Bioleaching of arsenic from medicinal realgar by pure and mixed cultures

The aim of this paper is to determine the efficiency of bioleaching of arsenic in realgar, a Chinese mineral drug, using pure cultures of Acidithiobacillus ferrooxidans or Acidithiobacillus thiooxidans and a mixed culture of A. ferrooxidans and A. thiooxidans. The experiments were carried out in shaker flasks, at 150 rpm, 30 °C at a culture pH of 1.80. To investigate the mechanism of the bioleaching in realgar, media with and without ferrous iron were chosen for the experiments. The results showed that the leaching rate of arsenic in realgar after 20 days was higher (43%) in A. ferrooxidans cultures with ferrous iron compared to cultures without ferrous iron (10%), and the leaching rate of A. thiooxidans cultures only increased from 21% to 23% in the presence of ferrous iron. The leaching rate of arsenic in mixed culture with ferrous iron was greatly enhanced from 16% to 56%, indicating that bioleaching in mixed culture is preferable for the dissolution of realgar.     

Bioreactor leaching of uranium from a low grade Indian silicate ore

Bio-leaching studies were carried out in a 2 L bioreactor- BIOSTAT-B^® equipped with a PLC based controller at 20–40% (w/v) pulp density using enriched culture of A.ferrooxidans for Turamdih uranium ore (Jharkhand, India). With the enriched culture of A.ferrooxidans adapted on Fe(II) at pH 2.0, 35 °C and 20% (w/v) pulp density, a 98.3% uranium recovery was recorded in 14 days. The leaching of uranium in the bioreactor improved the dissolution rate by reducing the time from 40 days in shake flask as per our earlier studies to 14 days. While investigating the importance of biogenic Fe(III) in the bio-leaching process a maximum recovery of 84.7% U₃O₈ was observed at pH 2.0 and 20% (w/v) pulp density in 10 h as compared to the uranium leaching of 38.3% in the control experiments. On raising the pulp density to 30%, uranium bio-recovery increased to 87.6% in 10 h at pH 2.0 with <76 μm size material. This showed a distinct advantage because of better mixing of slurry in the bioreactor with auto-controlled conditions that improved the kinetics.     

Cellular ATP and biomass of attached and planktonic sulfur-oxidizing Acidithiobacillus ferrooxidans

This study demonstrates differences in ATP levels between attached and planktonic cells of Acidithiobacillus ferrooxidans growing with elemental sulfur. A small fraction of 3.7–14.4% of the bacterial cells was attached to the sulfur particles. The highest cell attachment of 14.4% was at the end of the lag phase, decreasing to 3.7% into the latter part of the active growth phase. Therefore, attached cells and their ATP content made a minor contribution to the total culture biomass in the active growth phase. However, the cellular ATP content was 1.01 amol per attached cell and 0.34 amol per planktonic cell. The significantly (P < 0.01) lower ATP content was attributed to sulfur limitation in the planktonic cells. These results suggest that a negligibly small subpopulation may be a link in cooperative interaction whereby sulfur oxidation by attached cells under boundary conditions provides bioavailable substrates to planktonic cells in the population.     

Construction of recombinant Escherichia coli for enhanced bioconversion of colchicine into 3-demethylated colchicine at 70 l bioreactor level

A recombinant strain of Escherichia coli with CYP102A1 gene was developed for the demethylation of colchicine into their derivatives. The CYP102A1 gene responsible for demethylation was isolated from Bacillus megaterium ACBT03 and amplified using suitable primers. The amplified product was cloned into pET28a+ expression vector using host E. coli BL21(DE3) cells. The CYP3A4 (product of CYP102A1 gene) protein expression and other parameters like substrate toxicity, product toxicity and enzyme activity were optimized in shake flasks; and further scaled-up to 5 l bioreactor with 3 l working volume. In 5 l bioreactor, dissolved oxygen (DO) was optimized for maximum specific growth and enhanced 3-demethylated colchicine (3-DMC) production. The optimized conditions from shake flasks were scaled-up to 70 l bioreactor and resulted into ∼80% conversion of 20 mM colchicine in 48 h with a volumetric productivity of 6.62 mg l⁻¹ h⁻¹. Scale-up factors were measured as volumetric oxygen transfer coefficient (k_La) i.e., 56 h⁻¹ and impeller tip velocity (V_tip) i.e., 7.065 m s⁻¹, respectively. The kinetic parameters K_m, k_cat, and k_cat/K_m of the CYP3A4 enzyme using colchicine as the substrate were determined to be 271 ± 30 μM, 8533 ± 25 min⁻¹, and 31.49 μM min⁻¹, respectively, when IPTG induced recombinant E. coli culture was used.     

