Young-Jung Wee

The statistically optimized production of poly(γ-glutamic acid) by batch fermentation of a newly isolated Bacillus subtilis RKY3

For the production of poly(gamma-glutamic acid), a newly isolated Bacillus sp. RKY3 was phylogenetically identified as Bacillus subtilis based on its 16S rRNA gene sequence. The culture medium for the production of poly(gamma-glutamic acid) by B. subtilis RKY3 was optimized statistically. The parameters significantly affecting poly(gamma-glutamic acid) production were found to be glycerol, glutamic acid, yeast extract, and K(2)HPO(4). A further advanced statistical approach, central composite design, found the optimum levels of the screened variables as follows (gl(-1)): glycerol 17.6, glutamic acid 59.6; yeast extract 2.7; K(2)HPO(4) 2.3. The predicted response as poly(gamma-glutamic acid) production under the statistically optimized conditions was 48.5 g l(-1), which was only 0.4% different from the maximum poly(gamma-glutamic acid) concentration (48.7 g l(-1)) observed at the validation experiment using 7-l lab-scale fermentor containing 3 l of working volume.

Microwave-Assisted Synthesis of Diverse Pyrrolo[3,4-c]quinoline-1,3-diones and Their Antibacterial Activities

With the aim of developing a general and practical method for library production, a novel and efficient two-phase microwave-assisted cascade reaction between isatins and β-ketoamides in [Bmim]BF4/toluene was developed for the synthesis of pyrrolo[3,4-c]quinoline-1,3-diones. The features of this methodology are, the use of microwave-assisted rapid synthesis, mild reaction conditions, high yields, operational simplicity, facile product separation, and recyclability. Furthermore, the antibacterial activities of the pyrrolo[3,4-c]quinoline-1,3-dione derivatives produced were evaluated against Gram-negative bacteria (Escherichia coli, Pseudomonas aeruginosa, and Enterobacter aerogenes) and Gram-positive bacteria (Bacillus cereus and Staphylococcus aureus). These derivatives showed antibacterial activities against Gram-positive strains that were at least equivalent to that against Gram-negative strains. Compound 7{3,5} displayed the most potent antibacterial activity against P. aeruginosa (MIC = 0.5 μg/mL) and greater activity than standard ampicillin (MIC = 1 μg/mL). Compound 7{4,7} exhibited the best inhibitory activity against E. coli and E. aerogenes (MIC = 1 and 0.5 μg/mL), compared with the standard ampicillin (both MICs = 1 μg/mL). The synthesized pyrrolo[3,4-c]quinoline-1,3-diones are expected to be widely used as lead compounds for the development of new antibacterial agents.

Effect of fermentation inhibitors in the presence and absence of activated charcoal on the growth of Saccharomyces cerevisiae

The acidic hydrolysis of biomass generates numerous inhibitors of fermentation, which adversely affect cell growth and metabolism. The goal of the present study was to determine the effects of fermentation inhibitors on growth and glucose consumption by Saccharomyces cerevisiae. We also conducted in situ adsorption during cell cultivation in synthetic broth containing fermentation inhibitors. In order to evaluate the effect of in situ adsorption on cell growth, five inhibitors, namely 5-hydroxymethylfurfural, levulinic acid, furfural, formic acid, and acetic acid, were introduced into synthetic broth. The existence of fermentation inhibitors during cell culture adversely affects cell growth and sugar consumption. Furfural, formic acid, and acetic acid were the most potent inhibitors in our culture system. The in situ adsorption of inhibitors by the addition of activated charcoal to the synthetic broth increased cell growth and sugar consumption. Our results indicate that detoxification of fermentation media by in situ adsorption may be useful for enhancing biofuel production.

l-Lactic acid production by combined utilization of agricultural bioresources as renewable and economical substrates through batch and repeated-batch fermentation of Enterococcus faecalis RKY1

Enterococcus faecalis RKY1 was used to produce l-lactic acid from hydrol, soybean curd residues (SCR), and malt. Hydrol was efficiently metabolized to l-lactic acid with optical purity of >97.5%, though hydrol contained mixed sugars such as glucose, maltose, maltotriose, and maltodextrin. Combined utilization of hydrol, SCR, and malt was enough to sustain lactic acid fermentation by E. faecalis RKY1. In order to reduce the amount of nitrogen sources and product inhibition, cell-recycle repeated-batch fermentation was employed, where a high cell mass (26.3g/L) was obtained. Lactic acid productivity was improved by removal of lactic acid from fermentation broth by membrane filtration and by linearly increased cell density. When the total of 10 repeated-batch fermentations were carried out using 100g/L hydrol, 150g/L SCR hydrolyzate, and 20g/L malt hydrolyzate as the main nutrients, lactic acid productivity was increased significantly from 3.20g/L/h to 6.37g/L/h.

Synthesis of novel and diverse mollugin analogues and their antibacterial and antioxidant activities

Novel and diverse mollugin analogues (1-12) were synthesized using PhB(OH)2/AcOH-mediated electrocyclization reaction as a key step. The newly synthesized compounds were screened for antioxidant and antibacterial activities. Compounds 1, 2, 5, 6, 8, and 10-12 showed high antioxidant activities in DPPH inhibition (IC50=0.52-1.11 μM) compared with BHT (IC50=9.67 μM). Compounds 3 exhibited potent antibacterial activity against Staphylococcus aureus (KCTC-1916) bacterial strain at 100 μg/mL. Structures of newly synthesized compounds were confirmed by IR, (1)H NMR, (13)C NMR data and high-resolution mass spectrometry.

