Biodegradation of methyl parathion in the presence of goethite: The effect of Pseudomonas sp. Z1 adhesion

In this research, the influence of goethite on biodegradation kinetic of methyl parathion was investigated in the presence of Pseudomonas sp. Z1. Semipermeable membrane experiments were performed to demonstrate the role of adhesion of degrading bacteria to surface of goethite in biodegradation of methyl parathion. Sorption of methyl parathion and bacteria onto goethite particles were also measured to assess the distribution of methyl parathion and bacteria between water and goethite surface. The first-order degradation rate constant of methyl parathion in different concentrations of goethite was in the order of 0.1 g L⁻¹ > 0.01 g L⁻¹ > 0 g L⁻¹ > 1 g L⁻¹ > 20 g L⁻¹, suggesting the presence of low concentrations of goethite accelerated the biodegradation of methyl parathion and high concentrations of goethite inhibited this biodegradation process. According to the result of semipermeable membrane experiment, when no bacterial attachment occurred in the system, the promotive effect of 0.1 g L⁻¹ goethite for microbial degradation was disappeared and the inhibition effect of 20 g L⁻¹ goethite increased. The results clearly demonstrated that the adhesion of bacteria to goethite was beneficial to the biodegradation of methyl parathion. The information obtained is of fundamental significance for the understanding of microbial degradation of organic pollution in soil.     

Biodegradation of indole at high concentration by persolvent fermentation with the thermophilic fungus Sporotrichum thermophile

Indole and its derivatives form a class of toxic recalcitrant environmental pollulants. Sporotrichum thermophile was grown in a persolvent fermentation system containing a large amount of indole. The medium contained up to 20% by volume soybean oil and up to 2 g L⁻¹ indole. Most of the indole was partitioned in the organic solvent layer. When the organism was grown in the medium containing indole at 1 g L⁻¹, indole was totally consumed after 6 days. Under a fed–batch fermentation process where daily batches of indole (1 g L⁻¹) supplemented the microbial culture for 4 days, the biodegradation level was 3.0 g L⁻¹. These values make this process promising and worthy of further investigation for the microbial degradation of other toxic compounds.     

An efficient callus-based in vitro regeneration protocol for Warburgia Ugandensis Sprague,an important medicinal plant in Africa

Warburgia ugandensis Sprague is a woody species in the family Canellaceae and an important source of medicines in Africa. Natural propagation of W. ugandensis is problematic due to its recalcitrant seeds and lack of an efficient in vitro regeneration system for this species. This study describes an efficient regeneration protocol. Petiole bases and shoot tips were used as explants. Callus tissue developed when the explants were cultured on Murashige and Skoog medium containing 30 g L⁻¹ sucrose and 7 g L⁻¹ agar (MS30 medium), supplemented with 1.0 mg L⁻¹ indole-3-butyric acid (IBA), 1.6 mg L⁻¹ 6-benzylaminopurine (BA), and 0.1 mg L⁻¹ thidiazuron (TDZ). Adventitious buds were efficiently induced from the callus when the MS30 medium was supplemented with 0.8 mg L⁻¹ BA and 0.2 mg L⁻¹ IBA. Root induction occurred within 7–10 d on half-strength MS30 medium supplemented with 0.8–1.0 mg L⁻¹ 1-napthalene acetic acid (NAA), 0.2 mg L⁻¹ IBA, and 0.03% (w/v) activated charcoal (AC). Roots were followed by root elongation on the same medium but lacking NAA and IBA. Approximately 50% of the plantlets cultured produced roots, while more than 80% of the plantlets survived and successfully grew to maturity.

     

Smoke-saturated Water and Karrikinolide Modulate Germination,Growth, Photosynthesis and Nutritional Values of Carrot (Daucus carota L.)