Optimal conditions for enhanced β-mannanase production by recombinant Aspergillus sojae

Optimization of the growth conditions for maximum β-mannanase production in shake flasks by using recombinant Aspergillus sojae ATCC11906 (AsT1) was carried out by Box–Behnken design of response surface methodology. The highest β-mannanase activity on the fourth day of cultivation at 30 °C was obtained as 363 U/ml in the optimized medium consisting of 7% sugar beet molasses, 0.43% NH₄NO₃, 0.1% K₂HPO₄ and 0.05% MgSO₄ (by weight per volume) at 207 rpm. On the sixth day of cultivation under the optimized conditions, the highest β-mannanase activity was achieved as 482 U/ml which is 1.4-fold of 352 U/ml activity found on glucose medium previously.     

Alkaline lipase from a novel strain Burkholderia multivorans: Statistical medium optimization and production in a bioreactor

An alkaline lipase from Burkholderia multivorans was produced within 15 h of growth in a 14 L bioreactor. An overall 12-fold enhanced production (58 U mL⁻¹ and 36 U mg⁻¹ protein) was achieved after medium optimization following the “one-variable-at-a-time” and the statistical approaches. The optimal composition of the lipase production medium was determined to be (% w/v or v/v): KH₂PO₄ 0.1; K₂HPO₄ 0.3; NH₄Cl 0.5; MgSO₄·7H₂O 0.01; yeast extract 0.36; glucose 0.1; olive oil 3.0; CaCl₂ 0.4 mM; pH 7.0; inoculum density 3% (v/v) and incubation time 36 h in shake flasks. Lipase production was maximally influenced by olive oil/oleic acid as the inducer and yeast extract as the additive nitrogen. Plackett–Burman screening suggested catabolite repression by glucose. Amongst the divalent cations, Ca²⁺ was a positive signal while Mg²⁺ was a negative signal for lipase production. RSM predicted that incubation time, inoculum density and oil were required at their higher levels (36 h, 3% (v/v) and 3% (v/v), respectively) while glucose and yeast extract were required at their minimal levels for maximum lipase production in shake flasks. The production conditions were validated in a 14 L bioreactor where the incubation time was reduced to 15 h.     

Evaluation of cysteine ethyl ester as efficient inducer for glutathione overproduction in Saccharomyces spp.

Economical yeast based glutathione (GSH) production is a process that is influenced by several factors like raw material and production costs, biomass production and efficient biotransformation of adequate precursors into the final product GSH. Nowadays the usage of cysteine for the microbial conversion into GSH is industrial state of practice. In the following study, the potential of different inducers to increase the GSH content was evaluated by means of design of experiments methodology. Investigations were executed in three natural Saccharomyces strains, S. cerevisiae, S. bayanus and S. boulardii, in a well suited 50 ml shake tube system. Results of shake tube experiments were confirmed in traditional baffled shake flasks and finally via batch cultivation in lab-scale bioreactors under controlled conditions. Comprehensive studies showed that the usage of cysteine ethyl ester (CEE) for the batch-wise biotransformation into GSH led up to a more than 2.2 times higher yield compared to cysteine as inducer. Additionally, the intracellular GSH content could be significantly increased for all strains in terms of 2.29 ± 0.29% for cysteine to 3.65 ± 0.23% for CEE, respectively, in bioreactors. Thus, the usage of CEE provides a highly attractive inducing strategy for the GSH overproduction.     

