• Title/Summary/Keyword: Calcium alginate bead

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Enhancement of Growth and Secondary Metabolite Biosynthesis: Effect of Elicitors Derived from Plants and Insects

  • Jeong Gwi-Taek;Park Don-Hee
    • Biotechnology and Bioprocess Engineering:BBE
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    • v.10 no.1
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    • pp.73-77
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    • 2005
  • Plant-derived natural products have been and will continue to be valuable sources. Elicitors have been employed to modify cell metabolism in order to enhance the productivity of useful metabolites in plant cell/tissue cultures. In this study, several elicitors were used to improve the productivity of useful metabolites and to reduce culture time for archiving high concentration in P. ginseng hairy root cultures. The addition of chitosan, chitosan oligosaccharide and alginate oligosaccharide to the culture of P. ginseng hairy roots caused growth to be inhibited with the increase in elicitor concentration. The usage of the chitosan elicitor and D-glucosamine caused a slight decrease in hairy root growth, whereas total ginseng saponin accumulated slightly with the increase in elicitor concentration. When gel beads were added to the culture medium at the initial period, hairy root growth was enhanced. The maximum growth was 1.35 times higher than that of the control at $1\%$ (w/v). Total ginseng saponin content decreased due to the addition of alginate beads. This would result in consistent diffusion of lower levels of calcium ions during the culture period that promotes biomass growth.

High Cell Density Cultivation of Bifidobacterium longum Using a Calcium Carbonate-Alginate Beads System

  • Yu, Won-Kyu;Kim, Ji-Youn;Lee, Ki-Yong;Heo, Tae-Ryeon
    • Journal of Microbiology and Biotechnology
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    • v.12 no.3
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    • pp.444-448
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    • 2002
  • A $CaCO_3$-alginate beads system was developed for high cell density cultivation of Bifidobacterium longum and the cost-effective media were also screened. In batch process with $CaCO_3$, beads, two strains of B. longum showed both the highest viable cells and optical density in TPY medium, resulting in maximum optical density and viable cell counts of 12.40, $2.22{\times}10^10$ cfu/ml for B. longum ATCC 15707 and 13.71, $3.93{\times}10^10$ cfu/ml for B. longum HLC 3742. Released size distribution, according to $CaCO_3$-alginate bead size preparation, was smaller than others. These results were also examined by observing their morphology. The skim milk-based medium was most adequate to cultivate B. longum as the cheapest medium, and $10\%$ skim milk supplemented with $2\%$ glucose and $1\%$ yeast extract was a suitable medium, supporting the growth to $5.57{\times}10^10$ cfu/ml for ATCC 15707 and $6.82{\times}10^9$ cfu/ml for HLC 3742. During the long-term storage at $4^{\circ}C\;and\;-20{\circ}C$, B. longum cultivated with $CaCO_3$ beads had the highest stability. Consequently, $CaCO_3$-alginate beads buffer was found to be useful not only to cultivate B. longum but also to preserve cultures.

Release Properties of BSA from Pectin Heads for Colonic Drug Delivery (Colonic Delivery를 위한 펙틴 비드로부터 BSA의 방출 특성)

  • 최춘순;박상무;송원현;이창문;이기영;김동운;김진철
    • KSBB Journal
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    • v.18 no.2
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    • pp.161-164
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    • 2003
  • Oral drug delivery system using pectin gel was developed for colon-targeting of peptide drug. BSA(bovine serum albumin)-loaded pectin and pectin-alginate beads were prepared for drug release properties in vitro. Morphological studies by electron microscopy indicated that pectin and pectin-alginate beads were spherical in shape and approximately 1.0 mm. In order to find the suitable beads, effects of cross-linking agents (calcium chloride or zinc acetate) and drying temperature of beads were investigated. Drug release decreased with concentration of cross-linking agents and drying temperature. For colonic drug delivery from pectin and pectin-alginate beads, pectin degradable enzymes were added at 5 hrs from the beginning of drug release. After addition of enzymes, drug release was suddenly increased against free enzymes. Therefore, pectin and pectin-alginate beads can be promised as useful drug release carriers for colon-targeted delivery.