Plant-derived smoke is a positive regulator of seed germination and growth with regard to many plant species. Of the several compounds present in plant-derived smoke, karrikinolide or KAR₁ (3-methyl-2H-furo[2,3-c]pyran-2-one) is considered to be the major active growth-promoting compound. To test the efficacy of smoke-saturated water (SSW) and KAR₁ on carrot (Daucus carota L.), two separate pot experiments were simultaneously conducted in the same environmental conditions. SSW and KAR₁ treatments were applied to the plants in the form of aqueous solutions of variable concentrations. Prior to sowing, seeds were soaked in the solutions of SSW (25.8 µg L⁻¹_, 51.6 µg L⁻¹,103.2 µg L⁻¹ and 258.0 µg L⁻¹) and KAR₁ (0.015 µg L⁻¹, 0.150 µg L⁻¹, 1.501 µg L⁻¹ and 15.013 µg L⁻¹). Percent seed germination, vegetative growth, photosynthesis and nutritional values were the major parameters through which the plant response to the applied treatments was investigated. The results obtained indicated a significant improvement in all the plant attributes studied. In general, SSW (51.6 µg L⁻¹) and KAR₁ (1.501 µg L⁻¹) proved optimum treatments for most the parameters. As compared to the control, 51.6 µg L⁻¹ of SSW and 1.501 µg L⁻¹ of KAR₁ increased the percent seed germination by 58.0% and 54.4%, respectively. Over the control, the values of plant height and net photosynthetic rate were enhanced by 33.9% and 40.9%, respectively, due to 51.6 µg L⁻¹ of SSW, while the values of these parameters were increased by 25.2% and 34.0%, respectively, due to 1.501 µg L⁻¹ of KAR₁. In comparison with the control, treatment 51.6 µg L⁻¹ of SSW increased the contents of β-carotene and ascorbic acid by 32.7% and 37.9%, respectively, while the treatment 1.501 µg L⁻¹ M of KAR₁ enhanced these contents by 42.0% and 48.4%, respectively. This study provides an insight into an affordable and feasible method of crop improvement.

     

Genetic homogeneity and high shoot proliferation in banana (Musa acuminata Colla) by altering medium thiamine level and sugar type

To enhance the multiplication rate in Musa acuminata Colla (banana; ‘Grand Nain’) organogenesis, higher amounts of thiamine along with different sugar types and concentrations were evaluated at the proliferation phase. Thiamine at 1, 10, 50, 100, and 200 mg L⁻¹ was compared with 0.1 mg L⁻¹ thiamine found in conventional Murashige and Skoog (MS) medium. Maximum proliferation of banana was induced with 100 mg L⁻¹ thiamine. Additionally, 15, 30, and 45 g L⁻¹ sucrose, glucose, fructose, and sorbitol combined with regular and optimal levels of thiamine were tested. Glucose at 30 g L⁻¹ most improved shoot proliferation alone and enhanced shoot proliferation further, when combined with 100 mg L⁻¹ thiamine, followed by sucrose and fructose, whereas sorbitol completely inhibited growth and caused tissue browning. All evaluated vegetative traits were significantly affected by sugar type and concentration, and thiamine levels, unlike the photosynthetic pigments. Moreover, genetic stability of the plants recovered from the enhanced protocol was confirmed by inter-simple sequence repeats (ISSR) and randomly amplified polymorphic DNA (RAPD) analysis. A total of 230 bands generated by both marker types were monomorphic for the randomly selected regenerated plants, compared with their mother plant. Thus, the proliferation medium supplemented with 30 g L⁻¹ glucose and 100 mg L⁻¹ thiamine could be recommended for banana organogenesis. Results herein are of great importance and helpful in enhancing the commercial in vitro propagation protocols of banana, without the need of increasing the number of subcultures, which can cause somaclonal variation.

     

Soluble sugar,starch and phenolic status during rooting of easy- and difficult-to-root magnolia cultivars