In vitro penetration of swine oocytes by homologous spermatozoa: Distinct systems for gamete's co-incubation and oocyte's cryopreservation

In vitro penetration (IVP) of swine oocytes by homologous spermatozoa was evaluated in two experiments using four boars as semen donors. In experiment 1, the IVP rate and the number of penetrating spermatozoa (PSP) were compared using three co-incubation systems for vitrified oocytes and fresh sperm: (1) 35 mL petri dishes in a CO₂ incubator, (2) 35 mL petri dishes in bags (submarine system) and (3) glass flasks partially submerged in water bath with the same gas mixture used for the bag system. Mean PSP was 8.2 ± 10.1 and the IVP rate was 90.5%. The PSP differed across all systems (P = 0.0006): 15.5 ± 0.5 for flasks, 6.3 ± 0.4 for CO₂, and 3.9 ± 0.4 for bags. The IVP rate for flasks (95.0%) was greater (P = 0.01) than for CO₂ and bags (90.8% and 85.0%, respectively), but it did not differ between flasks and CO₂ for three boars (P > 0.05). In experiment 2, co-incubation was done as described for glass flasks in experiment 1. The IVP rate and PSP were compared for cryopreserved oocytes: either vitrified in open pulled straws (OPS), or frozen in cryotubes. Mean PSP was 5.4 ± 6.5 and IVP rate was 89.6%. Both PSP and IVP rate were greater (P < 0.0001) for oocytes frozen in cryotubes (7.0 ± 0.3% and 95.8%, respectively) than those frozen in OPS (3.7 ± 0.3% and 83.4%, respectively), with no differences found for three boars (P > 0.05). In summary, successful IVP of swine oocytes by homologous spermatozoa can be achieved using gametes incubated in glass flasks and oocytes frozen in cryotubes.     

Anthraquinones production in Rubia tinctorum cell suspension cultures: Down scale of shear effects

The effect of turbulence on suspended cells is one of the most complex problems in the scale-up of cell cultures. In the present paper, a direct comparison of the effects of turbulence on suspension cultures of Rubia tinctorum in a standard bioreactor and in shake flask cultures was done. A procedure derived from the well known global method proposed by Nishikawa et al. (1977) [39] was applied. Standard flasks and four-baffled shake flasks were used. The effect of turbulence and light irradiation on cell viability, biomass, and anthraquinones (AQs) production was evaluated. The biomass concentration and AQs production obtained using baffled shake flasks agitated at 360 rpm were similar to that achieved in R. tinctorum suspension cultures growing in a stirred tank bioreactor operating at 450 rpm, previously published (Busto et al., 2008 [17]). The effect of light on AQs production was found to be very significant, and a difference of up to 48% was found in cells with and without illumination after 7 days of culture. It is concluded that this down-scaled and simple flask culture system is a suitable and valid small scale instrument for the study of intracellular mechanisms of turbulence-induced AQs production in R. tinctorum suspension cultures.     

“Use of acidophilic bacteria of the genus Acidithiobacillus to biosynthesize CdS fluorescent nanoparticles (quantum dots) with high tolerance to acidic pH”

The use of bacterial cells to produce fluorescent semiconductor nanoparticles (quantum dots, QDs) represents a green alternative with promising economic potential. In the present work, we report for the first time the biosynthesis of CdS QDs by acidophilic bacteria of the Acidithiobacillus genus. CdS QDs were obtained by exposing A. ferrooxidans, A. thiooxidans and A. caldus cells to sublethal Cd²⁺ concentrations in the presence of cysteine and glutathione. The fluorescence of cadmium-exposed cells moves from green to red with incubation time, a characteristic property of QDs associated with nanocrystals growth. Biosynthesized nanoparticles (NPs) display an absorption peak at 360 nm and a broad emission spectra between 450 and 650 nm when excited at 370 nm, both characteristic of CdS QDs. Average sizes of 6 and 10 nm were determined for green and red NPs, respectively. The importance of cysteine and glutathione on QDs biosynthesis in Acidithiobacillus was related with the generation of H₂S. Interestingly, QDs produced by acidophilic bacteria display high tolerance to acidic pH. Absorbance and fluorescence properties of QDs was not affected at pH 2.0, a condition that totally inhibits the fluorescence of QDs produced chemically or biosynthesized by mesophilic bacteria (stable until pH 4.5–5.0). Results presented here constitute the first report of the generation of QDs with improved properties by using extremophile microorganisms.     

