Hydrodynamics and mass transfer in miniaturized bubble column bioreactors

Miniaturized bubble columns (MBCs) have different hydrodynamics in comparison with the larger ones, but there is a lack of scientific data on MBCs. Hence, in this study, the effect of gas hold-up, flow regimes, bubble size distribution on volumetric oxygen mass transfer coefficient at different pore size spargers and gas flow rates in MBCs in the presence and absence of microorganisms were investigated. It was found that flow regime transition occurred around low gas flow rates of 1.18 and 0.85 cm/s for small (16–40 µm) and large (40–100 µm) pore size spargers, respectively. Gas hold-up and K_La in MBC with small size sparger were higher than those with larger one, with an increasing effect in the presence of microorganisms. A comparison revealed that the wall effect on the flow regime and gas hold-up in MBCs was greater than bench-scale bubble columns. The K_La values significantly increased up to tenfold using small pore size sparger. In the MBC and stirred tank bioreactors, the maximum obtained cell concentrations were OD₆₀₀ of 41.5 and 43.0, respectively. Furthermore, it was shown that in MBCs, higher K_La and lower turbulency could be achieved at the end of bubbly flow regime.

     

Optimization of PEGylation Conditions for BSA Nanoparticles Using Response Surface Methodology

Chemical coupling of polyethylene glycol (PEG) to proteins or particles (PEGylation), prolongs their circulation half-life by greater than 50-fold, reduces their immunogenicity, and also promotes their accumulation in tumors due to enhanced permeability and retention effect. Herein, phase separation method was used to prepare bovine serum albumin (BSA) nanoparticles. PEGylation of BSA nanoparticles was performed by SPA activated mPEG through their free amino groups. Effect of process variables on PEGylation efficiency of BSA nanoparticles was investigated and optimized through response surface methodology with the amount of free amino groups as response. Optimum conditions was found to be 32.5 g/l of PEG concentration, PEG-nanoparticle incubation time of 10 min, incubation temperature of 27°C, and pH of 7 for 5 mg of BSA nanoparticles in 1 mL phosphate buffer. Analysis of data showed that PEG concentration had the most noticeable effect on the amount of PEGylated amino groups, but pH had the least. Mean diameter and zeta potential of PEGylated nanoparticles under these conditions were 217 nm and −14 mV, respectively. In conclusion, PEGylated nanoparticles demonstrated reduction of the negative surface charge compared to the non modified particles with the zeta potential of −31.7 mV. Drug release from PEGylated nanoparticles was almost slower than non-PEGylated ones, probably due to existence of a PEG layer around PEGylated particles which makes an extra resistance in opposition to drug diffusion.     

Continuous biodegradation of parathion by immobilized Sphingomonas sp. in magnetically fixed-bed bioreactors and evaluation of the enzyme stability of immobilized bacteria

Magnetically-modified Sphingomonas sp. was prepared using covalent binding of magnetic nanoparticles on to the cell surface. The magnetic modified bacteria were immobilized in the fixed-bed bioreactors (FBR) by internal and external magnetic fields for the biodetoxification of a model organophosphate, parathion: 93 % of substrate (50 mg parathion/l) was hydrolyzed at 0.5 ml/min in internal magnetic field fixed-bed bioreactor. The deactivation rate constants (at 1 ml/min) were 0.97 × 10^?3, 1.24 × 10^?3 and 4.17 × 10^?3 h^?1 for immobilized bacteria in external and internal magnetic field fixed-bed bioreactor and FBR, respectively. The deactivation rate constant for immobilized magnetically modified bacteria in external magnetic field fixed-bed bioreactor (EMFFBR) was 77 % lower than that of immobilized cells by entrapping method on porous basalt beads in FBR at 1 ml/min. Immobilized magnetic modified bacteria exhibited maximum enzyme stability in EMFFBR.     

Schizophyllan production by newly isolated fungus <Emphasis Type="Italic">Schizophyllum commune</Emphasis> IBRC-M 30213: optimization of culture medium using response surface methodology

Schizophyllan (SPG) is a commercially attractive biopolymer produced by Schizophyllum commune. An investigation on the potential for SPG production by Iranian native S. commune was conducted based on culture medium, fermentation conditions and bioreactor type, . Nine native fungal strains were isolated from the northern forest of Iran at different times. Based on growth rate and SPG production, one strain was selected for further study. Optimal medium composition and inoculum size for maximizing SPG production and minimizing biomass were determined using central composite design by setting sucrose, yeast extract, inoculum size, carboxymethyl cellulose and oleic acid in the ranges of 50–200 g/L, 1–4 g/L, 2–10%, 2–12 g/L and 0.032–0.222%, respectively. The results showed that optimal results were obtained at 93.47 g/L sucrose, 1.87 g/L yeast extract, 7.68% inoculum size, 9.07 g/L carboxymethyl cellulose and 0.13% oleic acid, with maximum SPG production of 9.97 g/L and minimum biomass of 35.18 g/L. Under these optimal conditions, the production of SPG was studied in stirred tank and bubble column bioreactors. The results revealed greater production in the stirred tank because of better mixing of the culture medium. The SPG produced was characterized using rheometery, Fourier transform infrared spectroscopy, nuclear magnetic resonance), scanning electron microscopy and gel permeation chromatography. The results of these characterizations demonstrated the similarity of the SPG produced by S. commune IBRC-M 30213 to commercial SPG. Thus, the SPG produced shows good potential as a polysaccharide for use in various industries.     