The aim of the study was to determine the effect of indole-3-butyric acid (IBA) and exogenous sucrose concentrations on in vitro rooting, soluble sugar, starch and phenolic production, and ex vitro survival of four magnolia cultivars. There was a significant linear increase in rooting of most magnolia genotypes with an increase in IBA concentration in the medium from 1 to 6 mg L^?1. A further increase of IBA concentration to 10 mg L^?1 decreased (‘Elizabeth’, ‘Burgundy’) or had no effect on rooting frequency (‘Spectrum’). The effect of IBA on rooting of magnolia shoots was modified by sucrose supply. The three out of four magnolia cultivars showed the highest rooting efficiency in the presence of 6 mg L^?1 IBA and 30 g L^?1 of sucrose. Generally, decreasing and increasing the sucrose supply from 30 g L^?1 significantly lowered the rooting frequency. In ‘Yellow Bird’, sucrose at 40 g L^?1 totally blocked root formation. It has been found that the poor rooting ability of ‘Yellow Bird’ coincided with a low soluble sugar content, and high production of starch and phenolics in the shoot bases during the whole rooting period as compared to easy-to-root cultivars. After 5 weeks of the growth on IBA medium, rooted and unrooted shoots were transferred to ex vitro conditions. Both types of shoots showed a high survival and rooting rate (85.4–100%), but they differed in their growth activity and quality. Sucrose concentration in the rooting medium had a post-effect on ex vitro root formation and survival of magnolia plantlets. Ex vitro establishment (13.3%) of recalcitrant ‘Yellow Bird’ was obtained only when the shoots were taken from rooting medium containing the lowest level of sucrose (20 g L^?1).

     

Mathematical modeling of the ethanol fermentation of cashew apple juice by a flocculent yeast: the effect of initial substrate concentration and temperature

In this work, the effect of initial sugar concentration and temperature on the production of ethanol by Saccharomyces cerevisiae CCA008, a flocculent yeast, using cashew apple juice in a 1L-bioreactor was studied. The experimental results were used to develop a kinetic model relating biomass, ethanol production and total reducing sugar consumption. Monod, Andrews, Levenspiel and Ghose and Tyagi models were investigated to represent the specific growth rate without inhibition, with inhibition by substrate and with inhibition by product, respectively. Model validation was performed using a new set of experimental data obtained at 34 °C and using 100 g L⁻¹ of initial substrate concentration. The model proposed by Ghose and Tyagi was able to accurately describe the dynamics of ethanol production by S. cerevisiae CCA008 growing on cashew apple juice, containing an initial reducing sugar concentration ranging from 70 to 170 g L⁻¹ and temperature, from 26 to 42 °C. The model optimization was also accomplished based on the following parameters: percentage volume of ethanol per volume of solution (%V _ethanol/V _solution), efficiency and reaction productivity. The optimal operational conditions were determined using response surface graphs constructed with simulated data, reaching an efficiency and a productivity of 93.5% and 5.45 g L⁻¹ h⁻¹, respectively.

     

Ferric iron and extracellular electron shuttling increase xylose utilization and butanol production during fermentation with multiple solventogenic bacteria

Xylose is the second most abundant sugar derived from lignocellulose; it is considered less desirable than glucose for fermentation, and strategies that specifically increase xylose utilization in wild-type cells are goals for biofuel production. Xylose consumption, butanol production, and hydrogen production increased in both Clostridium beijerinckii and a novel solventogenic bacterium (strain DC-1) when anthraquinone-2,6,-disulfonate (AQDS) or riboflavin were used as redox mediators to transfer electrons to poorly crystalline Fe(OH)₃ as an extracellular electron sink. Strain DC-1 was most closely related to Rhizobiales bacterium Mfc52 based on 95% 16S rRNA gene sequence similarity, which demonstrates that this response is not limited to a single genus of xylose-fermenting bacteria. Xylose utilization and butanol production were negligible in control incubations containing cells plus 3% (w/v) xylose alone during a 10-day batch fermentation, for both strains tested (n-butanol titers of 0.05 g L⁻¹). Micromolar concentrations of AQDS and riboflavin were added as electron shuttling compounds with poorly crystalline Fe(OH)₃ as an insoluble electron acceptor, and respective n-butanol titers increased to 6.35 and 7.46 g L⁻¹. Increases in xylose consumption for the iron treatments were relatively high, from less than 0.49 g L⁻¹ (xylose alone, no iron or electron shuttling molecules) to 25.98 and 29.15 g L⁻¹ for the AQDS and riboflavin treatments, respectively. Hydrogen production was also 3.68 times greater for the AQDS treatment and 5.27 greater for the riboflavin treatment relative to controls. Strain DC-1 data were similar, again indicating that the effects are not specific to the genus Clostridium.