Influence of operating parameters on concentration and purification of L -lactic acid using electrodialysis

An experimental investigation was presented to determine the optimum configuration of influential parameters (concentrate volume, flow rate, temperature, initial lactate concentration, voltage, and impurities) for the best performance. AMX-CMX ion-exchange membranes were used in all experiments. Temperature was found to possess an important role in the increase of lactate recovery, and it was not increased to high values due to membrane destruction. When the higher voltage was applied to electrodialyzer, the better performance of electrodialysis was observed due to enhancement of the driving force. It was found that, to achieve an optimum operating condition, feed volume, concentrate volume, flow rate, temperature, initial lactate concentration in concentrate, and voltage should be 2 L, 1 L, 0.8 L/min, 32°C, 1 g/L, and 15.0 V, respectively. Under these optimized conditions, 97% of lactate was successfully recovered from the fermentation broth, where the lactate flux and energy cost were 7.2 ± 0.6 moles/m2/h and 0.25 kWh/kg, respectively. The results of experiments indicate that the lactic acid in the fermentation broth can be economically purified by electrodialysis.

Enhanced production of extracellular proteolytic enzyme excreted by a newly isolated Bacillus subtilis FBL-1 through combined utilization of statistical designs and response surface methodology

An extracellular protease producing strain FBL-1 was newly isolated from soil, and it was identified as Bacillus subtilis through 16S rDNA sequence analysis. B. subtilis FBL-1 was used for extracellular protease production, and culture conditions were optimized by statistical methods. Three statistical approaches such as Plackett–Burman design, steepest ascent path analysis, and Box–Behnken design were successfully combined to optimize protease production, which resulted in significant enhancement of production. Through Plackett–Burman experimental design, fructose and yeast extract were screened as the significant components for the production of extracellular protease. The center points of each parameter were predetermined by the steepest ascent method. Based on the results obtained by Box–Behnken experimental design, the optimized level of significant parameters for protease production was determined by multiple regression analysis. The optimized levels of parameters were fructose 32.42 g L−1, yeast extract 15.02 g L−1, and incubation time 35.78 h. Protease activity predicted by the quadratic model developed in this work was 578.55 U mL−1, which was only 2.67% different from the experimental protease activity obtained by verification studies. The protease activity was significantly enhanced by 7.0-fold compared with the activity obtained from basal medium.

Homofermentative production of optically pure l-lactic acid from sucrose and mixed sugars by batch fermentation of Enterococcus faecalis RKY1

In the present study, lactic acid fermentation was carried out by batch culture of Enterococcus faecalis RKY1 using sucrose and mixed sugars as the major substrate. Maximum lactic acid productivity (5.2 g/L/h) was recorded when 50 and 100 g/L of sucrose were used as a carbon source. Sucrose concentration higher than 150 g/L resulted in the decrease of lactic acid productivity due to inhibition by high substrate concentration, but lactic acid productivity was remained > 3.0 g/L/h until the sucrose used for lactic acid fermentation increased up to 150 g/L. L-Lactic acid content of the total lactic acid produced from sucrose and mixed sugars was higher than 98%. When the fermentation media contained sucrose, the kinetic parameters showing specific rates such as μ, qS, and qP were relatively lower than those of fermentation using glucose as a sole carbon source, which might be due to additional time requirement to induce invertase enzyme for utilization of sucrose. There was no carbon catabolite repression observed when the sugar mixtures containing sucrose, glucose, and/ or fructose were used as a carbon source for lactic acid fermentation by E. faecalis RKY1.

Purification and characterization of microbial protease produced extracellularly from Bacillus subtilis FBL-1

An ammonium sulfate precipitation of fermentation broth produced by Bacillus subtilis FBL-1 resulted in 2.9-fold increase of specific protease activity. An eluted protein fraction from the column chromatographies using DEAE-Cellulose and Sephadex G-75 had 94.2- and 94.9-fold higher specific protease activity, respectively. An SDS-PAGE revealed a band of purified protease at approximately 37.6 kDa. Although purified protease showed the highest activity at 45°C and pH 9.0, the activity remained stable in temperature range from 30 to 50°C and pH range from 7.0 to 9.0. Protease activity was activated by metal ions such as Ca2+, Mg2+, Mn2+, Fe2+, Ca2+ and K+, but 10 mM Fe3+ significantly inhibited enzyme activity (53%). Protease activity was inhibited by 2 mM EDTA as a metalloprotease inhibitor, but it showed good stability against surfactants and organic solvents. The preferred substrates for protease activity were found to be casein (100%) and soybean flour (71.6%).

Enzymatic synthesis of chlorogenic acid glucoside using dextransucrase and its physical and functional properties

Chlorogenic acid, a major polyphenol in edible plants, possesses strong antioxidant activity, anti-lipid peroxidation and anticancer effects. It used for industrial applications; however, this is limited by its instability to heat or light. In this study, we for the first time synthesized chlorogenic acid glucoside (CHG) via transglycosylation using dextransucrase from Leuconostoc mesenteroides and sucrose. CHG was purified and its structure determined by nuclear magnetic resonance and matrix-associated laser desorption ionization-time-of-flight mass spectroscopy. The production yield of CHG was 44.0% or 141mM, as determined by response surface methodology. CHG possessed a 65% increased water solubility and 2-fold browning resistance while it displayed stronger inhibition of lipid peroxidation and of colon cancer cell growth by MTT assay, compared to chlorogenic acid. Therefore, this study may expand the industrial applications of chlorogenic acid as water-soluble or browning resistant compound (CHG) through enzymatic glycosylation.