Performance Comparison of Continuous Reactors for Bioethanol Production Based on Glycerol (글리세롤 기반의 바이오에탄올 생산을 위한 연속생산반응기의 성능 비교)

  • Lee, Sang-Jun;Song, Yoon-Seok;Kim, Sung-Bong;Kang, Sung-Woo;Han, Sung-Ok;Park, Chul-Hwan;Kim, Seung-Wook
    • KSBB Journal
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    • v.26 no.4
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    • pp.328-332
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    • 2011
  • Ethanol production using glycerol as a carbon source was performed by Enterobacter aerogenes immobilized on calcium alginate beads. To improve the ethanol production, the optimal conditions such as loading amount of immobilized cells and glycerol concentration were investigated. The optimal loading amount of immobilized cells and glycerol concentration were 10 mL of calcium alginate bead and 10 g/L, respectively. Consequently, glycerol consumption rate, ethanol concentration and yield were 0.32 g/$L{\cdot}h$, 3.38 g/L and 0.43 g/g on the batch production, respectively. Continuous production of ethanol was successfully achieved using two types of immobilized cell reactors (continuous stirred tank reactor and packed bed reactor) from 10 g/L of glycerol. In the continuous stirred tank reactor, glycerol consumption, ethanol concentration, specific productivity and yield were 9.8 g, 4.67 g/L, 1.17 g/$L{\cdot}h$, 0.48 g/g, respectively. The concentration of produced ethanol was 38-44% higher comparison to batch fermentation, and continuous stirred tank reactor showed better performance than packed bed reactor.

Microbial Removal Using Layered Double Hydroxides and Iron (Hydr)oxides Immobilized on Granular Media

  • Park, Jeong-Ann;Lee, Chang-Gu;Park, Seong-Jik;Kim, Jae-Hyeon;Kim, Song-Bae
    • Environmental Engineering Research
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    • v.15 no.3
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    • pp.149-156
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    • 2010
  • The objective of this study was to investigate microbial removal using layered double hydroxides (LDHs) and iron (hydr)oxides (IHs) immobilized onto granular media. Column experiments were performed using calcium alginate beads (CA beads), LDHs entrapped in CA beads (LDH beads), quartz sand (QS), iron hydroxide-coated sand (IHCS) and hematite-coated sand (HCS). Microbial breakthrough curves were obtained by monitoring the effluent, with the percentage of microbial removal and collector efficiency then quantified from these curves. The results showed that the LDH beads were ineffective for the removal of the negatively-charged microbes (27.7% at 1 mM solution), even though the positively-charged LDHs were contained on the beads. The above could be related to the immobilization method, where LDH powders were immobilized inside CA beads with nano-sized pores (about 10 nm); therefore, micro-sized microbes (E. coli = 1.21 ${\mu}m$) could not diffuse through the pores to come into contact with the LDHs in the beads, but adhere only to the exterior surface of the beads via polymeric interaction. IHCS was the most effective in the microbial removal (86.0% at 1 mM solution), which could be attributed to the iron hydroxide coated onto the exterior surface of QS had a positive surface charge and, therefore, effectively attracted the negatively-charged microbes via electrostatic interactions. Meanwhile, HCS was far less effective (35.6% at 1 mM solution) than IHCS because the hematite coated onto the external surface of QS is a crystallized iron oxide with a negative surface charge. This study has helped to improve our knowledge on the potential application of functional granular media for microbial removal.

Production of casein phosphopeptides using Streptococcus faecalis var. liquefaciens cell immobilization (Streptococcus faecalis var. liquefaciens 전세포 고정화법을 이용한 Casein Phosphopeptides 생산)

  • Lee, Ki-Sung;Shin, Jae-Yoon;Jang, Yi-Hyun;Kweon, Dae-Hyuk;Park, Ki-Moon;Jin, Yong-Su
    • KSBB Journal
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    • v.23 no.1
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    • pp.59-64
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    • 2008
  • Optimum conditions for production of casein phosphopeptides (CPP) from sodium casenate by immobilized cell culture of Streptococcus faecalis var. liquefaciens were investigated. Immobilized cells were made by mixing 60% sodium alginate solution with an equal volume of culture broth at the end of exponential phase and subsequently dropping the mixture into $CaCl_{2}$ solution. Optimum conditions for CPP production by the immobilized cells were the same as those ($50^{\circ}C$, pH 7.0, and 10% substrate concentration) by the crude enzyme solution from the supernatant of culture broth. Optimum loading volume of the immobilized cells into a batch reactor was 30% (w/v). Using a continuous reactor loaded by the immobilized cells under the identified optimal conditions, we were able to produce CPP continuously up to 30 days with a maximum CPP conversion efficiency of 20%.