     

Production of ginsenoside and polysaccharide by two-stage cultivation of Panax quinquefolium L. cells

Based on the results of carbon source consumption in cell suspension culture of Panax quinquefolium L., 30 g L⁻¹ sucrose was fed into a 5-L stirred tank bioreactor on day 16 of culture to enhance cell density and metabolite production. Using a fed-batch cultivation strategy, polysaccharide production was enhanced to 1.608 g L⁻¹, which was 1.96-fold greater than with batch cultivation. The maximum saponin yield (7.828 mg L⁻¹) was obtained on day 24 and was about 36% higher than the yields obtained using batch cultivation. In a two-stage culture process, a combined treatment with sucrose, lactoalbumin hydrolysate, and methyl jasmonate caused a significant increase in total saponin yield (31.52 mg L⁻¹) in cell cultures after 27 d. This value represents an increase of 4.03-fold compared with the total saponin yield in fed-batch cultivation. The two-stage culture mode provided the best method for the in vitro production of secondary metabolites from P. quinquefolium.     

Production of hexanoic acid from d-galactitol by a newly isolated Clostridium sp. BS-1

In a study screening anaerobic microbes utilizing d-galactitol as a fermentable carbon source, four bacterial strains were isolated from an enrichment culture producing H₂, ethanol, butanol, acetic acid, butyric acid, and hexanoic acid. Among these isolates, strain BS-1 produced hexanoic acid as a major metabolic product of anaerobic fermentation with d-galactitol. Strain BS-1 belonged to the genus Clostridium based on phylogenetic analysis using 16S rRNA gene sequences, and the most closely related strain was Clostridium sporosphaeroides DSM 1294^T, with 94.4% 16S rRNA gene similarity. In batch cultures, Clostridium sp. BS-1 produced 550 ± 31 mL L⁻¹ of H₂, 0.36 ± 0.01 g L⁻¹ of acetic acid, 0.44 ± 0.01 g L⁻¹ of butyric acid, and 0.98 ± 0.03 g L⁻¹ of hexanoic acid in a 4-day cultivation. The production of hexanoic acid increased to 1.22 and 1.73 g L⁻¹ with the addition of 1.5 g L⁻¹ of sodium acetate and 100 mM 2-(N-morpholino)ethanesulfonic acid (MES), respectively. Especially when 1.5 g L⁻¹ of sodium acetate and 100 mM MES were added simultaneously, the production of hexanoic acid increased up to 2.99 g L⁻¹. Without adding sodium acetate, 2.75 g L⁻¹ of hexanoic acid production from d-galactitol was achieved using a coculture of Clostridium sp. BS-1 and one of the isolates, Clostridium sp. BS-7, in the presence of 100 mM MES. In addition, volatile fatty acid (VFA) production by Clostridium sp. BS-1 from d-galactitol and d-glucose was enhanced when a more reduced culture redox potential (CRP) was applied via addition of Na₂S·9H₂O.     

Bioproduction of phenylethanoid glycosides by plant cell culture of Scrophularia striata Boiss.: from shake-flasks to bioreactor

Phenylethanoid glycosides (PeG) are a class of polyphenols found in some plants that have pharmaceutical effects as anti-inflammatories and anti-oxidants. The presence of PeG (acteoside) in the aerial parts of Scrophularia striata Boiss. has been demonstrated. Considerable progress has been made using plant cell cultures to stimulate formation and accumulation of secondary metabolites. The present study optimized phenylethanoid production from shake flasks to bioreactor using a cell culture of S. striata. The optimal conditions for production of cell biomass by scale-up to a bioreactor were determined to be a pH of 4.8, air flow rate of 0.5–1.5 l min⁻¹, and mixing speed of 110–170 rpm at 25 ± 1 °C in darkness. Growth parameters and PeG production were measured and compared with the results from the shake flasks. The results showed that cell biomass was high in the bioreactor (15.64 g l⁻¹ DW) and in the shake flasks (14.16 g l⁻¹ DW). The acteoside content in the bioreactor was 1404.20 μg g⁻¹ DW, which is threefold higher than in the shake flasks (459.71 μg g⁻¹ DW). The echinacoside concentration in the bioreactor was 1449.39 μg g⁻¹, 1.36-fold lower than in the shake flasks (1973.03 μg g⁻¹ DW). This study established an efficient way for production of acteoside, the major PeG, in a bioreactor.

