• Title/Summary/Keyword: Alginate beads

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The Differentiation of bone Marrow Stromal Cells into NP-like Cells through 3-Dimensional Co-culture System (3차원 Co-culture 시스템을 통한 BMSC의 NP-like Cell로의 분화)

  • Kim, D.H.;Kim, S.H.;Heo, S.J.;Shin, J.W.;Kim, Y.J.;Park, S.H.;Jun, J.W.;Shin, J.W.
    • Journal of Biomedical Engineering Research
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    • v.29 no.2
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    • pp.159-163
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    • 2008
  • The goal of this study is to investigate the effect and potential of three-dimensional Co-culture of BMSCs (bone marrow stromal Cells) and NP (nucleus pulposus) Cells on the differentiation of BMSCs into NP-like Cells. The NP Cells and BMSCs were isolated and cultured from New Zealand White rabbits. The isolated NP Cells and BMSCs were prepared in different alginate beads. Those two types of beads were separated by a track-etched membrane of $3\;{\mu}m$ pore in a 6-well culture plate. No growth factors were used. In addition to these, NP and BMSC were cultured in the beads independently for control. The number of Cells in Co-culturing system was half of those in two control groups. Proliferation and production of glycosaminoglycan (GAG) were evaluated along with histological observation. The GAG production rate(GAG contents/Cell) of Co-cultured BMSCs were much higher than that of BMSCs cultured alone. The total amounts of GAG produced by BMSCs in Co-culturing system were larger than those produced by BMSCs in control group and were comparable with those produced by NP alone even the number of each Cell was half of BMSCs in Co-culturing system. This study showed the potential of differentiation of BMSCs into NP-like Cells through three-dimensional Co-culture system even without any chemical agents.

Optimization of Screw Pumping System (SPS) for Mass Production of Entrapped Bifidus

  • Ryu, Ji-Sung;Lee, Yoon-Jong;Choi, Soo-Im;Lee, Jae-Won;Heo, Tae-Ryeon
    • Food Science and Biotechnology
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    • v.14 no.5
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    • pp.566-571
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    • 2005
  • Process of screw-pumping system (SPS) was optimized for mass production of encapsulated bifidus. SPS entrapment device was composed of feeding component, with optimized nozzle size and length of 18G (0.91 cm) and 4 mm, respectively, screw pump, and 37-multi-nozzle. Screw component had five wing turns [radius (r)=26 to 15 mm] from top to bottom of axis at 78-degree angle from middle of the screw, and two wings were positioned at screw edge to push materials toward nozzle. For nozzle component, 37 nozzles were attached to 20-mm round plate. Air compressor was attached to SPS to increase productivity of encapsulated bifidus. This system could be operated with highly viscous (more than 300 cp) materials, and productivity was higher than $1128\;{\pm}\;30\;beads/min$. Viability of encapsulated bifidus was $5.45\;{\times}\;10^8\;cfu$/bead, which is superior to that of encapsulated bifidus produced by other methods ($2.51{\times}10^8\;cfu$/bead). Average diameter of produced beads was $2.048\;{\pm}\;0.003\;mm$. Survival rate of SPS-produced encapsulated bifidus was 90% for Simulator of the Human Intestinal Microbial Ecosystem test and 88% in fermented milk (for 14 days). These results show SPS is effective for use in development of economical system for mass production of viable encapsulated bifidus.

Continuous Water Toxicity Monitoring Using Immobilized Photobacterium phosphoreum

  • Kim, Se-Kwon;Lee, Baek-Seok;Lee, Jeong-Gun;Seo, Hyung-Joon;Kim, Eun-Ki
    • Biotechnology and Bioprocess Engineering:BBE
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    • v.8 no.2
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    • pp.147-150
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    • 2003
  • Water toxicity monitoring based on the continuous cultivation of Photobacterium phorphoreum is presented. Normally, after 10 days of operation, a dark variant, which emits no light, appears and dominates the population, resulting in a rapid decrease in bioluminescence. Therefore, to overcome this problem, a fluidized-bed reactor is used in which alginate-immobilized cells are grown and leaking cells are continuously released into the effluent Experimental results revealed that the dominance of dark variants was suppressed inside the immobilized beads, thereby mitigating the rapid loss of bioluminescence. Plus, a high dilution rate (1.2 h$\^$-1/) prevented the occurrence of other microbial contamination in the reactor The concentration and bioluminescence of the released cells were sufficient to measure the water toxicity for more than 4 weeks.

Continuous Production of Gluconic Acid and Sorbitol from Glucose and Fructose using Perrneabilized cells of Zymomonas mobilis (투과화된 Zymomonas mobilis 균체를 이용한 Glucose와 Fructose로 부터 Gluconic Acid와 Sorbitol의 생산)

  • 김원준;박제균;김학성
    • Microbiology and Biotechnology Letters
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    • v.19 no.1
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    • pp.70-75
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    • 1991
  • Continuous and simultaneous production of gluconic acid and sorbitol from glucose and fructose was carried out by using glucose-fructose oxidoreductase and glucanolactonase of Zymomonas mobilis. In order to utilize the enzymes without purification, Zymomonas mobilis was permeabilized with toluene. Optimum conditions for permeabilization and reaction kinetics of permeabilized Zymomonas mobilis were studied. In batch operation with the permeabilized cells immobilized in alginate beads, about 90% conversion was obtained within 35 h reaction. Continuous production of gluconic acid and sorbitol using the immobilized permeabilized cells was carried out. Optimum conditions for continuous operation with the imn~obilized cells were; pH 6.2 and temperature $40^{\circ}C$. Maximum productivities for gluconic acid and sorbitol were about 14.5 g/l/h and 14.8 g/l/h respectively at the dilution rate of 0.075 $h^{-1}$ when 300 g/l each of substrates was fed.