Synthesis,crystal structure,and DNA-binding properties of a new copper (II) complex containing mixed-ligands of 2,2′-bipyridine and p-methylbenzoate

A novel copper complex of [Cu(bpy)(pba)₂ · H₂O] · 0.5H₂O (bpy = 2,2′-bipyridine, pba = p-methylbenzoate) was synthesized. The interaction of the complex to native fish sperm DNA was investigated through electrochemistry, electronic absorption spectroscopy and viscosity experiments. In the X-ray crystallography structure, the copper (II) ion is coordinated by two oxygen atoms of two p-methylbenzoate groups, two nitrogen atoms of 2,2′-bipyridine and one water molecule. The observed changes in the physicochemical features of the copper (II) complex on binding to DNA suggested that the complex bind to DNA with intercalation mode via 2,2′-bipyridine ring into DNA base pairs. Electrochemical studies revealed that the complex prefer to bind to DNA in Cu(I) form rather than Cu(II) oxidation state form. Additionally, the nuclease activity of the title complex was assessed by gel electrophoresis assay and the results shown that the copper complex can cleave pBR322 DNA effectively in the presence of ascorbic acid.     

The role of volumetric power input in the growth,morphology, and production of a recombinant glycoprotein by Streptomyces lividans in shake flasks

The impact of flask geometry on Streptomyces lividans growth and morphology, production and O-mannosylation of a recombinant O-glycoprotein (APA from Mycobacterium tuberculosis) was described and associated to the evolution of the volumetric power input (P/V) in three shake flask geometries. During the exponential growth, the highest P/V was found in baffled flasks (BF) with 0.51 kW/m³, followed by coiled flasks (CF) with 0.44 kW/m³ and normal Erlenmeyer flasks (NF) with 0.20 kW/m³ (flasks volume of 250 mL, filling with 50 mL and agitated at 150 rpm). During the stationary phase, P/V decreased 20% in BF and CF, but increased two times in NF, surely due to changes in mycelial morphology and its effects on rheology. Also, NF cultures were carried out at a filling volume and agitation of 15 mL, 150 rpm (15 mL-NF), and 25 mL, 168 rpm (25 mL-NF), in order to raise P/V closely to the values obtained in CF. However, different growth, morphology and recombinant protein productivity were obtained. These data indicate that P/V is not a definitive parameter that can determine bacteria growth and morphology, not even glycoprotein production. But it can be proposed that the oxygen transfer in the center of the pellets and hydromechanical stress might be the more relevant parameters than P/V.     

The physical characterisation of a microscale parallel bioreactor platform with an industrial CHO cell line expressing an IgG4

There is a growing body of evidence that the ambr™ workstation from TAP Biosystems performs well in terms of helping to select appropriate clones for scale-up studies. Here we have investigated the physical characteristics of this microscale bioreactor system and found that these are quite different from those that exist in larger scale stirred bioreactors. For example, the flow regime in the ambr™ vessel is transitional rather than turbulent and the sparged air/oxygen superficial gas velocity is relatively very low whilst the specific power input is much higher (~400 W/m³) when compared to that used at larger scales (typically ~20 W/m³). This specific power input is necessary in order to achieve k_La values sufficiently high to satisfy the oxygen demand of the cells and control of dO₂. In line with other studies, we find that the culture of CHO cells in a 15 mL ambr™ bioreactor gave similar cell growth and productivity to that achieved in a 5 L stirred bioreactor whilst the results from shake flasks were significantly different. Given the differences in physical characteristics between the ambr™ and larger stirred bioreactors, we suggest that this similarity in biological performance is due to their similar control capabilities and the ‘equivalence of the stress parameters’ across the scales when compared with shake flasks.     

Bioleaching of chalcopyrite by pure and mixed cultures of Acidithiobacillus spp. and Leptospirillum ferriphilum

Bioleaching is an economical method for the recovery of metals that requires low investment and operation costs. Furthermore, it is generally more environmentally friendly than many physicochemical metal extraction processes. The bioleaching of chalcopyrite in shake flasks was investigated with pure and mixed cultures of Acidithiobacillus ferrooxidans, Acidithiobacillus thiooxidans, Acidithiobacillus caldus, and Leptospirillum ferriphilum. The mixed cultures containing both iron- and sulfur-oxidizing bacteria were more efficient than the pure culture alone. The presence of sulfur-oxidizing bacteria positively increased the dissolution rate and the percentage recovery of copper from chalcopyrite. Mixed cultures consisting of moderately thermophilic L. ferriphilum and A. caldus leached chalcopyrite more effectively than mesophilic A. ferrooxidans pure and mixed cultures. The decrease of the chalcopyrite dissolution rate in leaching systems containing A. ferrooxidans after 12–16 days coincided with the formation of jarosite precipitation as a passivation layer on the mineral surface during bioleaching. Low pH significantly reduces jarosite formation in pure and mixed cultures of L. ferriphilum and A. caldus.     