     

Effect of carbon sources on the growth and ethanol production of native yeast Pichia kudriavzevii ITV-S42 isolated from sweet sorghum juice

The importance of non-Saccharomyces yeast species in fermentation processes is widely acknowledged. Within this group, Pichia kudriavzevii ITV-S42 yeast strain shows particularly desirable characteristics for ethanol production. Despite this fact, a thorough study of the metabolic and kinetic characteristics of this strain is currently unavailable. The aim of this work is to study the nutritional requirements of Pichia kudriavzevii ITV-S42 strain and the effect of different carbon sources on the growth and ethanol production. Results showed that glucose and fructose were both assimilated and fermented, achieving biomass and ethanol yields of 0.37 and 0.32 gg⁻¹, respectively. Glycerol was assimilated but not fermented; achieving a biomass yield of 0.88 gg⁻¹. Xylose and sucrose were not metabolized by the yeast strain. Finally, the use of a culture medium enriched with salts and yeast extract favored glucose consumption both for growth and ethanol production, improving ethanol tolerance reported for this genre (35 g L⁻¹) to 90 g L⁻¹ maximum ethanol concentration (over 100%). Furthermore Pichia kudriavzevii ITV-S42 maintained its fermentative capacity up to 200 g L⁻¹ initial glucose, demonstrating that this yeast is osmotolerant.

     

Production of d-arabitol by a newly isolated Kodamaea ohmeri

A new yeast, isolated from natural osmophilic sources, produces d-arabitol as the main metabolic product from glucose. According to 18S rRNA analysis, the NH-9 strain belongs to the genus Kodamaea. The optimal culture conditions for inducing production of d-arabitol were 37 °C, neutral pH, 220 rpm shaking, and 5% inoculum. The yeast produced 81.2 ± 0.67 g L⁻¹ d-arabitol from 200 g L⁻¹ d-glucose in 72 h with a yield of 0.406 g g⁻¹ glucose and volumetric productivity Q_\textP Q_{\text{P}} of 1.128 g L⁻¹ h⁻¹. Semi-continuous repeated-batch fermentation was performed in shaker-flasks to enhance the process of d-arabitol production by Kodamaea ohmeri NH-9 from d-glucose. Under repeated-batch culture conditions, the highest volumetric productivity was 1.380 g L⁻¹ h⁻¹.     

Morpho-anatomical and physiological changes of Indian sandalwood (Santalum album L.) plantlets in ex vitro conditions to support successful acclimatization for plant mass production

Santalum album L. (Indian sandalwood) is an economically important but vulnerable tropical tree species. Cultures were established via direct shoot regeneration from axillary buds on Murashige and Skoog (MS) medium supplemented with 2.5 mg L^?1 6-benzylaminopurine (BAP). The shoots were multiplied using MS medium containing 1.0 mg L^?1 BAP and 0.5 mg L^?1 indole-3 acetic acid and rooted on half strength MS medium containing 1.0 mg L^?1 indole-3 butyric acid. The rooted plantlets were hardened and acclimatized in greenhouse using soilrite® and cocopeat (1:1) mixture. The concentrations of photosynthetic pigments were analyzed and detected less under in vitro conditions (6.05 μg g^?1 FW) as compared to the 4 weeks old hardened (6.91 μg g^?1 FW) and 12 weeks old acclimatized plantlets (7.8 μg g^?1 FW) under greenhouse (ex vitro) environment. The anatomical evaluation of plantlets at subsequent stages of propagation suggested that the in vitro raised plantlets possessed structural abnormalities such as underdeveloped cuticle, unorganized tissue systems, reduced mesophyll tissues, fewer vascular elements and mechanical tissues, and loosely arranged thin walled paranchymatous ground tissues, which were slowly repaired during ex vitro hardening and acclimatization process to validate the developmental adaptation of micropropagated plantlets for maximum survival in the field (98.0% survival rate). The findings could help in the optimization of high-frequency commercial micropropagation of S. album for year-round production, and supply of this economically prominent vulnerable plant species to the farmers and the industries that rely on it.