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Citric Acid Production by Succharomycopsis lipolytica in Air-lift and Membrane Recycle Bioreactors (기포탑 및 막 재순환 생물반응기에서의 Saccharomycopsis lipolytica에 의한 구연산 생산)

  • 조대철;정봉현;장호남
    • Microbiology and Biotechnology Letters
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    • v.17 no.6
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    • pp.624-628
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    • 1989
  • A study on the citric acid production using Saccharomycopsis lipolytica (NRRL Y7576) was carried out in shake-flasks, air-lift and membrane recycle bioreactors. The cells entrapped in Ca-alginate beads were used in shake-flasks and air-lift reactor. Repeated batch fermentation in shake-flasks was successfully performed for 34 days and resulted in a yield of 54%. Increased yield (63%) was obtained in the air-lift reactor operation using nitrogen deficient medium (NDM). In the membrane recycle bioreactor operation, the maximal dry cell mass concentration was 39 g/1 at a dilution rate of 0.02 h$^{-1}$ and the yield with NDM was higher than that with growth medium. In addition, the yield and volumetric productivity with pure oxygen supply were greatly improved compared with those with air supply.

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Cryopreservation of Zygotic Embryos of Herbaceous Peony (Paeonia lactiflora Pall.) by Encapsulation-Dehydration

  • Kim Hyun-Mi;Shin Jong-Hee;Sohn Jea-Keun
    • KOREAN JOURNAL OF CROP SCIENCE
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    • v.49 no.4
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    • pp.354-357
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    • 2004
  • A simplified technique which cryoprotects zygotic embryos by encapsulation-dehydration was developed for the germplasm conservation of herbaceous peony (Paeonia lactiflora Pall.). The highest survival rate $(85\%)$ was obtained from embryos treated by encapsulation-dehydration. The zygotic embryos were precultured on MS medium containing 0.3mg/L $GA_3$ for 1 day. The precultured embryos were encapsulated in $3\%$ (w/v) alginate beads and immersed for 1 h in MS medium containing 2 M glycerol and 0.5 M sucrose. The encapsulated embryos were dehydrated for 5h by air drying prior to direct immersion in liquid nitrogen. This encapsulation-dehydration method appears to be a promising technique for germplasm cryopreservation of a herbaceous peony.

Semicontinuous Production of Blud Pigment from Gardenia Fruit by Immobilized Cells of Bacillus subtilis KS-380 Using Air Bubble Column Reactor (Air Bubble Column Reactor를 이용하여 Bacillus Subtilis KS-380의 고정화에 의한 치자로부터 청색 색소의 생산)

  • 류병호;조경자
    • Journal of the Korean Society of Food Science and Nutrition
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    • v.19 no.5
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    • pp.395-402
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    • 1990
  • The semicontinuous production of blue pigment from gardenia fruit by immobilized cells of Bacillus subtilis KS-380 which excreted $\beta$-glucosidase was investigated in comparison with free cells, . The blue pigment produced higher productivity under the conditions of aeration of 0.2m$\ell$/min and 2mm diameter of gel beads by using 3.5% sodium alginate. Semicontinuous production by immobilized cell showed the highest productivity with replacement of fresh production medium in every 24hr for fourth fermentation cycle following the conditions of blue pigment productivity.

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Ethanol Production from Lactose by Immobilized Reactor System Using a Fusant Yeast Strain of Saccharomyces cerevisiae and Kluyveromyces fragilis

  • Lee, Chu-Hee;Bang, Jeong-Hee;Hyun, Nam-Doo
    • Korean Journal of Microbiology
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    • v.30 no.5
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    • pp.355-359
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    • 1992
  • Yeast cells of a fusant strain constructed by protoplast fusion of Saccharomyces cerevisiae and Kluyveromyces frugilis were immobilized on calcium alginate beads. The increment of the ethanol tolerance of this strain to 8.0%, when compared with the parent K, fragilis, was confirmed. Based on the results from jar fermentation, a packed-bed reactor of theh immobilized yeast cells was operated. The optimal performance of the immobilized yeast reactor for ethanol production was achieved when supplying 10% lactose (suplemented 1.0% yeast extract) at a temperature of 30.deg.C. The maximal ethanol productivity was obtained as 13.3 g/I/hr at a dilution rate of $0.76 hr^{-1}$.

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Nitrogen removal performance of anammox process with PVA-SA gel bead crosslinked with sodium sulfate as a biomass carrier

  • Tuyen, N.V.;Ryu, J.H.;Yae, J.B.;Kim, H.G.;Hong, S.W.;Ahn, D.H.
    • Journal of Industrial and Engineering Chemistry
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    • v.67
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    • pp.326-332
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    • 2018
  • In this study,the result shows that polyvinyl alcohol-sodium alginate (PVA-SA) gel bead crosslinked with sodium sulfate are better among the different methods by comparing the relative mechanical strength, mechanical strength swelling and expansion coefficient of beads in water. Subsequently, anammox biomass entrapment by PVA-SA gel was introduced into continuous stirred tank reactor (CSTR). After 24 operation days, the nitrogen removal efficiency achieved 60%, while the nitrogen loading rate (NLR) was $0.14kgN/m^3/d$ and the experiment data indicated that PVA-SA gel bead crosslinked with sodium sulfate can be used to initiate anammox process. Furthermore, it is an alternative for culturing anammox in a long-term operation.