Growth tolerance of Zygomycetes Mucor indicus in orange peel hydrolysate without detoxification

The capability of two zygomycetes strains, Mucor indicus and an isolate from tempeh (Rhizopus sp.), to grow on orange peel hydrolysate and their tolerance to its antimicrobial activity, was investigated. Both fungi, in particular M. indicus, tolerated up to 2% d-limonene in semi-synthetic media during cultivation in shake flasks, under aerobic as well as anaerobic conditions. The tolerance of M. indicus was also tested in a bioreactor, giving rise to varying results in the presence of 2% limonene. Furthermore, both strains were capable of consuming galacturonic acid, the main monomer of pectin, under aerobic conditions when no other carbon source was present. The orange peel hydrolysate was based on 12% (dry w/v) orange peels, containing d-limonene at a concentration of 0.6% (v/v), which no other microorganism has been reported to be able to ferment. However, the hydrolysate was utilised by M. indicus under aerobic conditions, resulting in production of 410 and 400 mg ethanol/g hexoses and 57 and 75 mg fungal biomass/g sugars from cultivations in shake flasks and a bioreactor, respectively. Rhizopus sp., however, was slow to germinate aerobically, and neither of the zygomycetes was able to consistently germinate in orange peel hydrolysate, under anaerobic conditions. The zygomycetes strains used in the present study demonstrated a relatively high resistance to the antimicrobial compounds present in orange peel hydrolysate, and they were capable of producing ethanol and biomass in the presence of limonene, particularly when cultivated with air supply.     

Significance of Oxygen Supply in Jarosite Biosynthesis Promoted by Acidithiobacillus ferrooxidans

Jarosite [(Na⁺, K⁺, NH₄ ⁺, H₃O⁺)Fe₃(SO₄)₂(OH)₆] is an efficient scavenger for trace metals in Fe- and SO₄ ^2--rich acidic water. During the biosynthesis of jarosite promoted by Acidithiobacillus ferrooxidans, the continuous supply of high oxygen levels is a common practice that results in high costs. To evaluate the function of oxygen in jarosite production by A. ferrooxidans, three groups of batch experiments with different oxygen supply levels (i.e., loading volume percentages of FeSO₄ solution of 20%, 40%, and 70% v/v in the flasks), as well as three groups of sealed flask experiments with different limiting oxygen supply conditions (i.e., the solutions were not sealed at the initial stage of the ferrous oxidation reaction by paraffin but were rather sealed at the end of the ferrous oxidation reaction at 48 h), were tested. The formed Fe-precipitates were characterized via X-ray powder diffraction and scanning electron microscope-energy dispersive spectral analysis. The results showed that the biosynthesis of jarosite by A. ferrooxidans LX5 could be achieved at a wide range of solution loading volume percentages. The rate and efficiency of the jarosite biosynthesis were poorly correlated with the concentration of dissolved oxygen in the reaction solution. Similar jarosite precipitates, expressed as KFe₃ (SO₄) ₂(OH)₆ with Fe/S molar ratios between 1.61 and 1.68, were uniformly formed in unsealed and 48 h sealed flasks. These experimental results suggested that the supply of O₂ was only essential in the period of the oxidation of ferrous iron to ferric but was not required in the period of ferric precipitation.     

