR of 40–60 mol photons m^?2 day^?1, respectively. The annual average biomass yield (photosynthetic efficiency) was 0.4?±?0.5 g DW mol^?1 photons. However, biomass yields of 1.5 g DW mol^?1 photons close to the theoretical maximum were obtained at low PAR. The productivity (including the night biomass losses) ranged during all seasons from ?5 up to 30 g DW m^?2 day^?1 with a mean productivity of 9?±?7 g DW m^?2 day^?1. Low night temperatures of the culture medium and elevated day temperatures to the species-specific optimum increased the productivity. Thus, continuous regulation of the biomass concentration and the culture temperature with regard to the fluctuating weather conditions is essential for process optimization of outdoor microalgal production systems in temperate climates.     

Improved biomass production of cyanobacteria by reutilization of the culture medium

The biomass production of a cyanobacterium (Nostoc sp.) in a photoreactor with a low illuminated surface area to volume ratio was improved by the reutilization of the culture medium. After six succesive utilizations the growth ofNostoc sp. amounted to 2.15 g/l with an average content in phycobiliproteins of 14.4% on dry weight basis. The procedure reported allowed an 80% increase in biomass. The cellular self-sedimentation proved to be effective for biomass separation between reutilization steps.