     

Azo dyes decolorization under high alkalinity and salinity conditions by Halomonas sp. in batch and packed bed reactor

Biodecolorization and biodegradation of azo dyes are a challenge due to their recalcitrance and the characteristics of textile effluents. This study presents the use of Halomonas sp. in the decolorization of azo dyes Reactive Black 5 (RB5), Remazol Brilliant Violet 5R (RV5), and Reactive Orange 16 (RO16) under high alkalinity and salinity conditions. Firstly, the effect of air supply, pH, salinity and dye concentration was evaluated. Halomonas sp. was able to remove above 84% of all dyes in a wide range of pH (6–11) and salt concentrations (2–10%). The decolorization efficiency of RB5, RV5, and RO16 was found to be ≥ 90% after 24, 13 and 3 h, respectively, at 50 mg L⁻¹ of dyes. The process was monitored by HPLC-DAD, finding a reduction of dyes along the time. Further, Halomonas sp. was immobilized in volcanic rocks and used in a packed bed reactor for 72 days, achieving a removal rate of 3.48, 5.73, and 8.52 mg L⁻¹ h⁻¹, for RB5, RV5 and RO16, respectively, at 11.8 h. The study has confirmed the potential of Halomonas sp. to decolorize azo dyes under high salinity and alkalinity conditions and opened a scope for future research in the treatment of textile effluents.

     

Production and partial characterization of biosurfactant produced by Streptomyces sp. R1

The present study focused on developing a wild-type actinomycete isolate as a model for a non-pathogenic filamentous producer of biosurfactants. A total of 33 actinomycetes isolates were screened and their extracellular biosurfactants production was evaluated using olive oil as the main substrate. Out of 33 isolates, 32 showed positive results in the oil spreading technique (OST). All isolates showed good emulsification activity (E₂₄) ranging from 84.1 to 95.8%. Based on OST and E₂₄ values, isolate R1 was selected for further investigation in biosurfactant production in an agitated submerged fermentation. Phenotypic and genotypic analyses tentatively identified isolate R1 as a member of the Streptomyces genus. A submerged cultivation of Streptomyces sp. R1 was carried out in a 3-L stirred-tank bioreactor. The influence of impeller tip speed on volumetric oxygen transfer coefficient (k _L a), growth, cell morphology and biosurfactant production was observed. It was found that the maximum biosurfactant production, indicated by the lowest surface tension measurement (40.5 ± 0.05 dynes/cm) was obtained at highest k _L a value (50.94 h⁻¹) regardless of agitation speed. The partially purified biosurfactant was obtained at a concentration of 7.19 g L⁻¹, characterized as a lipopeptide biosurfactant and was found to be stable over a wide range of temperature (20–121 °C), pH (2–12) and salinity [5–20% (w/v) of NaCl].

     

Characterization of Candida sp. NY7122, a novel pentose-fermenting soil yeast

Yeasts that ferment both hexose and pentose are important for cost-effective ethanol production. We found that the soil yeast strain NY7122 isolated from a blueberry field in Tsukuba (East Japan) could ferment both hexose and pentose (d-xylose and l-arabinose). NY7122 was closely related to Candida subhashii on the basis of the results of molecular identification using the sequence in the D1/D2 domains of 26S rDNA and 5.8S-internal transcribed spacer region. NY7122 produced at least 7.40 and 3.86 g l⁻¹ ethanol from 20 g l⁻¹ d-xylose and l-arabinose within 24 h. NY7122 could produce ethanol from pentose and hexose sugars at 37°C. The highest ethanol productivity of NY7122 was achieved under a low pH condition (pH 3.5). Fermentation of mixed sugars (50 g l⁻¹ glucose, 20 g l⁻¹ d-xylose, and 10 g l⁻¹ l-arabinose) resulted in a maximum ethanol concentration of 27.3 g l⁻¹ for the NY7122 strain versus 25.1 g l⁻¹ for Scheffersomyces stipitis. This is the first study to report that Candida sp. NY7122 from a soil environment could produce ethanol from both d-xylose and l-arabinose.     