Bio-resolution of a chiral epoxide using whole cells of Bacillus megaterium ECU1001 in a biphasic system

Optically active epoxides can be prepared by kinetic resolution of racemic mixtures using stereospecific epoxide hydrolases. To increase the bio-resolution efficiency of a sparingly water-soluble epoxide (glycidyl phenyl ether, GPE), we investigated the use of organic/aqueous two-phase system. Various conditions were systematically examined and optimized in shake flasks. Isooctane was found to be the most suitable solvent as the organic phase. The phase volume ratio (ϕ_o/w) and biocatalyst concentration were shown to be sensitive parameters affecting both the reaction rate and the enzyme enantiospecificity in the biphase system. An isooctane/aqueous system was developed to overcome the low solubility and instability of GPE in the aqueous phase, resulting in a significant improvement of enatiomeric ratio (E-value) from 39.5 to 94.0 and an average productivity of 18.8 mg GPE/(h g) biocatalyst to 48.9 mg GPE/(h g) biocatalyst, respectively. Resolution of a 90.1 g/l solution of racemic glycidyl phenyl ether in isooctane phase was successfully carried out in a mechanically stirred reactor (120 ml), affording (S)-glycidyl phenyl ether in high (100%) enantiomeric excess with a yield of 44.5%.     

Statistical optimization of enzymatic degradation process for oil palm empty fruit bunch (OPEFB) in rotary drum bioreactor using crude cellulase produced from Aspergillus niger EFB1

Oil palm empty fruit bunch (OPEFB) was pretreated with 2% (v/v) HNO₃ and degraded by Aspergillus niger EFB1 crude cellulase. Through 2 Level Factorial Design (2LFD), it was found that OPEFB concentration, temperature, incubation time, concentration of Tween 80 and agitation speed have significant effect in reducing sugar production. A standard Response Surface Methodology (RSM) design known as Central Composite Design (CCD) was used to optimize the enzymatic degradation condition of OPEFB in rotary drum bioreactor. Reducing sugar level of 1.183 g/L was obtained with the following optimized degradation conditions: 1.95% (w/v) OPEFB, 0.5% (v/v) Tween 80, 55 °C, 87.5 rpm in the incubation period of 3 days and 16 h. The optimal degradation condition improved reducing sugar production by 1.07 fold compared to that before optimization in shake flasks culture. The optimization strategy of enzymatic degradation of OPEFB inside rotary drum bioreactor led to increase in glucose, xylose, arabinose, galactose and mannose production by 3, 2.5, 1.64, 19.37 and 22.52 fold, respectively. The improvement in reducing sugar and polyoses production were comparable with the reduction in OPEFB cellulose and hemicellulose content by 89.32% and 48.17% respectively after enzymatic degradation in optimized condition.     

Desarrollo de un bioadsorbente laminar con Phanerochaete chrysosporium hipertolerante al cadmio,al níquel y al plomo para el tratamiento de aguas

BackgroundThe use of basidiomycetes for metal removal is an alternative to traditional methods. In this, the biomass acts as a natural ionic exchanger removing metals from solution.ObjectiveTo develop a laminar biosorbent using a basidiomycete fungus resistant to high Cd, Ni and Pb concentrations.MethodsThe tolerance of Trametes versicolor, Pleurotus ostreatus and Phanerochaete chrysosporium was evaluated using increasing concentrations of the heavy metal salts, cadmium sulphate, lead acetate and nickel chloride. A biosorbent system was developed based on polyethylene sheets with a fungal biomass. It was evaluated in bubble columns using synthetic wastewater with the 3 metal salts at a rate of 300 mg/l. Finally, in a complementary experiment using shake flasks, the effect of a higher amount of biomass related to the metal removal efficiency was evaluated.ResultsP. chrysosporium strain was more tolerant to C₄H₆O₄Pb (10,000 mg/l), Cl₂Ni (300 mg/l) and CdSO₄·8H₂O (1,500 mg/l). In a reactor, under non-ligninolytic conditions, the fungus removed 69% of the chemical oxygen demand and produced enzymes such as LiP (0.01 U/l) and MnP (0.6 U/l.). An accumulation of metals in the wall was observed. By increasing the biomass to 1.6 (w/v), the metal biosorption was favored in the mixture (57% Pb, 74% Cd, and 98% Ni) and separately (95% Pb, 60% Cd, and 56% Ni). Competition between Ni and Pb by ligands of the wall was observed.ConclusionA novel laminar system based on P. chrysosporium viable biomass was developed. It has a large surface area and tolerance to high concentrations of Cd, Ni and Pb. It seems to be an alternative for the removal of metals from water.