Effect of process variables on supercritical fluid disruption of Ralstonia eutropha cells for poly(R-hydroxybutyrate) recovery

This research focuses on the disruption of the gram-negative bacterium Ralstonia eutropha cells by supercritical CO2 for poly(R-hydroxybutyrate) (PHB) recovery. The variables affecting cell disruption such as drying strategy, type of modifier, and cultivation time, as well as operating pressure, temperature, and repeated release of supercritical CO2 pressure, have been studied. Effect of this disruption technique on PHB molecular mass was also investigated. PHB recovery was examined using a combination of this method and chemical pretreatments. For salt pretreatment, the cells were exposed to 140 mM NaCl and heat (60 degrees C, 1 h). The cells were also exposed to 0.2-0.8% (w/w) NaOH to examine the effect of alkaline pretreatment. Bacterial cells treated in growth phase exhibited less resistance to disruption than nutrient-limited cells in the stationary phase. It was also found that the wet cells could be utilized to recover PHB, but purity of the product was lower than that obtained from freeze-dried cells. Pretreatment with a minimum of 0.4% (w/w) NaOH was necessary to enable complete disruption with two times pressure release. Salt pretreatment was less effective; however, disruption was improved by the application of alkaline shock. The proposed method is economic and comparable with other recovery methods in terms of the percentage of PHB recovery and energy consumption, while it is environmentally more benign.     

Process parameters study of α-amylase production in a packed-bed bioreactor under solid-state fermentation with possibility of temperature monitoring

Production of α-amylase in a laboratory-scale packed-bed bioreactor by Bacillus sp. KR-8104 under solid-state fermentation (SSF) with possibility of temperature control and monitoring was studied using wheat bran (WB) as a solid substrate. The simultaneous effects of aeration rate, initial substrate moisture, and incubation temperature on α-amylase production were evaluated using response surface methodology (RSM) based on a Box-Behnken design. The optimum conditions for attaining the maximum production of α-amylase were 37°C, 72% (w/w) initial substrate moisture, and 0.15 L/min aeration. The average enzyme activity obtained under the optimized conditions was 473.8 U/g dry fermented substrate. In addition, it was observed that the production of enzyme decreased from the bottom of the bioreactor to the top.     

Effect of Arginine on Pre-nucleus Stage of Interferon Beta-1b Aggregation

Understanding the mechanism of aggregation of a therapeutic protein would not only ease the manufacturing processing but could also lead to a more stable finished product. Aggregation of recombinant interferon (IFNβ-1b) was studied by heating, oxidizing, or seeding of unformulated monomeric solution. The formation of aggregates was monitored by dynamic light scattering (DLS) and UV spectroscopy. The autocatalytic monomer loss model was used to fit the data on aggregation rates. The influence of pre-nucleation on aggregation step was demonstrated by inducing the liquid samples containing a monomer form of folded IFNβ-1b by heat and also an oxidizing agent. Results tend to suggest that the nucleus includes a single protein molecule which has been probably deformed. Seeding tests showed that aggregation of IFNβ-1b was probably initiated when 1.0% (w/w) of monomers converted to nucleus form. Chemiluminescence spectroscopy analysis of the sample indicated the generation of 3.0 μM of hydrogen peroxide (H₂O₂) during nucleation stage of IFNβ-1b aggregation. Arginine with a concentration of 200 mM was sufficient to suppress aggregation of IFNβ-1b by decreasing the rate of pre-nucleation step. We proposed the formation of pre-nucleus structures prior to nucleation as the mechanism of aggregation of IFNβ-1b. Furthermore, we have showed the positive anti-aggregation effect of arginine on pre-nucleation step.KEY WORDS: aggregation, arginine, interferon beta-1b, mechanism, pre-nucleus     

Extensive biodegradation of highly chlorinated biphenyl and Aroclor 1242 by Pseudomonas aeruginosa TMU56 isolated from contaminated soils

A bacterial strain, designated TMU56, was isolated from soil that had been contaminated with electrical transformer fluid (Askarel) for over 35 years. The isolate was identified as Pseudomonas aeruginosa using its 16S rDNA sequence. This strain was found to grow on monochlorobiphenyls (CBs), including 2-chlorobenzoic acid and 4-chlorobenzoic acid. It was also found to grow on 2,4-, 2,5-, 2,2′-, and 4,4′-diCB, as well as on a wide range of other xenobiotic compounds. This is the first reported representative of the genus Pseudomonas that is capable of growing on 2,4,4′-triCB, 2,2′,5,5′-tetraCB and 2,2′,4,4′,5,5′-hexaCB as sole carbon sources. Washed benzoate-grown cells were able to degrade 89% and 56% of 2,4-diCB and 2,2′,4,4′,5,5′-hexaCB, respectively. Gas chromatography analysis of individual congeners in Aroclor 1242 (200 ppm) following a 4-day incubation showed 73.3% degradation of PCBs without the need for biphenyl as an inducer. The strain exhibited no noticeable specificity for the percentage of congener transformation or degree of chlorination.