Large-scale cultivation of Spirulina in a floating horizontal photobioreactor without aeration or an agitation device

A low-cost floating photobioreactor (PBR) without the use of aeration and/or an agitation device, in which carbon was supplied in the form of bicarbonate and only wave energy was utilized for mixing, was developed in our previous study. Scaling up is a common challenge in the practical application of PBRs and has not yet been demonstrated for this new design. To fill this gap, cultivation of Spirulina platensis was conducted in this study. The results demonstrated that S. platensis had the highest productivity at 0.3 mol L⁻¹ sodium bicarbonate, but the highest carbon utilization (104 ± 2.6%) was obtained at 0.1 mol L⁻¹. Culture of Spirulina aerated with pure oxygen resulted in only minor inhibition of growth, indicating that its productivity will not be significantly reduced even if dissolved oxygen is accumulated to a high level due to intermittent mixing resulting from the use of wave energy. In cultivation using a floating horizontal photobioreactor at the 1.0 m² scale, the highest biomass concentration of 2.24 ± 0.05 g L⁻¹ was obtained with a culture depth of 5.0 cm and the highest biomass productivity of 18.9 g m⁻² day⁻¹ was obtained with a depth of 10.0 cm. This PBR was scaled up to 10 m² (1000 L) with few challenges; biomass concentration and productivity during ocean testing were little different than those at the 1.0 m² (100 L) scale. However, the larger PBR had an apparent carbon utilization efficiency of 45.0 ± 2.8%, significantly higher than the 39.4 ± 0.9% obtained at the 1 m² scale. These results verified the ease of scaling up floating horizontal photobioreactors and showed their great potential in commercial applications.

     

Continuous production of isopropanol and butanol using <Emphasis Type="Italic">Clostridium beijerinckii</Emphasis> DSM 6423

Clostridium beijerinckii DSM 6423 was studied using different continuous production methods to give maximum and stable production of isopropanol and n-butanol. In a single-stage continuous culture, when wood pulp was added as a cell holding material, we could increase the solvent productivity from 0.47 to 5.52 g L⁻¹ h⁻¹ with the yield of 54% from glucose. The overall solvent concentration of 7.51 g L⁻¹ (39.4% isopropanol and 60.6% n-butanol) with the maximum solvent productivity of 0.84 g L⁻¹ h⁻¹ was obtained with two-stage continuous culture. We were able to run the process for more than 48 overall retention times without losing the ability to produce solvents.     

Bioreactor production of 2,3-butanediol by Pantoea agglomerans using soybean hull acid hydrolysate as substrate

Production of 2,3-butanediol (2,3-BD) by Pantoea agglomerans strain BL1 was investigated using soybean hull hydrolysate as substrate in batch reactors. The cultivation media consisted of a mixture of xylose, arabinose, and glucose, obtained from the hemicellulosic fraction of the soybean hull biomass. We evaluated the influence of oxygen supply, pH control, and media supplementation on the growth kinetics of the microorganism and on 2,3-BD production. P. agglomerans BL1 was able to simultaneously metabolize all three monosaccharides present in the broth, with average conversions of 75% after 48 h of cultivation. The influence of aeration conditions employed demonstrated the mixed acid pathway of 2,3-BD formation by enterobacteria. Under fully aerated conditions (2 vvm of air), up to 14.02 g L⁻¹ of 2.3-BD in 12 h of cultivation were produced, corresponding to yields of 0.53 g g⁻¹ and a productivity of 1.17 g L⁻¹ h⁻¹, the best results achieved. These results suggest the production potential of 2,3-BD by P. agglomerans BL1, which has been recently isolated from an environmental consortium. The present work proposes a solution for the usage of the hemicellulosic fraction of agroindustry biomasses, carbohydrates whose utilization are not commonly addressed in bioprocess.